Cover

Tools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)

CLOSE THIS BOOKTools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)
VIEW THE DOCUMENT(introduction...)
VIEW THE DOCUMENTAcknowledgements
VIEW THE DOCUMENTPreface
VIEW THE DOCUMENTGuide to the user
VIEW THE DOCUMENTIntroduction
A. Analysis
VIEW THE DOCUMENTA.1. Definition
VIEW THE DOCUMENTA.2. Initial conditions and problem areas
Technical Chapter 1: Analysis
VIEW THE DOCUMENT1.1 Blow pipe assaying
VIEW THE DOCUMENT1.2 Pycnometer
VIEW THE DOCUMENT1.3 Manual magnetic separator by Dr A. Wilke
VIEW THE DOCUMENT1.4 Quick-test-strips merckoquant
VIEW THE DOCUMENT1.5 Rifflebox
B. Underground mining
VIEW THE DOCUMENTB.1. Definition
VIEW THE DOCUMENTB.2. Existing situation and problem areas
VIEW THE DOCUMENTB.3. Organizational measures
VIEW THE DOCUMENTB.4 Environmental and health aspects
Technical Chapter 2: Safety Techniques
VIEW THE DOCUMENT(introduction...)
VIEW THE DOCUMENT2.1 Safety kit
Technical Chapter 3: Ventilation
VIEW THE DOCUMENT3.1 Bricked brattice, bricked duct
VIEW THE DOCUMENT3.2 Small blowers, manual fans
VIEW THE DOCUMENT3.3 Air-jet ventilator
VIEW THE DOCUMENT3.4 Hydro-compressor
VIEW THE DOCUMENT3.5 Ventilation oven
VIEW THE DOCUMENT3.6 Wind sail
VIEW THE DOCUMENT3.7 Box blower
VIEW THE DOCUMENT3.8 Bell blower baaders blower
Technical Chapter 4: Water supply and drainage
VIEW THE DOCUMENT4.1 Pneumatic positive-displacement pump
VIEW THE DOCUMENT4.2 Chinese liberation pump
VIEW THE DOCUMENT4.3 Water bag
VIEW THE DOCUMENT4.4 Bucket-chain conveyor
VIEW THE DOCUMENT4.5 Pneumatic high-pressure pump
Technical Chapter 5: Support
VIEW THE DOCUMENT5.1 Rigid support in drifts and stopes
VIEW THE DOCUMENT5.2 Single mechanical prop
VIEW THE DOCUMENT5.3 Hydraulic prop support
VIEW THE DOCUMENT5.4 Rock bolts, rods, rock stabilizers
Technical Chapter 6: Lighting
VIEW THE DOCUMENT6.1 Underground lighting equipment
Technical Chapter 7: Stoping
VIEW THE DOCUMENT7.1 Pneumatic jack hammer, drilling stand, jackleg
VIEW THE DOCUMENT7.2 Gasoline hammer drill
VIEW THE DOCUMENT7.3 Wedge ram
VIEW THE DOCUMENT7.4 Electric hammer drill with stand Y D Z
VIEW THE DOCUMENT7.5 Manual mining methods
VIEW THE DOCUMENT7.6 Pneumatic charging machine for explosives
Technical Chapter 8: Loading
VIEW THE DOCUMENT8.1 Mucking sheet
VIEW THE DOCUMENT8.2 Hand scraper and tray
VIEW THE DOCUMENT8.3 Scraper loader
VIEW THE DOCUMENT8.4 Pneumatic overhead loader
VIEW THE DOCUMENT8.5 Chute, charging hopper
Technical Chapter 9: Hauling
VIEW THE DOCUMENT9.1 Manual winch
VIEW THE DOCUMENT9.2 Motor cars as hauling machines, depth indicators
VIEW THE DOCUMENT9.3 Block and pulley
VIEW THE DOCUMENT9.4 Trackless and track bound haulage
VIEW THE DOCUMENT9.5 Passenger lifting moving ladder
C. Surface mining
VIEW THE DOCUMENTC.1. Definition
VIEW THE DOCUMENTC.2. Initial conditions and problem areas
VIEW THE DOCUMENTC.3. Factors related to environment and health
VIEW THE DOCUMENTC.4. Pit and quarry industry
Technical Chapter 10: Surface Mining Equipment
VIEW THE DOCUMENT(introduction...)
VIEW THE DOCUMENT10.1 Aerial cable-way by gravity
VIEW THE DOCUMENT10.2 Cable tool drill
VIEW THE DOCUMENT10.3 Suction dredge
VIEW THE DOCUMENT10.4 Hydram, hydraulic ram pump, rife ram
VIEW THE DOCUMENT10.5 Noria
VIEW THE DOCUMENT10.6 Tyre pump
VIEW THE DOCUMENT10.7 Archimedian screw
VIEW THE DOCUMENT10.8 Boat mill
VIEW THE DOCUMENT10.9 Hydraulic mining gravel pump mining
Technical Chapter 11: Other special techniques
VIEW THE DOCUMENT11.1 Welding additives
VIEW THE DOCUMENT11.2 Rubber tanks, flexible tanks
VIEW THE DOCUMENT11.3 BY-Pass oil filters, by-pass micro-filters
VIEW THE DOCUMENT11.4 Eccentric motor, vibrator, shaker
D. Beneficiation
VIEW THE DOCUMENTD.1. Definition
VIEW THE DOCUMENTD.2. Initial conditions and problem areas
VIEW THE DOCUMENTD.3. Proposals for procedural and organizational solutions
VIEW THE DOCUMENTD.4. Environmental and health aspects
VIEW THE DOCUMENTD.5. Processing of diamonds
VIEW THE DOCUMENTD.6. Gold beneficiation processing
VIEW THE DOCUMENTD.7 The processing of phosphate-containing raw-minerals into p-fertilizers
Technical Chapter 12: Crushing
VIEW THE DOCUMENT(introduction...)
VIEW THE DOCUMENT12.1 Jaw crusher, jaw breaker
VIEW THE DOCUMENT12.2 Roll crusher, roll grinder
VIEW THE DOCUMENT12.3 Ball mill
VIEW THE DOCUMENT12.4 Stamp mill, hammer mill
VIEW THE DOCUMENT12.5 Chilean mill edge mill, roller mill
VIEW THE DOCUMENT12.6 ''See-saw'' crusher, ''rocker'' crusher
Technical Chapter 13: Classification
VIEW THE DOCUMENT13.1 Set of rigid screens
VIEW THE DOCUMENT13.2 Screen riddle, vibrating screen
VIEW THE DOCUMENT13.3 Cantilever grizzly
VIEW THE DOCUMENT13.4 Sizing drum, classifying drum
VIEW THE DOCUMENT13.5 Cone classifier
VIEW THE DOCUMENT13.6 Countercurrent hydraulic classifier
VIEW THE DOCUMENT13.7 Hydro-cyclone
VIEW THE DOCUMENT13.8 Log washer, spiral classifier
VIEW THE DOCUMENT13.9 Rake classifier
VIEW THE DOCUMENT13.10 Sluice, sluice box, washing sluice
Technical Chapter 14: Sorting
VIEW THE DOCUMENT14.1 Jig screen, hand-jigging
VIEW THE DOCUMENT14.2 Simple hand jig, moving bed(percussion) jig
VIEW THE DOCUMENT14.3 Hand piston jig
VIEW THE DOCUMENT14.4 Piston jig, ''harzer'' jig
VIEW THE DOCUMENT14.5 Pulsator classifier pan american jig
VIEW THE DOCUMENT14.6 Sluices with or without linings/insets, long tom
VIEW THE DOCUMENT14.7 Ground sluice
VIEW THE DOCUMENT14.8 Pinched sluice, fanned sluice
VIEW THE DOCUMENT14.9 Air separator, dry blower
VIEW THE DOCUMENT14.10 Settling basin, buddle
VIEW THE DOCUMENT14.11 Circular buddle
VIEW THE DOCUMENT14.12 Dolly tub
VIEW THE DOCUMENT14.13 Bumping table, concussion table
VIEW THE DOCUMENT14.14 Racking table, tilting frame
VIEW THE DOCUMENT14.15 Sweeping table, belt table
VIEW THE DOCUMENT14.16 Vibrating table
VIEW THE DOCUMENT14.17 Humphrey's spiral, spiral separator
VIEW THE DOCUMENT14.18 Spiral concentrator
Technical Chapter 15: Gold Benefication
VIEW THE DOCUMENT15.1 Amalgam press
VIEW THE DOCUMENT15.2 Amalgamating table
VIEW THE DOCUMENT15.3 Amalgamating barrel
VIEW THE DOCUMENT15.4 Rocker, cradle
VIEW THE DOCUMENT15.5 Mechanized, compact gold processor
VIEW THE DOCUMENT15.6 Hydraulic gold trap
VIEW THE DOCUMENT15.7 Retort for, amalgam
VIEW THE DOCUMENT15.8 Centrifugal separator
VIEW THE DOCUMENT15.9 Gold pan, batea
VIEW THE DOCUMENT15.10 Jigs with jig bed, russel jig
VIEW THE DOCUMENT15.11 Gold leaching
VIEW THE DOCUMENT15.12 Gold separation by smelting
VIEW THE DOCUMENT15.13 Gold-coal-agglomeration
Technical Chapter 16: 0ther Sorting and Separating Techniques
VIEW THE DOCUMENT16.1 Roasting oven, calcining furnace
VIEW THE DOCUMENT16.2 Salt gardens, salt works, salterns
VIEW THE DOCUMENT16.3 Sulfur production in heap smelting or chamber ovens
VIEW THE DOCUMENT16.4 Autoclaves for extracting sulfur
VIEW THE DOCUMENT16.5 Copper sulfate plant
VIEW THE DOCUMENT16.6 Electrostatic sorting
VIEW THE DOCUMENT16.7 Flotation
Technical Chapter 17: Drying
VIEW THE DOCUMENT17.1 Drying oven
VIEW THE DOCUMENT17.2 Solar houses
VIEW THE DOCUMENT17.3 Drying areas, drying surfaces
Technical Chapter 18: Clarification
VIEW THE DOCUMENT18.1 Thickener
VIEW THE DOCUMENT18.2 Lamella-thickener
VIEW THE DOCUMENT18.3 Continuous (rake) thickener
E. Mechanization and energy supply
VIEW THE DOCUMENTE.1. Introduction
VIEW THE DOCUMENTE.2. Energy source
VIEW THE DOCUMENTE.3. Drive unit
VIEW THE DOCUMENTE.4. Energy conversion
VIEW THE DOCUMENTE.5. Distribution of energy
VIEW THE DOCUMENTE.6. Energy systems
VIEW THE DOCUMENTE.7. Aspects of mechanization in mining
VIEW THE DOCUMENTE.8. Environmental and health aspects
Technical Chapter 19: Energy Techniques
VIEW THE DOCUMENT(introduction...)
VIEW THE DOCUMENT19.1 Bicycle drive pedal drive
VIEW THE DOCUMENT19.2 Animal-powered whim
VIEW THE DOCUMENT19.3 Water balance
VIEW THE DOCUMENT19.4 Wind generator
VIEW THE DOCUMENT19.5 Savonius rotor
VIEW THE DOCUMENT19.6 Water wheel
VIEW THE DOCUMENT19.7 Horizontal water wheel
VIEW THE DOCUMENT19.8 Rope turbine
VIEW THE DOCUMENT19.9 Solar cells
VIEW THE DOCUMENT19.10 Solar collector (solar thermal)
VIEW THE DOCUMENT19.11 Water turbine
VIEW THE DOCUMENT19.12 Internal combustion engine
VIEW THE DOCUMENTBibliography
VIEW THE DOCUMENTList of manufacturers and suppliers
VIEW THE DOCUMENTList of abbreviations
CLOSE THIS BOOKTools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)
VIEW THE DOCUMENT(introduction...)
VIEW THE DOCUMENTAcknowledgements
VIEW THE DOCUMENTPreface
VIEW THE DOCUMENTGuide to the user
VIEW THE DOCUMENTIntroduction
A. Analysis
Technical Chapter 1: Analysis
B. Underground mining
Technical Chapter 2: Safety Techniques
Technical Chapter 3: Ventilation
Technical Chapter 4: Water supply and drainage
Technical Chapter 5: Support
Technical Chapter 6: Lighting
Technical Chapter 7: Stoping
Technical Chapter 8: Loading
Technical Chapter 9: Hauling
C. Surface mining
Technical Chapter 10: Surface Mining Equipment
Technical Chapter 11: Other special techniques
D. Beneficiation
Technical Chapter 12: Crushing
Technical Chapter 13: Classification
Technical Chapter 14: Sorting
Technical Chapter 15: Gold Benefication
Technical Chapter 16: 0ther Sorting and Separating Techniques
Technical Chapter 17: Drying
Technical Chapter 18: Clarification
E. Mechanization and energy supply
Technical Chapter 19: Energy Techniques
VIEW THE DOCUMENTBibliography
VIEW THE DOCUMENTList of manufacturers and suppliers
VIEW THE DOCUMENTList of abbreviations

Techniques and processes for Small Scale Mining
by Michael Priester, Thomas Hentschel, Bernd Benthin

A Publication of the Deutsches Zentrum f�r Entwicklungstechnologien - GATE A division of the Deutsche Gesellschaft f�r Technische Zusammenarbeit (GTZ) GmbH - 1993

The authors:

Dr.-Ing. Michael Priester, mining engineer, has accumulated very extensive experience in small-scale mining and mining/environment in developing countries in such commodities as zinc, tungsten, lead-silver, antimony, coal, diamonds and gold. He is a specialist in traditional techniques for exploitation and beneficiation, exploration projects, assistance and education.

Dipl.-Geogr. Thomas Hentschel has gained extensive experience in small-scale mining in Latin America. He is specialized in economic and energy aspects, transport infrastructure and environmental aspects.

Dipl.-Econ. Bernd Benthin specialized in social-economic and historical-technical aspects os small-scale mining. He as well as the afore mentioned belongs to the team of Projekt-Consult, Beratung in Entwicklungsl�ndern GmbH.

Front cover:
Humphrey’s spiral for the concentration of tin ores in Kalauyo Mine near La Paz, Bolivia

Die Deutsche Bibliothek - CIP-Einheitsaufnahme

Priester, Michael:
Tools for mining: techniques and processes for small scale mining; a publication of Deutsches Zentrum f�r Entwicklungstechnologien - GATE, a division of the Deutsche Gesellschaft f�r Technische Zusammenarbeit (GTZ) GmbH /
Michael Priester; Thomas Hentschel; Bernd Benthin. -
Braunschweig; Wiesbaden: Vieweg, 1993
ISBN 3-528-02007-6
NE: Hentschel, Thomas:; Benthin, Bernd:

The author’s opinion does not necessarily represent the view of the publisher.

All rights reserved
© Deutsche Gesellschaft f�r Technische Zusammenarbeit (GTZ) GmbH, Eschborn 1993
Published by Friedr. Vieweg & Sohn Verlagsgesellschaft mbH, Braunschweig
Vieweg is a subsidiary company of the Bertelsmann Publishing Group International.
Printed in /germany by Lengericher Handelsdruckerei, Lengerich
ISBN 3-528-02007-6

CLOSE THIS BOOKTools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)
VIEW THE DOCUMENT(introduction...)
VIEW THE DOCUMENTAcknowledgements
VIEW THE DOCUMENTPreface
VIEW THE DOCUMENTGuide to the user
VIEW THE DOCUMENTIntroduction
A. Analysis
Technical Chapter 1: Analysis
B. Underground mining
Technical Chapter 2: Safety Techniques
Technical Chapter 3: Ventilation
Technical Chapter 4: Water supply and drainage
Technical Chapter 5: Support
Technical Chapter 6: Lighting
Technical Chapter 7: Stoping
Technical Chapter 8: Loading
Technical Chapter 9: Hauling
C. Surface mining
Technical Chapter 10: Surface Mining Equipment
Technical Chapter 11: Other special techniques
D. Beneficiation
Technical Chapter 12: Crushing
Technical Chapter 13: Classification
Technical Chapter 14: Sorting
Technical Chapter 15: Gold Benefication
Technical Chapter 16: 0ther Sorting and Separating Techniques
Technical Chapter 17: Drying
Technical Chapter 18: Clarification
E. Mechanization and energy supply
Technical Chapter 19: Energy Techniques
VIEW THE DOCUMENTBibliography
VIEW THE DOCUMENTList of manufacturers and suppliers
VIEW THE DOCUMENTList of abbreviations

Acknowledgements

Deutsches Zentrum f�r Entwicklungstechnologien- GATE

Deutsches Zentrum f�r Entwicklungstechnologien - GATE - stands for German Appropriate Technology Exchange. It was founded in 1978 as a special division of the Deutsche Gesellschaft fur Technische Zusammenarbeit (GTZ) GmbH. GATE is a centre for the dissemination and promotion of appropriate technologies for developing countries. GATE defines “Appropriate technologies” as those which are suitable and acceptable in the light of economic, social and cultural criteria. They should contribute to socio-economic development whilst ensuring optimal utilization of resources and minimal detriment to the environment. Depending on the case at hand a traditional, intermediate or highly-developed can be the “appropriate" one. GATE focusses its work on the key areas:

- Dissemination of Appropriate Technologies: Collecting, processing and disseminating information on technologies appropriate to the needs of the developing countries: ascertaining the technological requirements of Third World countries: support in the form of personnel, material and equipment to promote the development and adaptation of technologies for developing countries.

- Environmental Protection. The growing importance of ecology and environmental protection require better coordination and harmonization of projects. In order to tackle these tasks more effectively, a coordination center was set up within GATE in 1985.

GATE has entered into cooperation agreements with a number of technology centres in Third World countries.

GATE offers a free information service on appropriate technologies for all public and private development institutions in developing countries, dealing with the development, adaptation, introduction and application of technologies.

Deutsche Gesellschaft fur Technische Zusammenarbeit (GTZ) GmbH

The government-owned GTZ operates in the field of Technical Cooperation. 2200 German experts are working together with partners from about 100 countries of Africa, Asia and Latin America in projects covering practically every sector of agriculture, forestry, economic development, social services and institutional and material infrastructure. - The GTZ is commissioned to do this work both by the Government of the Federal Republic of Germany and by other government or semi-government authorities.

The GTZ activities encompass:

- appraisal, technical planning, control and supervision of technical cooperation projects commissioned by the Government of the Federal Republic or by other authorities

- providing an advisory service to other agencies also working on development projects

- the recruitment, selection, briefing, assignment, administration of expert personnel and their welfare and technical backstopping during their period of assignment

- provision of materials and equipment for projects, planning work, selection, purchasing and shipment to the developing countries

- management of all financial obligations to the partner-country.

Deutsches Zentrum fur Entwicklungstechnologien - GATE
in: Deutsche Gesellschaft fur Technische Zusammenarbeit (GTZ) GmbH
P. O. Box 5180
D-65726 Eschborn
Federal Republic of Germany
Tel.: (06196) 79-0
Telex: 41523-0 gtz d
Fax: (06196) 797352

CLOSE THIS BOOKTools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)
VIEW THE DOCUMENT(introduction...)
VIEW THE DOCUMENTAcknowledgements
VIEW THE DOCUMENTPreface
VIEW THE DOCUMENTGuide to the user
VIEW THE DOCUMENTIntroduction
A. Analysis
Technical Chapter 1: Analysis
B. Underground mining
Technical Chapter 2: Safety Techniques
Technical Chapter 3: Ventilation
Technical Chapter 4: Water supply and drainage
Technical Chapter 5: Support
Technical Chapter 6: Lighting
Technical Chapter 7: Stoping
Technical Chapter 8: Loading
Technical Chapter 9: Hauling
C. Surface mining
Technical Chapter 10: Surface Mining Equipment
Technical Chapter 11: Other special techniques
D. Beneficiation
Technical Chapter 12: Crushing
Technical Chapter 13: Classification
Technical Chapter 14: Sorting
Technical Chapter 15: Gold Benefication
Technical Chapter 16: 0ther Sorting and Separating Techniques
Technical Chapter 17: Drying
Technical Chapter 18: Clarification
E. Mechanization and energy supply
Technical Chapter 19: Energy Techniques
VIEW THE DOCUMENTBibliography
VIEW THE DOCUMENTList of manufacturers and suppliers
VIEW THE DOCUMENTList of abbreviations

Preface

This technical handbook on small-scale mining in developing countries is the result of a supra-regional Technical Cooperation project conducted by the Federal Republic of Germany. The objective of the project was to develop needs-oriented technologies by reviewing existing technical and economic documentation on process problems and their solutions. This analysis, which focuses by way of example on the Andean states, has been conducted by Projekt-Consult GmbH on behalf of the Deutsche Gesellschaft fur Technische Zusammenarbeit (GTZ) GmbH.

The contents of the publication “Tools for Mining" were presented to the participants of a seminar on small-scale mining held for SADC countries in Livingstone, Zambia, in February 1991, and it immediately became evident that the problems of smallscale mining in Africa and the Far East do not differ substantially from those encountered in the Andean countries. First published in Spanish, the interest shown in an English edition was such that the GTZ decided to publish an English-language version.

For many people in the Andean states of Latin America, small-scale mining is the mainstay of their income. The small mines, most of which employ less than ten persons, operate under exceptionally hard conditions. Indeed, their manual techniques are reminiscent of engineering in Europe prior to the industrial revolution. The low productivity level leads to extremely low wages, often poor safety conditions and social problems. In addition, small-scale mining frequently causes serious environmental pollution.

This publication aims to provide smallscale miners with technical alternatives. These technical innovations are intended as a comprehensive approach to the problems of small-scale mining, endeavouring as they do to improve the microeconomic, macroeconomic, social and ecological outputs. The handbook deals with analysis, mining activities, beneficiation and energy, and contains hints on technical issues and work organisation. It also includes information about historical mining machinery - which is comprehensively documented in Central Europe - modern, small-scale mining equipment and traditional techniques. By merging historical, modern and traditional elements, a basis is generated for developing appropriate technology in line with actual needs. Although only limited documentation was available concerning locally developed, traditional techniques in the small-scale mining sector in Africa and Asia, the handbook is nonetheless suitable for global use as the techniques described can be implemented everywhere, thus making a major contribution to technology transfer and innovations in small-scale mining outside Latin America too.

The strategy of local production and implementation of socio-culturally, economically and ecologically appropriate technology on which this handbook is based has already proven its feasibility and its worth many a time in the field.

CLOSE THIS BOOKTools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)
VIEW THE DOCUMENT(introduction...)
VIEW THE DOCUMENTAcknowledgements
VIEW THE DOCUMENTPreface
VIEW THE DOCUMENTGuide to the user
VIEW THE DOCUMENTIntroduction
A. Analysis
Technical Chapter 1: Analysis
B. Underground mining
Technical Chapter 2: Safety Techniques
Technical Chapter 3: Ventilation
Technical Chapter 4: Water supply and drainage
Technical Chapter 5: Support
Technical Chapter 6: Lighting
Technical Chapter 7: Stoping
Technical Chapter 8: Loading
Technical Chapter 9: Hauling
C. Surface mining
Technical Chapter 10: Surface Mining Equipment
Technical Chapter 11: Other special techniques
D. Beneficiation
Technical Chapter 12: Crushing
Technical Chapter 13: Classification
Technical Chapter 14: Sorting
Technical Chapter 15: Gold Benefication
Technical Chapter 16: 0ther Sorting and Separating Techniques
Technical Chapter 17: Drying
Technical Chapter 18: Clarification
E. Mechanization and energy supply
Technical Chapter 19: Energy Techniques
VIEW THE DOCUMENTBibliography
VIEW THE DOCUMENTList of manufacturers and suppliers
VIEW THE DOCUMENTList of abbreviations

Guide to the user

This technical handbook on small-scale mining in developing countries serves as a general source of information and as a planning and consulting guide for mining, exploration and beneficiation engineers as well as other technical-staff members of planning and consulting companies and organizations both in developing and in developed countries. Although the handbook caters to the special needs of small-scale mining in Latin American countries, incorporating particularly the traditional techniques employed in countries in the Andean region, it has a worldwide application. Included in this handbook are also guidelines for craftsmen and artisans and their affiliated consulting organizations who are interested in diversifying their product line.

Prerequisites for the successful application of this handbook include a technical knowledge on the part of the reader, as well as the ability to think abstractly and the capability to understand and interpret technical sketches and drawings.

Due to the large quantity of information which has emerged from the complex array of mining activities, a structuring of the data is crucial to ensure the convenient use of the handbook. The handbook covers all basic information about mining, in particular focusing on the extraction and beneficiation of ores, precious metals, coal, salt, industrial minerals, and precious stones. Since the selection of mining and processing equipment relies more upon specific operational data, such as production rate and the degree of mechanization, rather than the type of mineral being extracted, the information given in this handbook is divided into five main chapters according to the following five categories: Analysis, Underground Mining, Surface Mining, Beneficiation and Energy.

Each of these five chapters includes an introduction containing definitions, problem areas, environmental and health risks, and organizational advice. This is followed by a presentation of technical information on individual techniques and procedures, which in some cases is divided into specific work categories. Each of these techniques is summarized in a technical outline containing a compact presentation of the technical data, costs, and conditions and restrictions of application. Especially with regard to the conditions for application, the evaluation of these techniques is based on more subjective criteria; for example, service and maintenance costs can only be approximated in a small-scale mining handbook through comparison with costs for equipment which perform comparable functions. As a result, these evaluations cannot be universally correlated with each other.

The degree of environmental impact is presented on a linear scale, providing an initial basis for defining the technology's effect on the environment. Negative environmental effects through the depletion of mineral resources, or those associated with the supplying of energy, were not taken into consideration here; these effects are discussed in the chapter on Energy. Those techniques that are energy intensive and cannot utilize regenerative sources of energy are included in the environmental impact evaluation. Damage to the environment caused by the manufacture of spare parts for mining equipment are not considered here unless the production pertains to major machinery components. The environmental material-balance sheet for reagents has, however, been incorporated into the data analysis for the most part.

The section on suitability for local production examines the possibilities for manufacturing at the local level. The investigation does not focus on manufacturing by the mines directly, but rather production in non-mining industries such as wood, metal and other special machine-manufacturing shops which, due to the fact that they do not belong to the mining sector, are not equipped with special machines or special knowledge in the manufacture of such mining equipment. Besides providing information on the local conditions required for machine manufacturers, the handbook also includes photos, drawings and simple dimensioning aids. Every technical outline has a numbered title and name of the technique or technology, mining sector and work category, enabling rapid identification and classification of the technique or technology according to its area of application.

The technical section of the handbook also includes names of manufacturers and bibliography for further information. Abbreviations used in the handbook are explained in the List of Abbreviations.

A Subject Index is provided at the end of the handbook to assist the reader in quickly locating particular text subjects within the work-organization and technical sections.

Those mineral resources which require special mining or processing techniques are presented in the handbook separately:

- industrial minerals extraction in the chapter on Surface Mining, since this primarily involves the mining of bulk materials. The techniques presented in Chapter D are suitable for the processing of raw materials for industrial and construction purposes, and can normally be used without difficulty.

- techniques for diamond processing are presented in Chapter D, whereby sorting of raw materials is the main difficulty since in some cases the feed material contains significantly less than 1 g/ton valuable mineral.

- gold beneficiation is also contained in the section on beneficiation and processing. This additionally includes information concerning the problems and risks of contamination in the amalgamation process as well as a collection of flowsheets from various gold-processing plants. Special separation techniques for gold extraction are described in Subchapter 15. Crushing, classification and some sorting processes employed in gold beneficiation are not gold-specific techniques and are therefore found in a beneficiation of the handbook. The mining of gold, whether surface or underground, likewise does not need to be addressed separately.

Some of the described modern techniques for smallscale mining are under patent protection in case of local production. The valid legal requirements must be considered.

CLOSE THIS BOOKTools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)
VIEW THE DOCUMENT(introduction...)
VIEW THE DOCUMENTAcknowledgements
VIEW THE DOCUMENTPreface
VIEW THE DOCUMENTGuide to the user
VIEW THE DOCUMENTIntroduction
A. Analysis
Technical Chapter 1: Analysis
B. Underground mining
Technical Chapter 2: Safety Techniques
Technical Chapter 3: Ventilation
Technical Chapter 4: Water supply and drainage
Technical Chapter 5: Support
Technical Chapter 6: Lighting
Technical Chapter 7: Stoping
Technical Chapter 8: Loading
Technical Chapter 9: Hauling
C. Surface mining
Technical Chapter 10: Surface Mining Equipment
Technical Chapter 11: Other special techniques
D. Beneficiation
Technical Chapter 12: Crushing
Technical Chapter 13: Classification
Technical Chapter 14: Sorting
Technical Chapter 15: Gold Benefication
Technical Chapter 16: 0ther Sorting and Separating Techniques
Technical Chapter 17: Drying
Technical Chapter 18: Clarification
E. Mechanization and energy supply
Technical Chapter 19: Energy Techniques
VIEW THE DOCUMENTBibliography
VIEW THE DOCUMENTList of manufacturers and suppliers
VIEW THE DOCUMENTList of abbreviations

Introduction

The role of small-scale mining worldwide, both in developed and developing countries, should not be underestimated. It must be taken into consideration that the definition "small-scale mining" varies greatly from country to country. The criteria used here are cost of investment (less than 1,000,000- US$), number of employees (up to 100 employees), crude ore production rate (less than 100,000 t/a), annual sales, size of the mining concession, amount of reserves, or a combination of these individual criteria. These criteria are still under discussion, and uniform guidelines based on objective criteria have not yet been established.

Consequently small-scale mining in developing countries is defined by subjective criteria, some of which characterize this sector as a craft-activity:

- the absence or low degree of mechanization due to a high proportion of heavy manual labor,

- low safety standards,

- poorly-trained personnel,

- lack of technical personnel in the plant, resulting in deficient planning in both mining and processing activities,

- comparatively poor utilization of resources due to nonselective mining of high-grade ores and poor recovery,

- low pay scale,

- low work productivity,

- periods of non-continuous mining, as a result of mining only seasonally or when world market prices reach a certain minimum level,

- insufficient consideration of environmental impact

- chronic lack of capital,

- some illegal operations due to mining without concession rights.

In general, the situation in small-scale mining can be characterized as a vicious circle that, without external assistance, can hardly be broken:


Figure

Despite the difficult conditions that beset small-scale mining, the industry holds a substantial position in mining worldwide. Of the total world mining production, a considerable proportion is accounted for by small-scale mining.

Table: Precentage of Total World Production of Selected Raw Materials/Minerals represented by Small-Scale Mining (Source: Noetstaller)

Metals

Industrial minerals

beryllium

100 %

iron

12 %

fluorite

90 %

barite

60 %

mercury

90 %

lead

11 %

graphite

90 %

sand and gravel

30 %

tungsten

80 %

zinc

11 %

talc

90 %

stones for building

30 %

chrome

50 %

cobalt

10 %

vermiculite

90 %

salt

20 %

antimony

45 %

gold

10 %

pumice

90 %

coal

20 %

manganese

18 %

silver

10 %

feldespar

80 %

asbestos

10 %

tin

15 %

copper

8 %

clay

75 %

phosphate

10 %


gypsum

70 %


For many developing countries throughout the world, small-scale mining provides an important source of income as well as a significant source of foreign monetary exchange.

Table: The Most Important Small-Scale Mining Countries and Coresponding Minerals Processed (Source: Noetstaller)

Country

Raw Material mined by Small-Scale Mining

Latin America


Argentine

antimony, asbestos, beryl, lithium, mercury, bismuth, tungsten

Bolivia

antimony, lead, gold, sulphur, silver, tungsten, zinc, tin

Brazil

beryl, chromite, gold, precious stones, titanium, tin

Chile

barite, lead, gold, copper, manganese, mercury, sulphur, coal

Dominican Republic

gold

Guatemala

antimony, lead, mica, manganese, tin, tungsten

Colombia

antimony, lead, chromite, precious stones, iron, gold, coal, platinum mercury, zinc,

Cuba

copper, manganese, pyrite

Mexico

fluorite, mercury, sulphur, uranium, tin

Peru

antimony, lead, diatomite, gold, copper, manganese, molybdenum, silver, bismuth, zinc, tin

Venezuela

asbestos, diamonds, gold

Ecuador

gold

Asia


Myanmar

antimony, manganese, tin, tungsten

China

antimony, iron, coal, tin, tungsten

India

barite, borates, iron, mica, coal, manganese, tin

Indonesia

gold, tin

Iran

barite, lead, copper, zinc

Malaysia

gold, iron, manganese, zinc, tin, tungsten

Papua-New Guinea

gold

Philippines

chromite, gold, coal, copper, silver, zinc

Thailand

antimony, tin, tungsten

Turkey

lead, chromite, copper, magnesite, mercury, zinc

Africa


Algeria

antimony, barite, diatomite, mercury, zinc

Ethiopia

gold, manganese, platinum

Gabon

gold

Ghana

diamonds, gold

Kenya

beryl, precious stones, gold, copper, silver

Lesotho

diamonds

Liberia

diamonds, gold

Madagaskar

gold, rare earth, bismuth

Morocco

antimony, barite, lead, manganese, zinc, tin

Nigeria

asbestos, barite, lead, gold, zinc, tin

Rwanda

beryl, gold, tin, tungsten

Sierra Leone

diamonds

Tunesia

lead, mercury, zinc

Tanzania

diamonds, mica, gold, magnesite, precious stones, tin, tungsten

Uganda

beryl, bismuth, tungsten

Central African Rep.

diamonds, gold

Zimbabwe

antimony, beryl, chromite, precious stones, mica, gold, copper, lithium, manganese, silver

Small-scale mining activities and mine workers have an integral interrelationship with their surroundings -nature, culture and people, technology and economy: mining disturbs nature through the depletion of its natural resources and its deleterious impact on the environment, which it is dependent upon for its energy and raw materials. Mining on the one hand, and culture and people on the other, have greatly influenced each other since prehistoric times: mining activities provided culturally significant metals and precious stones; mining has always, still to this day, led the way for rural and technological development. Mining, with its tools and equipment, utilizes this technology to generate income through the materials it produces. This interrelationship can be depicted as follows:


Figure

A comprehensive promotion of small-scale mining must consider the social suitability, assessed needs, profitability and environmental compatibility; only then can subsequent improvements in the working conditions of small-scale miners be achieved. In particular, the following measures are essential:

Table: Catalogue of possible Promotion Measures for the various Stages of Production


On-site technical and organizational consultation

Research and development

Policy on raw materials

Exploration

Training in:
- analysis
- deposit geology and mineralogy
- geological mapping

Development of appropriate:
- methods of analysis
- instrument kits

National assistance through:
- regional exploration programs
- providing suitable maps
- service facilities
- reducing bureaucratic requirements

Mining, Exploitation

Training in organization and implementation of:
- exploration activities
- safety measures
- mining operation
- mecanization
- training in the operation of machines

Development of appropriate:
- mining methods and equipment
- haulage facilities
- safety procedures
- ventilation methods

Implementation of:
- security and health control
- technical advice
Devising a social security system for small-scale mining

Beneficiation

Training in:
- operation of machines
- planning, operation, optimization and supervision of beneficiation plants
- water management
- handling/treatment of chemicals which are hazardous to health and the environment

Development of appropriate:
- crushing and grinding equipment
- beneficiation techniques and machines for small-scale mining, e.g.:

- mobile systems
- heap leaching
- flotation
- mechanization of equipment

- analysis of concentrates

Promotion and construction of:
- central processing plants
- infrastructure for
- transportation
- water source facilities

Marketing, Investments

Training in:
- plant management
- marketing
- accounting
- profitability calculations
- credit/loan facilitation
- cooperatives

Development of appropriate:
- credit schemes for small- scale mining
- organizational structures
- advertising

formulation of raw material policy suited to small-scale mining
- debureaucratization
- legalizing small mines
- government purchase of products at market prices
- management consulting
- credit and tax incentives

The objective of this technical handbook on small-scale mining is to provide technical alternatives and organizational improvements for small-scale mining. The goal of these technical innovations is to assist the small-scale mining industry in numerous ways in solving its problems; specifically, this can be accomplished by:

- improving operational success by increasing mine output,
- job generation with low specific cost,
- improving the quality of social and economic living conditions,
- increasing production through semi-mechanization1) using regenerative sources of energy,
- improving job safety, and
- minimizing environmental impact.

1)Semi-mecanization is defined here as a form of mechanization in which only individual steps of the total mining and beneficiation operations are mechyanized (e.g. mechanization of the crushing process by use of a breaker). Additionally, semi-mechanization also defines an operation in which the control and feeding of the machine are performed entirely manually.

The techniques or methods discussed in this handbook are summarized according to five categories: analysis, surface and underground mining, beneficiation, and energy supply. In addition to purely technical solutions, the handbook also provides alternatives for improvement of organizational problems typical to small-scale mining. In conjunction with that, historical mining machines, modern small-scale mining equipment, and traditional techniques were examined within the scope of the investigation. The integration of the historical, modern and traditional elements serves as the basis here for the development of an appropriate technology.

This technology is aimed not only at the small-scale miners themselves. The majority of the mining and dressing techniques identified to be applicable for small-scale mining, due to their suitability for local production, offer various approaches to the promotion of crafts and small manufacturing industries.

The craftsmen and the small to medium-scale manufacturers can especially profit from the production of machines and facilities for the small-scale mining industry and resulting diversification of product lines when

- competetive products do not yet exist on the local market, and

- if the local market for mining and processing equipment is protected from the import market as a result of, amongst others, import duties, shortage of foreign exchange, and high transportation costs.

Small-scale craftmen or manufacturers associated with the mining industry can:

- deliver faster and cheaper

- more accurately meet the customers needs

- benefit from the relationship to become independent and self-organized

- shorten repair and maintenance time, which is especially important in seasonal small-scale mining operations.

The following results are expected from the application of the recommended technical and organizational improvements for small-scale mining in developing countries:

- local production of equipment for appropriate mining and beneficiation technology by craftshops and small-scale manufacturers. This would be developed to meet demand within the country itself and, in addition, could lead to the intensification of a South-South cooperation

- consultancy for small-scale mining operations, accompanied by installation of appropriate equipment, support for adaption developments, etc.

- educational measures; training of small-scale mining personnel, planners and consultants in suitable educational facilities, for example in the areas of analysis, geology, mineral-deposit geology, work organization and techniques in mining and beneficiation, work safety, marketing and economics

- development of new concepts for environmentally and economically advantageous energy supply systems, such as the use of renewable energy sources

- development and implementation of environmental protection measures in small-scale mining (e.g. decreasing the amount of lumber needed for mine supports, reducing or even eliminating mercury emissions in the gold amalgamation process, addressing problems of cyanide-leaching in gold-ore processing, reducing contamination of waste water by, for example, reagents from flotation processing or slurry effluents from beneficiation operations).

The effects of such a politically-instigated developmental program would include creating and securing jobs in the non-agricultural sector, qualifying workers in the mining and craft industries, import-substitution of raw materials in the industrial, energy, and agricultural sectors, substituting locally- manufactured for imported machinery and equipment, as well as contributing to regional development.

As a whole, these measures lead to the internalizing of costs and income in the areas influenced by mining i.e. the mines themselves, the craft and manufacturing industries, as well as the suppliers of raw materials.

CLOSE THIS BOOKTools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)
A. Analysis
VIEW THE DOCUMENTA.1. Definition
VIEW THE DOCUMENTA.2. Initial conditions and problem areas

Tools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)

A. Analysis

A.1. Definition

The section on analysis includes the determination of the chemical and physical properties of soil, rock and ore samples as well as of concentrates, middlings and tailings from beneficiation processing. The analytical procedure used here consists of the following four steps:

1. sampling,
2. chemical or physical analysis of sample material,
3. classification and statistical analysis of data, and
4. interpretation of the results.

The application of analytical procedures in the small-scale mining industry are particularly significant for prospecting, exploration, quality control during mining, beneficiation, marketing and environmental protection.

A.2. Initial conditions and problem areas

Small-scale mining in developing countries suffers from a lack of knowledge concerning crude ore reserves as well as product composition. The situation is worsened by the fact that ihomogeneous mineralization exists, especially in deposits of sub-volcanic genesis as are characteristic of the Andean region. As a result, variations in mineralization occur within small proximities with regard to both geological relationships and mineralogical and geo-chemical compositions. A good example of this can be seen in Bolivian tin deposits, where the tin source can be Cassiterite (for chemical composition see Table), Cylindrite, Teallite or Frankeite (three Sulfostannates) or Stannite. Knowledge of the entire geological relationship is critical for planning. not only the mining procedure but especially the beneficiation processing.

The composition of concentrates is frequently not known by the small-scale mining operators, which can be disadvantageous for selling the products. Impurities in the concentrates result in lower prices for the product following high penalty deductions assessed by the buyers or the beneficiation plant, and further impairing the marketing of profitable by-products. The Cascabel Mine in Bolivia (Dept. La Paz) serves as an example, which, despite higher lead, silver and tin contents in its concentrates, is only able to market its products with great difficulty, suffering large penalty assessments (price discounts) due to abnormally high levels of mercury contamination. These mineralization problems occur not only in the primary vein ore deposits, but are also present in placer deposits; deficient product knowledge is the reason why valuable platinum contents in alluvial gold deposits (e.g. in Colombia) are not being mined and consequently not being separately marketed.

Another characteristic problem of small-scale mining in developing countries is the questionable credibility of the analyses, which, as a rule, are performed by the buyer himself. Control checks have shown that results of the analyses are being manipulated to the advantage of the buyer and to the disadvantage of the small-scale mine operators. Primarily, the silver contents were given as too low, and the residual moisture levels as too high, which is difficult to prove in the absence of control measures.

The resulting conclusion is that the small-scale mining industry needs to implement its own control program. In addition to quality control during mining (grade control) and beneficiation and marketing planning, analytical procedures suitable for small-scale mining are also important for prospecting and exploration activities.

The use of centralized analytical methods becomes inconvenient or even impossible for small-scale mining due to the location-dependency of stationary analytical techniques, and the lack of infrastructure in the remotely-located, isolated small-scale mining operations.

The need exists within the small-scale mining industry for a simple, portable analyitical procedure. The main criteria should include low cost and quick performance with limited equipment and time requirements while avoiding unnecessary measuring precision. The extent to which the analytical results are representative and are reproducable is determined more through the quality and preciseness of the sampling rather than the application of the most optimal method of analysis. An analysis which is precise to several places behind the decimal point is worthless when an improper sampling procedure results in inaccurate figures in front of the decimal point.

The lack of simple analysing procedures for smallscale mining is not limited just to developing countries; this is an area calling for research-anddevelopment efforts.

A.2.1 SAMPLING

The sampling procedure is of primary importance for the technical planning of mining and beneficiation operations. However, a very precise and exact analysis is of no value if the sample being analyzed is not representative. A sample is representative of its original geologic environment only when the same chemical, mineralogical and physical relationships characteristic of the specific geologic area are exhibited in the sample. These relationships are defined by the mineral or element distribution, humidity, granulation and grain-size distribution, permeability, etc. When a waste dump, mineral deposit or beneficiation product is analyzed, it is not possible to examine the entire dump or deposit, or the total product quantity, but only portions of the whole. Proper conclusions can only be made from these sampled portions when they are representative of the whole.

In the testing of a pile of crude ore, for example, it is not sufficient to take only one chunk of ore from the pile, which may be representative of only the country-rock or the mineralization itself. An analysis of this sample alone would result in erroneous conclusions concerning the metal-content of the deposit in general. Several sampling techniques which consistently produce representative results are discussed below:

Bulk sampling is employed for the sampling of loose fine-to-coarse-grained materials, such as in the analysis of tailings, waste dumps, products, and crude ores. Numerous smaller samples are taken from a number of various arbitrary locations throughout the material pile without preference to any particularly richer or poorer regions. The sampling procedure should not only include numerous different sample locations but should also ensure that the grain-size of the samples also vary, in that samples of the finer fractions and the fines are also collected along with the large pieces of ore. In so doing, the sample volume or quantity should always be at least ten times greater than that of the largest individual sample in order to assure that the effects of classification, whether from deposition in the pile or from selectivity during blasting, are statistically compensated.

Channel sampling is a method of sampling exposed in-situ ore-bodies. In this procedure, sample material is obtained from a groove, constant in width and depth, cut into the rock over a specific length, for example from the hanging wall to the foot wall across the width of the face during drifting; for example, a slit 10-cm in height and 5-cm in depth is cut out along the entire stope width with the sample material being collected on a tarp spread on the roadway floor below.

In-situ ore bodies can also be tested by grab sampling. Over the affected sample area, for example the area of the face, numerous equally-sized samples are randomly taken by hammering, digging or prying off loosened chunks without any locational preference for richer or poorer zones of mineralization. This sampling method is considerably easier to carry out than channel sampling, especially in hard ore bodies.

Cuttings-sampling recovers sample material from the washed drill dust or drill cuttings which are produced during drill-and-blast drifting and mining. As a result, the collected sample material originates not just from exposed surfaces, but rather represents a three-dimensional sampling area when an entire drilling-grid is sampled. An additional advantage of this method is that the sample material already exists in a finely-comminuted form.

In order to avoid systematic causes of errors, sampling should always be conducted by only one and the same person.


Fig.: Manual quartering of sample material by mixing, coning, mixing, flattening, quartering, and discarding of two opposite-lying quarters. Source: Schroll

For further treatment larger-sized samples are crushed and subsequently quartered. This is performed by heaping the crushed sample material into a cone, thoroughly mixing it several times via shovelling, and again heaping it into a cone by pouring. The cone is then pressed or stomped flat, and the resulting flat cone base is divided into four equal segments. Two of the quarters, located opposite one another, are analogously processed further, while the remaining two quarters are discarded. This procedure is repeated as often as required until the desired sample quantity has been reached. The conical pouring of the sample material assures the homogeneity of the sample.

The homogeneity of ores, alluvial deposits, tailings or other mined waste, and the degree to which the samples are representative, is particularly important where the element or mineral-content is low. This occurs in discrete aggregates, where the valuable mineral exists as separate grains independent of the mineralized matrix. An important example is gold. Gold analysis demands values of a magnitude of less than 1 g/t. Gold particles can appear as gold glitters or nuggets with individual weights of up to more than 1 9. If, for example, one ton of crude ore which has only a single 1-9 gold nugget is analyzed by using 100kg of sample material which happens to contain this nugget, the results will indicate 10 9 of gold/l, which of course is too high. Statistically, in 9 out of 10 cases the nugget would not be contained in a 100-kg crudeore sample, so that the gold content is then assessed at 0 g/t. This effect is known as the nugget effect and requires, in such cases, multiple samples of large quantities. The more nonhomogeneous the sample material, the higher the number of samples required in order to obtain a statistical median value which approaches the true value for the material as a whole.

A.2.2 MINERALOGICAL EXAMINATION

Under certain conditions, an optical measuring or visual estimation of the ore content underground can serve as a substitute for an analysis. The prerequisites for this are:

- a relatively high proportion of ore minerals in the total material, since only then is the measured or estimated value of sufficient accuracy, and

- high visibility of the ore mineral under the conditions of examination. This requires clean working faces or sampling surfaces, perhaps involving the use of artificial methods to improve visibility, for example with ultra-violet lamps to detect mineral luminescence.

The visual evaluation is significant in lead-zinc mining in hydrothermal deposits with classic vein patterns. As a rule, testing is combined in this case with geological mapping of the hanging or footwalls. In so doing, the total width of the wall and the width of the ore veins are measured onto one profile. The profile must run vertically along the strike and dip of the vein; otherwise the values appear unrealistically high. If the profile is divided into several fragments, the sum of the individual vein thicknesses can be determined (for example, 25 cm galena, 15 cm sphalerite over a thickness of 175 cm). From this information, the volumetric proportion of the various ore minerals can be calculated. When the densities of each ore mineral and host rock are included, the total weight proportion of the ore minerals can then be established. With this information, and the additional knowledge of the metal content in each ore mineral, the metal-content distribution (% by weight) of the sampled profile can be determined. The incorporation of correction factors to account for mineral intergrowths, etc., can increase the accuracy of this method. This form of sampling or testing has proven itself even in highly mechanized operations in industrialized countries where it competes against modern procedures, such as portable X-ray fluorescent analysis.

Another mining sector which employs optical evaluation is scheelite mining, where the mine face is irradiated with an ultra-violet lamp which induces fluorescence of the scheelite.

As is true for sampling procedures, a high degree of accuracy in the optical test results can only be attained through disciplined work procedures and a great deal of experience.

A.2.3 ADVANTAGES OF MINIMIZING ACCURACY

All analysing procedures and evaluation methods exhibit a linear relationship between degree of accuracy and the cost of analysis, or, in other words, the more accurate the analysis, the more complex the equipment and the higher the costs. The lower the detection limit of the analytical method, i.e. the smaller the analyzed value is, the more expensive the analysis will be. Looking at this fact, it is absolutely necessary from an economical standpoint that the small-scale mining industry employs the cheapest method of analysing available within the desired accuracy and metal-content limits.

A.2.4 DETERMINATION OF ELEMENT DISTRIBUTION IN RAW ORE AND CONCENTRATES

Lack of knowledge about the contents of the different elements in raw ore, mine waste and concentrates is frequently the cause for the inefficient or uneconomic performance of small-scale mining operations. As a rule, only the contents of the desired metals in the ore and concentrate are examined. Consequently, the causes for undesired metal contents in the products, and subsequent penalty assessments, are not known by the small-scale miner. Additionally the accounting statements from the ore buyer do not explicitly indicate the reasons for penalty deductions. Commercially marketable byproducts also remain unidentified.

A number of various contaminating metals and elements which may be present in the mine products lead to penalties, assessed by the smelters in the form of price reduction, when the content of these metals exceed a maximum tolerance level. These elements, their maximum tolerance limits, and the penalty amounts are established by the smelting standards, varying according to smelting process, market situation and buyer. Consequently, a definite statement concerning these elements and tolerance limits cannot be made; however, as a general reference, the following table lists some critical elements which are deleterious to non-ferrous metal ore concentrates:

As a rule, non-ferrous metal smelters penalize:

Bi

In almost all concentrates

Hg

in almost all concentrates

S

in concentrates of valuable oxide minerals

As

in Pb-Ag-concentrates

Cu

in Pb-Ag-concentrates

Cd

in Pb-Ag-concentrates

Se

in almost all concentrates

Penalties can lead to a considerable decrease in profit for small-scale mining operations. Therefore, knowledge of the element and trace-element distribution should be obtained, as much as possible, before initiating any mining activities or planning the beneficiation plant in order to establish a marketing strategy.

Similar to the deleterious metals, element contents which would be worth recovering and marketing in the form of by-products are also often overlooked; for example, zircon sand from alluvial deposits, gold-containing pyrite and arsenopyrite from complex sulphide veins. Here, as well, a knowledge of the element distribution prior to the start of any mining activities is crucial in order to formulate an optimal marketing strategy.

The practice of performing complete analyses on a concentrate sample and on a mixed raw-ore sample, conducted by a competent laboratory for the purpose of determining the contents of all relevant metals, trace-elements and cations, should become standard procedure for the small-scale mining industry. Governmental support of these needs, for example by providing inexpensive analyses, would significantly contribute to promoting the small-scale mining industry.

The performing of mineral analyses also serves an important function from an environmental-protection viewpoint by identifying environmentally-damaging components such as sulfur in coal, residual mercury in gold tailings, cyanide and arsenic contents in mining wastes, etc.

A.2.5 DETERMINATION OF THE VALUABLE-MINERAL SOURCE

In addition to a purely geochemical examination of the raw materials, a mineralogical knowledge, especially of the valuable-mineral sources, is of major priority in small-scale mining. Since beneficiation processing in small-scale mining usually leaves the material components of the minerals unchanged, this identification of the valuable-mineral source is particularly important for planning and marketing. This can be accomplished through microscopic examination of polished sections, which enables experienced microscope analysts to quickly and easily semi-quantitatively recognize segregations, trace element minerals, etc.

The question, for example, of whether silver appears as a silver mineral or as a lattice element of lead or zinc minerals can strongly influence the beneficiation, marketing and profitability of a mining operation.

Equally important is the mineralogical composition of the raw material in primary gold deposits, in which the gold can occur as free gold or bound to pyrite or arsenopyrite as "refractory ore".

Whatever the situation, it is essential that the major ore minerals can be marketed. Some ore deposits produce main valuable minerals which are sellable only with great difficulty, if at all; such as the complex ore deposits with spienles sulfades (antimony and arsenic) as the metal source.

One example is the Taricoya Mine in Bolivia, whose raw ore reserves are relatively promising according to FONEM, as here shown in the Table:

Pb: 3.45 %

Ag: 379 g/t

Sb: 6.48 %

Au: 7 g/t

However, because the main ore mineral is composed of specular jamsonite (Pb4FeSb6S14) selling the concentrates is very difficult.

The above example shows that the results of mineralogical studies play an important role in determining whether or not an ore deposit can be mined profitably using the simple mining methods characteristic of small-scale mining.

A.2.6 OTHER RAW MATERIAL STUDIES

In addition to chemical and mineralogical composition, other characteristic data are also important, depending upon the material, for the analysis of raw mineral reserves. Examples are:

- ash content' thermal value, sulfur content, caking capacity, etc. for fossil fuels (coal, peat);
- compressive strength of a cube, cleavability and permeability for construction materials;
- swelling characteristic for certain clays (vermiculite);
- weaving characteristic for asbestos;
- coloration for pigment raw materials (barite, kaolin);
- grain sizes for many raw materials (large grain size for graphite and mica, fine grain size for kaolin;
- hardness for grinding material (corundum, garnet).

The following table presents a list of essential ore minerals including primary physical characteristics and types of veins and host rocks.

Table: Characteristics of Ore Minerals including Vein Types, Gangue or Matrix, Asociated Minerals and Host Rocks:

Name

Composition

Content of valuable minerals

Density

Tennnacity 1)

Ordinary lead-zinc mineralization:

galena

PbS

Pb: 86.6 %

7.2-7.6

4

sphalerite

ZnS

Zn: 67.0 %

3.9-4.1

2

wurtzite

ZnS

Zn: 67.0 %

4.0-4.1

2

greenockite

CdS


4.8

*

cerussite

PbCO3

Pb: 77.5 %

6.4-6.6

1

anglesite

PbSO4

Pb: 68.3 %

6.3-6.4

1

smithsonite

ZnCO3

Zn: 52.1 %

4.0-4.5

2

Mixed lead-silver-zinc-gold mineralization:

bournonite

CuPbSbS3

Pb: 42 %

5.75.9

3

boulangerite

Pb5Sb4S11

Pb: 55 %

5.9-6.5

2

jamesonite

Pb4FeSb6S14

Pb: 40 %

5.6

4

tetrahedrite

Cu12Sb4S13

Ag: up to 19 %

4.6-5.1

2

free silver

Ag

Ag: up to 100 %

10.1-11.1

6

stephanite

Ag5SbS4

Ag: 68 %

6.2-6.4

2-4

argentite

Ag2S

Ag: 87 %

7.2-7.4

6

proustite

Ag3AsS3

Ag: 65 %

5.6

2

pyrargyrite

Ag3SbS3

Ag: 60 %

5.8

2

petzite

Ag3AuTe2

Ag: 41.8 %





Au: 25.4 %

8.7-9.1

5

free gold

Au

Au: up to 100 %

15.5-19.3

6

copper minerals:

free copper

Cu

Cu: up to 100 %

8.5-9.0

6

covellite

CuS

Cu: 66.5 %

4.6-4.8

4

chalcocite

Cu2S

Cu: 79.9 %

5.5-5.8

4

bornite

Cu5FeS4

Cu: 63 %

4.9-5.3

2-4

chalcopyrite

CuFeS2

Cu: 34.7 %

4.1-4.3

3

enargite

Cu3AsS4

Cu: 48 %

4.4-4.5

2

cuprite

Cu2O

Cu: 88.8 %

6.1

2

malachite

Cu2(OH)2CO3

Cu: 57 %

4.0-4.1


azurite

CU2(OH/CO3)2 Cu: 55 %

3.8

2


tin minerals:

cassiterite

SnO2

Sn: 78.1 %

6.8-7.1

2

teallite

PbSnS2

Sn: 30%

6.4

4

franckeite

Pb5Sn3Sb2S14 Sn: 17 %

59

4


stannite

Cu2FeSnS4

Sn: 27.5 %

4.3-4.5

2

antimony minerals:

antimonite

Sb2S3

Sb: 71.4 %

4.6-4.7

4

antimonochre

Sb2O3(H2O)

Sb: var.

5.6-6.6

**

bismuth minerals:

free bismuth

Bi

Bi: up to 100 %

9.7-9.8

2

bismuthinite

Bi2S3

Bi: 81 %

6.8

4

bismuthochre/bismite

Bi2O3

6.7-7.5

**


tungsten minerals:

scheelite

CaWO4

W: 63.8 %

6.1

2

wolframite

(Fe,Mn)WO4

WO3: 76 %

7.1-7.5

2

ferberite

FeWO4

WO3: 76.4 %

7.5

2

huebrerite

MnWO4

WO3: 76.6 %

7.1

2

tungstic ochre/tungstite

WO2(OH)2

4.0-4.5

**


additional and accompanying minerals:

realgar

As4S4

As: 70 %

3.6


orpiment

As2S3

As: 61 %

35


molybdenite

MoS2

Mo: 60 %

4.6-5.0


pyrite

FeS2


5.0-5.2


pyrrhotite

FeS


4.6-4.8


haematite

Fe2O3


4.9--5.3


arsenopyrite

FeAsS


5.9-6.2


limonite

FeOOH


aprooox.4


jarosite

KFe3((OH)6/(SO4)2)

3.1-3.3



argentojarosite

AgFe3((OH)6/(SO4)2)

?



plumbojarosite

PbFe6((OH)6/(SO4)2)

?



1)Tenacity characterizes brittleness or breaking characteristics of the mineral

Explanation of tenacity/Remarks:

1

very brittle

2

brittle

3

less brittle

4

mild

5

ductile

6

very ductile

*

exists as fine intergrowths

**

exists in pulverized form due to weathering

1)

Tenacity characterizes brittleness or breaking characteristics of the mineral

Table: Characteristics of Ore Minerals including Vein Types, Gangue or Matrix, Associated Minerals and Host Rocks:

Name

Composition

Density

quartz

SiO2

2.6-2.7

calcite

CaCO3

2.6-2.8

siderite

FeCO3

3.7-3.9

dolomite

CaMg(CO3)2

2.8-2.9

fluorite

CaF2

3.1-3.2

barite

BaSO4

4.3-4.7

vivianite

Fe3PO4 8H2O

2.6-2.7

apatite

Ca5(F,Cl,OH)(PO4)3

2.9-3.1

epidote

(Ca2Fe)(AI2O)(OH)Si2O7SiO4

3.4-3.5

tourmaline

Complex boron-hydroxylic silicate

3.0-3.1

orthoclase

(K,Na)AISi3O8

2.5-2.7

plagioclase

(Ca,Na)(Al,Si)4O8

2.6-2.7

alunite

KAI3(OH)6(SO4)2

2.6-2.9

HOST ROCK

Name

Density

granite

2.6-2.7

diorite

2.8-2.9

syenite

2.6-2.8

dacite

2.6-2.7

andecite

2.5-2.6

trachyte

2.6-2.8

basalt

2.7-3.2

porphyry

2.7-2.9

gneiss

2.4-2.7

quartzite

2.3-2.6

sandstone

2.2-2.5

clay shale

2.6-2.7

CLOSE THIS BOOKTools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)
Technical Chapter 1: Analysis
VIEW THE DOCUMENT1.1 Blow pipe assaying
VIEW THE DOCUMENT1.2 Pycnometer
VIEW THE DOCUMENT1.3 Manual magnetic separator by Dr A. Wilke
VIEW THE DOCUMENT1.4 Quick-test-strips merckoquant
VIEW THE DOCUMENT1.5 Rifflebox

Tools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)

Technical Chapter 1: Analysis

1.1 Blow pipe assaying

General Ore Mining
Analysis

germ.:

Lotrohrprobierkunde

span.:

analisis con soplete

Manufacturer:

Krantz

TECHNICAL DATA:

Dimensions:

approx. 20 - 25 cm long, pointed nozzle with 0.4 - 0.5 mm jet of platinum or nickel

Weight:

approx. 50 grams

Degree of Mechanization:

not mechanized

Form of Driving Energy:

either blown by mouth or

Alternative Forms:

driven by compressed air

Mode of Operation:

intermittent

Materials for operation:


Type:

charcoal, clay vessel, glass tube, fuel Na2CO3 (soda) K2C2O2

(sorrel-

salt) Na2B4Ox7 × 10 H2O (borax) Na(NHg)HPO4 × 4H2O(microcosmic salt)

ECONOMIC DATA:

Investment Costs:

blowpipe approx. 30 DM

Operating Costs:

predominantly determined by cost of reagents and labor costs

Related costs:

very accurate weighing scale (to ± 0.1 mg), lineal scale for determinin small silver and gold grains, magnifying lens

CONDITIONS OF APPLICATION:

Operating Expenditure:

low |————|———| high

Maintenance Expenditure:

low |———|————| high

Personnel Requirements:

highly experienced analyst

Type of Analysis:

semi-quantitative and qualitative

Accuracy of Results:

+ 2 g/t for Au and Ag

On-site Performability:

Ag, Au, Cu, Pb, Bi, Sn, Co, Ni, Hg can be determined quantitatively

Replaces other equipment:

all other analytical-chemical methods such as RFA, liquid chemicals

Regional Distribution:

previously widely-distributed sampling and analyzing method in industrialized countries; has since been replaced by new methods.

Operating Experience:

very good |———|————| bad

Environmental Impact:

low |———|————| very high

Suitability for Local Production:

very good |————|———| bad


Parts of the blowpipe and the heater, possibly the stand as well as the small-scale compressor could be locally produced.

Lifespan:

very long |———|————| very short

Bibliography, Source: Plattner, Wehrle, Kest, Kolbeck, Frick-Dausch

OPERATING PRINCIPLE:

Blowpipe analysis is a multiple-step procedure for qualitatively or semi-quantitatively determining the individual elements contained within a small quantity of sample. The process involves dry thermal procedures, sometimes in combination with wet testing methods. The sample is heated in an open or half-closed pipe, melted to a bead with borax (Na2B4O7 × 10 H2O) or microcosmic salt (NaNH4HPO4 × 4 H2O) under oxidizing and reducing conditions, burned directly in a flame to determine flame color, or heated with coal under oxidizing and reducing conditions. A small flame torch serves as the energy source, which is intensified by blowing into it through a tapered tube, the blowpipe. The discoloration of smelt, sublimate, corona or flame in each particular assay or experiment, together with any distinct odors and/or reactions which may appear, provide Information on the chemical composition of the sample.

REMARKS:

Of importance is a waterbag, which is an extension of the pipe for collecting condensed water, to prevent It being expelled during blowing.

Lamps with cotton wick and rape-oil, paraffin, tree oil and mixtures of alcohol (spirits) with gasoline (benzine) or oil of turpentine are suitable.

Polished pieces of charcoal of approx. 30 × 30 × 40 mm are employed as a base. If charcoal is not available, the foundation or base can be prepared using coal dust and starch paste.

In 1670, Erasmus Bartholin conducted the first scientific research on the use of the blowpipe. A homogeneous air current can be achieved during blowing by connecting the blowpipe to an available compressed air line. If this is not possible, a pumped-up tire, for example from a wheel barrow or automobile, can be used as a compressed air tank.

The advantages of blowpipe analysis are the simplicity of both the determination and the required equipment. Samples can be analyzed very quickly and comparatively accurately, which is particularly important in an operating mine. Special sample preparation, such as extensive crushing, etc. are not necessary.

The analysis methods, which appear complex in their description, can be greatly simplified when standard assays are conducted on known metals.

SUITABILITY FOR SMALL-SCALE MINING:

Semi-quantitative and qualitative analytical technique requiring simple and low-cost equipment; demands, however, a highly-experienced operator. In metal mining, the blowpipe analysis is suitable for grade control and for assaying during prospecting and exploration.


Fig.: View of blowpipe with changeable precious-metal nozzle (above left). Source: Frick-Dausch

Table: The primary chemical reactions of blowpipe analysis. Source: Frick-Dausch

A. Heating of the substance in a half-closed pipe

1. A distillate develops: water.

2.
A pure white sublimate develops:
Salts of ammonia: simultaneous occurrence of NH3 odor.
Mercury chloride: melts, evaporates and condenses in a needle-like form.
Mercury all-chloride: sublimates without melting; hot sublimate is yellow, cold is white.
Arsenic tri-oxide: fine-crystalline white sublimate.
Antimony tri-oxide: melts to a yellow liquid and sublimates at higher temperatures.

3.
A coloured sublimate develops:
Arsenic and high-grade arsenic ores: mirror of arsenic, garlic odor.
Antimony: mirror of antimony.
Arsenic sulphides, arsenopyrite: hot sublimate is dark, cold varies from yellow to red.
Antimony sulphides: at higher temperatures; hot sublimate is black, cold is red-brown.
Sulphur: melts easily, condenses as a yellow sublimate.
Mercury sulphide: black sublimate which when rubbed with a match changes only very slowly into a red modification.
Mercury grey sublimate from metallic mercury.

4.
A gas develops:
Oxygen: from chlorates and peroxides.
Carbon all-oxide: from carbonates and bi-carbonates. CO2-gas put into lime water produces a white precipitate, which then dissipates when acidified with HCI, contrary to CaSO4.
Ammonia: from salts of ammonia
Hydrogen sulphide: from water-bearing sulphides.

B. Heating in a half-closed pipe with potassium-bisulphate
Nitrate and nitrite form NO2.
Bromides emit red-brown bromine vapors.
Iodides release violet-colored iodine vapors.
Chlorides form hydrogen chloride.

C. Heating in a pipe open on both sides (calcination test)
Free sulphur and metal sulphides form SO2.
Tellurium emits white smoke, which partially condenses.
Selenium sublimates black, on the upper edge often reddish, Selenium odor.
Arsenic substances emit white, volatile, cristalline arsenic tri-oxide.

D. Bead test

a) Borax bead: borax Na2B4O7 10 H2O

Borax bead

Coloring element

Oxidation bead

Reduction bead


hot

cold

hot

cold

Mn

violet1)

red-violet

colorless

colorless

Ni

violet (recognizeable only for a short time)

red-brown

cooolorless or

colorless or grey2)





grey

Co

blue

blue

blue

blue

Cu

green

blue-green to light blue

colorless

sealing-tax red opaque3)

Vd

yellowish

green-yellowish

brownish

lllight greenish

Cr

dark yellow to red

green

green

green

U

yellow-red

yellowish

green4)

green4)

Mo

yellowish5)

colorless

yellow

light brown-yellow

Wo

yellow to colorless

colorless

yellow

light brown-yellow

Ti

yellowish

colorless

yellow-brown

yellow-brown

Fe

yellow-red

yellow to colorless

greenish

greenish


1) black when solution is too strong
2) from finely-divided metallic nickel
3) easy to produce with tin, highly characteristic
4) when saturation is too strong and by whirling, greenish-black and muddy
5) only in a very pure oxidizing flame completely free of reducing components

b) Phosphor salt test; phosphor salt (= microcosmic salt) NaNH4HPO4 × 4H2O

Phosphor salt bead

coloring element

oxidation bead

reduction bead


hot

cold

hot

cold

Mn

violet

violet

colorless

colorless

Co

blue

blue

blue

blue

Cu

green

blue-green to light blue

colorless to greenish

sealing-wax red opaque1)

Mo

yellowish2)

colorless2)

brownish-green

green

Cr

red, then dirty green, finally clear green

as with oxidation bead, but colors more intense



Vd

dark yellow

yellow

brownish

green

U

yellow

yellow-green

dirty green

green

Ti

yellowish to colorless

colorless

yellow

violet3)

Wo

yellowish to colorless

colorless

dirty green

blue4)

Ni

reddish-brown

yellow to reddish-yellow

reddish to yellowish with SnCl2 grey and muddy

Fe

red-yellow, then green-yellow, finally brownish

like oxidation bead, but colors less intense

1) with the help of tin
2) only in a very pure oxidizing flame completely free of reducing components
3) calcined with a trace of ferro sulphate, blood red; very sensitive!
4) with a trace of ferro sulphate, blood red; also very sensitive (e.g. wolframite!). With SnCl2 and without Fe-additive, dark green.

E. Flame coloration

Yellow flame:

sodium

Reddish-yellow flame:

calcium

Red flame: lithium;

strontium


Differentiation between Li and Sr:
LiCl is more volatile than SrCI2. LiCI develops at once and does not last.
Green flame: barium: yellowish-red lasting coloration.

Boric acid: very sensitive when sample is mixed with CaF2 and H2SO4; evaporates as BF3
Copper nitrate: pure green (copper chloride: blue).
Phosphoric acid: light bluish-green, especially after moistening the sample with H2SO4.

Blue flame: copper chloride.
Selenium: selenium odor.

Violet flame: potassium; rubidium; caesium.
Separation of Na and K: viewed through a cobalt glass, the light from Na fades, and the potassium flame appears purple-violet.

F. Sample with cobalt solution

The sample is soaked with a cobalt solution (1:10) and heated on a magnesia stick in the oxidizing flame.
Blue coloration: silicic acid and silicates: light blue.

alumina: dark blue (Thenard's-blue).

Green coloration: zinc oxide, pure green (Rinnmann's-green).
Tin oxide: blue-green.

G. Soda-saltpeter-melt

Light yellow melt: chrome.
Light reddish-yellow melt: uranium.

Vanadium produces a very pale-yellowish-colored melt; colorless when cold.
Ferro oxide does not go into solution.

Greenish-blue melt: manganese.
Testing for: molybdenum, tungsten, vanadium, columbium, titanium
The soda-salpeter-melt is rubbed with water in a flask filtered, and the filtrate is acidified with H2SO4. A piece of metallic zinc is soaked in the solution for a longer period of time.

Tungsten: The solution slowly turns sky-blue
Molybdenum: solution slowly turns brownish-black.
Vanadium: solution becomes light blue, then later green. If the sulphuric solution is treated with hydrogen peroxide, vanadium causes a yellow-brown coloration.
Columbium: the dry mass is treated with concentrated H2SO4. When cooled, the solution is poured into a threefold volume of water and zinc is added. In the presence of columbium the solution first becomes blue and then changes to a turbid brownish-black
Titanium: present if a white powder, which slowly turns violet, precipitates out when an aqueous solution of the melt is acidified.
Special reaction for titanium: potassium bisulphate bead is dissolved in water and hydrogen peroxide is added; if the solution becomes brownish-yellow, titanium is present.
To test for manganese, alcohol is added to an aqueous solution of the melt and the precipitated manganese dioxide is filtered off. In the presence of chrome, testing for the other metals according to the described method is not possible.

H. Testing on Coal

1. Sublimates

Yellow sublimate: hot - dark yellow lead, bismuth (often bead).
White sublimate: hot - yellow zinc; when moistened with cobalt nitrate and strongly annealed: green.Blue sublimate: cadmium.
White sublimate, adhering to sample: tin (involatile).
White sublimate: hot - yellow. molybdenum. When a reducing flame is briefly held over a molybdenum sublimate, perpendicular to longitudinal direction of coal, a dark blue band of Mo3O2 develops in the middle of the white sublimate. Highly characteristic.
Brownish sublimate: silver (silver bead).
Grey sublimate and odorous fumes: selenium.
White sublimate and arsenic odor: arsenic.
White sublimate, slightly volatile and thick fumes: antimony.

2. Reduction with soda

White bead: silver, lead, bismuth, antimony, tin.

Colored bead: copper, gold.

Grey metallic spangle: iron, nickel, cobalt (magnetic) and platinum metals (non-magnetic).
Important special samples: sulphur (Hepar test). The substance is melted with soda under reducing conditions and placed on a thin sheet of silver. After moistening, a brownish-black coating develops on the silver sheet in the presence of sulphur.

Flourine: heating of the sample substance in a lead crucible with SiO2 and H2SO4 (Browning test, see below).

Tellurium: when tellurium ores are slightly warmed with concentrated H2SO4, the sulphuric acid turns red.

Uranium: the sample substance is first melted with soda, then with saltpeter; the melt is mixed with water to a pulp, which is then placed on a filter; acetic acid and solution of ferro potassium cyanide are added, which produces a brownish-red spot in the presence of uranium.

Silicic acid and flourine: Browning Test: the sample is mixed with calcium chloride and sulphuric acid to a pulp in a thimble-shaped lead crucible which is then covered by a lead lid with a hole in the middle. A wet piece of black filter paper (available by Schleicher and Schull) is placed over the hole, and a second, standard filter paper (wet and folded) is placed on top to keep the black paper wet. Following warming of the crucible in a water bath for about 10 minutes, silicon flouride escapes which hydrolytically dissociates during deposition of white silicic acid when it comes in contact with the moisture of the black filter paper. Upon completion of testing, the presence of silicic acid in the sample is revealed by a white spot on the black filter paper where it covers the hole in the lid. Very characteristic and highly sensitive. The procedure can also be used to test for flourine by mixing the sample substance with silicic acid and sulphuric acid. Boric acid can be disruptive since it similarly volatilizes.

1.2 Pycnometer

General Ore Mining
Analysis

engl.:

specific gravity bottle

germ.:

Pyknometer

span.:

picnometro (densimetro)

TECHNICAL DATA:

Dimensions:

available in volumes from approx. 10 ml to 1,000 ml

Weight: 50 ml-size:

16 grams

Extent of Mechanization:

not mechanized

Mode of Operation:

intermittent

Throughput/Performance:

approx. 10 - 12 measurements/h

Operating Materials:


Type:

water

ECONOMIC DATA:

Investment Costs:

30 to 100 DM

Operating Costs:

predominantly labor cost

Related Costs:

weighing scale with minimum accuracy of ±0.1g, cost approx. 200 DM

CONDITIONS OF APPLICATION:

Operating Expenditure:

low |———|————| high

Maintenance Expenditure:

low |———|————| high

Personnel Requirements:

experience in collecting and evaluating test data

Type of Analysis:

quantitative/qualitative

Accuracy of Results:

dependent weighing accuracy.

Time Requirement:

approx. 5 min.

On-site Performability:

pycnometric determination of density through the use of mechanical scales can easily be performed in the field, especially when at least 10 g of material is available for testing. The weighed sample for determining density should be dry and must be insoluble in a medium (e.g. water).

Operating Experience:

very good |———|————| bad

Environmental Impact:

low |———|————| very high

Suitability for Local Production:

very good |————|———| bad


Precision instrument made of glass which cannot be manufactured


locally; the mechanical scale also cannot, in most instances, be locally manufactured.

Lifespan:

very long |———|————| very short

OPERATING PRINCIPLE:

The pycnometer determines the density or specific weight of insoluble mineral fragments or powder. It is a carefully calibrated, very precise volumetric measuring apparatus. Three weighings to determine the density are taken as follows:

- with the dry, empty container (tare)
- with the container filled with dry mineral sample and
- with the container including sample filled with water in the absence of bubbles

The density is determined according to the following formula:

SPECIAL APPLICATIONS:

Determination of mineral density (mineral-identification method) and determination of beneficiation product densities.

REMARKS:

The accuracy of determination is particularly high when the differential quantities to be measured are not too small, such as when the pycnometer is half-full with sample material.

This measuring method, which measures density to an accuracy of ±0.1 g/m³ and therefore meets mining requirements, necessitates only minor equipment expenditures. A mechanical weighing scale accurate to ±0.1 g has been proven sufficient and enables this method to be applied in the field.

SUITABILITY FOR SMALL-SCALE MINING:

Pycnometer assaying is a simple and accurate method for determining density and is therefore well-suited for the evaluation of product quality and for mineral determination.

1.3 Manual magnetic separator by Dr A. Wilke

Metal Mining
General Analysis

germ.:

Handmagnetscheider nach Dr. Wilke

span.:

separador magnetico manual segun Dr. A. Wilke, separador magnetico manual

Producer:

Krantz

TECHNICAL DATA:

Dimensions:

Dia: approx. 3 cm, H: approx. 8 cm

Weight:

approx. 150 g

Externa power needs:

none, due to permanent magnet

Throughput/Performance:

for example, 30 min required for the quantitative separation of a 5-g heavy-mineral sample into five portions of differing magnetic susceptibility

Technical Efficiency:

relatively high selectivity

Operating Materials:

none .

ECONOMIC DATA:

Investment Costs:

approx. 200 DM

Operating Costs:

no operating materials, therefore only labor costs

Related Costs:

for quantitative determination: weighing scale

CONDITIONS OF APPLICATION:

Operating Expenditure:

low |———|————| high

Maintenance Expenditure:

low |———|————| high

Location Requirements:

none

Sample Requirements:

sample must be dry and dissociated.

Period of Analysis:

several minutes

Accuracy:

quantitative analysis is possible with liberated sample material. Probability of error ± 10 %

Regional Distribution:

not yet employed in small-scale mining in South America

Operating Experience:

very good |———|————| bad

Environmental Impact:

low |———|————| very high

Suitability for Local Production:

very good |————|———| bad

Under What Conditions:

requires a very strong, homogeneous permanent magnet and good membrane material.

Lifespan:

very long |———|————| very short

Bibliography, Source: Manufacturer information

OPERATING PRINCIPLE:

The pocket magnetic separator by A. Wilke is made of a strong, cylindrical permanent magnet with a cylindrical pole gap which can be moved up and down in a brass container by means of a pull rod. The container is covered by a transparent graduated plastic tube with increments in millimeters, and by means of screwing can be adjusted within this plastic tube to change the height of the magnetic surface above the sample material being separated. In this way the separation capability of the magnetic separator is varied, being greatest at the greatest height and smallest at the smallest height (thus biotite is Just barely separable).

To perform the analysis, the sample is thinly spread over a smooth, non-magnetic plate (glass, wood) and magnetically separated over the entire surface by placing the magnetic separator on the plate. The magnetic particles are attracted by and adhere to the magnet. The magnetic separator is then placed on another plate, and the enclosed magnet is lifted by the pull rod, resulting in the release of the magnetic particles. Starting with the minerals exhibiting the highest magnetic susceptibility, the magnetic separator can selectively separate a number of different magnetic fractions. Weighing the entire sample and the products can provide quantitative results when the sample material is completely analyzed.

AREAS OF APPLICATION:

Apparatus for selective separation of magnetic components of mineral sands, ground minerals and ores (beneficiation products).
Generation of monomineralic specimen for microscopic and chemical analysis.
Quantitative determination of composition of mineral mixtures.

Highly magnetic substances which can be separated:
Magnetite, maghemite, franklinite, pyrrhotine;
Moderately or weakly magnetic substances:
arsenopyrite, chromite, hematite, ilmenite, limonite, manganite, wolframite, rhodochrosite, garnet, amphiboles and pyroxenes.

DESIGN INSTRUCTIONS:

In addition to its analytical application, locally-manufactured pocket magnetic separators can be used in beneficiation for the purpose of recleaning concentrates, for example to separate out magnetic heavy-mineral particles from precious metal concentrates. Loud-speaker magnets (strong permanent magnets), placed in a plastic container and calibrated with distance washers made of cardboard, paper, wood, plastic or similar material, are suitable for this purpose.

SUITABILITY FOR SMALL-SCALE MINING:

Pocket magnetic separators are ideally suited for quick quantitative determination of magnetic mineral contents in raw ores and beneficiation products.

The simplest magnetic separators are well suited, depending upon the situation, for recleaning concentrates by removing magnetic components.

1.4 Quick-test-strips merckoquant

General Ore Mining
Analysis

germ.:

Schnellteststreifen Merckoquant

span.:

tire de prueba rapida Merckoquant

Manufacturer:

Merck

TECHNICAL DATA:

Dimensions:

Dia 3 cm, H: approx. 10 cm for 100 test-strips

Weight:

approx. 100 - 150 g

Throughput/Performance:

one analysis per test-strip

ECONOMIC DATA:

Investment Costs:

between 20 and 35 DM/100 quick-test-strips

Operating Costs:

none

Related Costs:

laboratory equipment to bring mineral samples into solution: mortar, acids, glass flasks and possibly an alcohol burner for quantitative analyses; analytical balance for samples in an aqueous solution.

CONDITIONS OF APPLICATION:

Operating Expenditure:

low |———|————| high

Maintenance Expenditure:

low |———|————| high

Personnel Requirements:

highly precise weighing scale necessary for quantitative determination

Location Requirements:

none

Sample Requirements:

sample must be completely dissolved in an aqueous solution.

Duration of Analysis:

several seconds

Accuracy of Analysis:

varies depending upon the type of substances being analyzed; values for arsenic, for example, are accurate to ±0.1 ppm, for pH-values to 0.5 pH.

Regional Distribution:

not widely distributed to date.

Operator Experience:

very good |———|————| bad

Environmental Impact:

low |———————| very high


depending upon type and degree of sample preparation (sample solution).

Suitability for Local Production:

very good |————|———| bad


not possible

Bibliography, Source: Manufacturer information

OPERATING PRINCIPLE:

Merckoquant quick-test-strips consist of plastic strips which have a sealed test-zone on one end impregnated with reagents, buffers and other compounds. These provide a quick preliminary identification in the range 2 1 mg/l (ppm). Application involves dipping the reaction-zone end into the aqueous sample solution for 1 to 2 seconds, and then comparing it to a color scale (included with the strips).

AREAS OF APPLICATION:

For quick determination of metal-contents in water (environmental impact assessments), raw-ore solutions, beneficiation products, etc. Control of reagents during simple cyanide leaching of gold.

REMARKS:

The following can be determined:

arsenic:

0.1

-

3 ppm

cobalt:

10

-

1000 ppm

copper:

10

-

300 ppm

molybdenum:

5

-

250 ppm

nickel:

10

-

500 ppm

silver:

0.5

-

10 g/l

zinc:

10

-

250 ppm

tin:

10

-

200 ppm

Total hardness:

4

-

25

pH-value:

0

-

14

Solutions which are too highly concentrated can be diluted with distilled water until the measureable concentration range is reached.

SUITABILITY FOR SMALL-SCALE MINING:

Highly suitable for environmental impact assessment (water) in that it provides fast and location-independent analysis and is very simple to use; unsuitable for raw-material analysis due to substantial difficulties in sample preparation.

1.5 Rifflebox

Metal Mining General
Analysing

germ.:

Riffelteiler

span.:

partidor de muestras acanalado

Manufacturer:

Haver + Boecker, Siebtechnik

TECHNICAL DATA:


Dimensions:

approx. 30 cm H × 60 cm W × 30 cm D

Weight:

approx. 2 - 5 kg depending on thickness of material

External power needs:

not mechanized

Throughput/Performance:

several hundred kg/in

Technical Efficiency:

good representation of sub-samples

ECONOMIC DATA:


Investment Costs:

300 to 1200 DM for equipment manufactured in the FRG; approx. 100 DM when locally manufactured

Operating Costs:

labor costs only

Related Costs:

none

CONDITIONS OF APPLICATION:

Operating Expenditure:

low |———|————| high

Maintenance Expenditure:

low |———|————| high

Location Requirements:

none

Sample Requirements:

sample must be crushed to a size less than half the riffle width.

Duration of Separation:

very short

Replaces other Equipment:

mechanized sample-divider

Regional Distribution:

already distributed in the laboratories of organizations involved with small-scale mining.

Operating Experience:

very good |———|————| bad

Environmental Impact:

low |———|————| very high

Suitability for Local Production:

very good |———|————| bad

Under What Conditions:

ordinary metal-working shops

Lifespan:

very long |———|————| very short

Bibliography, Source: Schroll, manufacturer information

OPERATING PRINCIPLE:

The sample-divider directs the sample material over riffles which alternately distribute the sample to one side or the other, thereby guiding it into two separate compartments; the sample material of one container is then retained for testing, that of the other is discarded.

AREAS OF APPLICATION:

Sample preparation through a stepwise halving of sample material from individual or composite samples of raw-ores from ore-vein or alluvial deposits, or of beneficiation products.

REMARKS:

Riffleboxes are very simple dividers which are known for their success in producing highly representative sub-samples.

SUITABILITY FOR SMALL-SCALE MINING:

Riffleboxes are highly suitable for small-scale mining application especially since they can be locally manufactured and because they offer an easily-operable method for improving sample preparation, which increases the analytical accuracy associated with small-scale mining.


Fig: Physical Principle of the Rifflebox. Source: Lauer


Fig.: Rifflebox for example preparation. Source: Armstrong


Fig.: Rifflebox with (1) sample divider, (2) feed tray and (3) receiving tray, from Schubert.

CLOSE THIS BOOKTools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)
B. Underground mining
VIEW THE DOCUMENTB.1. Definition
VIEW THE DOCUMENTB.2. Existing situation and problem areas
VIEW THE DOCUMENTB.3. Organizational measures
VIEW THE DOCUMENTB.4 Environmental and health aspects

Tools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)

B. Underground mining

B.1. Definition

Underground mining includes all aspects of raw mineral extraction by man assisted by the use of technical aids. In addition to the activities involving mining and haulage, it also includes exploration and provision of the necessary infrastructure as well as all measures for the miner's safety. Included among these are:

- drilling

- drainage

- blasting

- ventilation

- loading

- lighting

- haulage

- roof support.

The frequently-used small-scale mining method in developing countries, characterized as a shallow digging or excavating (cateo), can be regarded as a transitory form of open-pit mining.

Deposit exploration in small-scale mining in Latin America and other developing countries is performed using underground mining development methods (tunnelling), due to the comparatively high cost of core drilling.

B.2. Existing situation and problem areas

Small-scale mining in the developing countries extracts raw ores from extremely varying deposit types. The following ore-deposit types can be considered suitable for small-scale mining methods:

- alluvial or placer deposits,

- oxidation zones,

- magmatic hydrothermal vein ore deposits with defined veins (which, however, frequently contain complex mineralizations as a result of extreme telescoping),

- pegmatite veins,

- low-sulphide gold-quartz-veins,

- veins with high-grade gold-containing sulphides (which can be enriched into a sulphide concentrate by flotation),

- pneumatolytic and metasomatic deposits.

In can generally be stated that in small-scale mining the individual mineralized parts or excavations are of small dimension. The mine buildings are sometimes so small that the use of technical improve meets in the form of standardized, mechaninized mining equipment is impossible. An example of this is the large tungsten deposit Kami in Bolivia, where numerous small veinlets and associated difficulties in mechanizing the operation have led to a predominantly manual extraction of the ore.

Besides the purely technical problems accompanying nonmechanized mining, small-scale mines, particularly the cooperative mining operations (span: Cooperativas Mineras), also encounter a multitude of organizational difficulties, namely;

- inappropriate extracting/ mining methods,
- low degree of division of labor,
- lack of coordinated efforts.

The organizational problems are especially apparent in the structure devided in "cuadrillas", typically four-man mining teams in the cooperatives. At the Cooperativa Minera Progreso in Kami, it could be observed that every cuadrilla in the cooperative was given the right to mine the portion of the deposit extending above or below of 15 meters drift. This results in unplanned, irregular and totally varying mining activities which have limited advance rates due to the lack of ventilation, supports, etc.

These technical and organizational deficits are responsible for the especially low specific performance rates characteristic of small-scale mining in developing countries. As a result, many small mines, although rich in ore, must be classified as economically marginal operations.

These economical inefficiencies lead to further problems specific to small-scale mining:

- Insufficient safety measures. Deficient cash availability has caused mine operators to save on expenses, particularly in the areas of ventilation and support, as well as in supplying safety equipment for miners.

- The economic problems of miners' families force the women and children to work in the mines (see photo). While women, due to tradition and religious beliefs, are only allowed to work above ground, i.e. in the beneficiation processing activities, children as young as 10 - 12 years old are already working underground mining the ore. These children frequently work in extremely small holes which are inaccessible to adult miners.

- The high exploitation costs and related costs incurred in poorly-organized, manual small-scale underground mining force the operators to more selectively mine only the high-grade zones in the vein. This screening-out method of mining (= highgrading) which follows only the rich portions of ore veins is a form of destructive exploitation which can lead to substantial macro-economic damages. In areas where poorer deposits become inaccessible or are abandoned due to destructive exploitation of rich ores, a later mining becomes technically difficult or if not impossible. Even under changing economic conditions (as for example higher world market prices for mineral resources), the deposits that have been destroyed through exploitation mining practices still may not be mineable. This situation applies only to unorganized small-scale mining of large deposits; the unique macro-economic value of small-scale mining lies in its ability to adapt to small deposits which could not be mined by any other organinized form of mining.

A further goal of the handbook "Tools for Mining" is to help solve the problems associated with small-scale underground mining. Recommended work-organization improvements are presented below which can benefit small-scale mining operators without requiring additional investment costs:

- lowering the cut-off grade,
- extending the life-span of the deposits,
- improving work conditions (increased safety, elimination of child labor practices),
- improving mine productivity,
- increasing incomes, and
- stimulating the economy through job security.

B.3. Organizational measures



B.3.1 USE OF GRAVITY TO REDUCE HANDLING

Small-scale mining frequently employs inefficient loading and transport methods. Loose material is rehandled a number of times through reloading, redumping, relocating. Particularly primitive and unproductive are the mining methods practiced in the small-scale mining cooperatives where the miners are organized into small mining teams (cuadrilla) which work from the haulage level downward. In these mines, hoists are the standard form of ore transport (see photo, Technical Outline 9.1), sometimes being found every 15 - 20 meters. This is a situation in which changes in mining procedures in order to increase production, listed below as a three-fold concept, are not only logical but also necessary:

1. A reorganization which incorporates division of work duties (job specialization) should be established.

2. A mining procedure should be chosen which employs gravity to increase the efficiency of loading and transport activities.

3. Shaft haulage should be centralized where possible; this involves planning and driving of haulage drifts for the transport of raw ore to the haulage shaft or blind shaft.

A planned loading procedure through the use of loading platforms, raise chutes and bunkers can significantly increase mine productivity and reduce loading and transportation costs. Furthermore, a centralization of shaft haulage can simplify a mechanization of the hoisting equipment.

B.3.2 BACKFILL WITH HAND-PICKED ROCKS

Another method for reducing haulage costs is the hand-sorting of waste rocks underground for further use as packing or backfill material in the excavations. In deposits where portions of unmineralized hanging or foot wall also need to be mined, hand sorting can significantly decrease the volume of raw-ore to be transported. Although hand-sorting in small-scale underground mines in developing countries is a frequent occurrence (see photo, bottom), the sorted-out waste material is not always used in the excavations for backfill, but rather hauled separately out of the mine and deposited on the surface. A change in this practice could contribute significantly to lowering transport costs, improving safety at the mining face and, especially in the small manually-operated mines, alleviating drift and shaft haulage activities. Aside from these, a systematic back-filling can also contribute towards improving the ventilation in the mine, for example by filling in old man (abandoned) workings and thereby preventing short circuits in the ventilation flow.

B.3.3 DIVISION OF LABOR IN UNDERGROUND MINING

One basic organizational deficiency in small-scale mining is the frequent lack of work specialization. Especially the cooperatives' "cuadrilla" work procedures repeatedly lead to difficulties due to the parallellism or duplication of work performed by these small mining teams. As a result, a continuous working operation is not possible, and due to economic and organizational necessities, the work activities are limited to a few critical areas. Mining, haulage and beneficiation are performed sequentially, and other essential tasks are negelected for the present time; as a result, work activities such as development of deposits (even where this is possible internally inside the ore-body structure), timbering and maintenance of galleries (see photo) are not performed.

This has the following effects:

- lack of safety in the mining operations


- a steadily worsening mineral-reserves situation which further lowers the ability of the operations to receive credits and further impedes potential investment through exploration funds (e.g. from the Fondo Nacional de Exploracion Minera, FONEM, Bolivia).

These problems can be countered by a systematic division of labor in the mining operations. This normally requires, however, that the existing distrust first be eliminated. This lack of confidence has been the primary cause of failure so far for numerous projects which attempted to promote a cooperative work system, despite the fact that a concept incorporating rotating job responsibilities not only contains components for specialized training, but also most ideally encompasses the cooperative idea.

Furthermore, a system of work specialization could also facilitate essential planning and coordination activities such as ventilation, supply of energy, mine planning and mine safety.

The introduction of work specialization should include the negociation of personnel salaries based on performance or productivity.

B.3.4 COST REDUCTION IN DRILLING, BLASTING, MAULING, CRUSHING

Depending upon deposit geology and existing mechanization and equipment both on the surface and underground, possibilities exist for reducing costs for drilling, blasting, hauling and crushing. The following relationships regulate potential savings within these cost categories:

fewer drill holes per drilling round (lower drilling costs) produces coarser material (higher crushing costs), stronger explosives (higher blasting costs) results in fewer and/or smaller drill holes (lower drilling costs), electrical milk-second detonator (higher detonator costs) yields finer-grained material (lower loading and crushing costs).

In mines with defined veins without impregnation zones, coarser mined materials can make the hand-sorting or backfilling work easier. Optimization possibilities are dependent on the specific mineralization conditions and the technical capabilities of the mine operation.

B.3.5 SELECTING AN APPROPRIATE STOPING METHOD

The primary deficiency in underground mining operations is the lack of mine planning. As a rule, a type of exploitation mining in the form of irregular excavating or room-and-pillar mining is practiced without any prior planning. This results in lower recovery, lack of safety, and adverse macroeconomic effects due to a partial destruction of the deposits. The different mining methods can be classified according to the type of mine development and support and roof-control measures as follows:

Table: Main Classification of Mining Methods

Mining Method

Roof Control


with pillars

with backfilling

with roof caving

Longwall type (50 m and longer advancing face)


longwall mining
inclined cut-and-fill mining
overhand stoping
cut-and-fill stoping

longwall mining

drift type (2-4 m face width, gallery driving)


drift stoping
cut-and-fill stoping
cross cut stoping

cross cut stoping

room-and-pillar type (drifts separated by pillars which are mined in retreat)


pillar mining
cross-cut stoping

pillar mining
sublevel caving
cross cut stoping

panel type (large axially-expanding rooms extending to mine limits boundary)

panel mining
room-and-pillar mining
breast stoping


panel mining
room and pillar stoping
stall pillar stoping
glory hole
sublevel stoping

block type(excavation chamber not open or visible)


block caving with
square sets

block caving

In the following sections, mining methods are presented (according to Stoces) which, under the special conditions of small-scale mining in the Andean region, contribute to lowering costs, increasing productivity, improving the use of resources (through higher recovery) and decreasing the effort required to extract the ore (consequently increasing mine safety).

Pillar mining


Fig.: Development of pillar mining in an inclined deposit. Source: Stoces

Pillar mining is characterized by irregular forms and arrangements of the excavation chambers, determined by the characteristics of the deposit, the chambers being separated by pillars of varying shapes to support the roof.

It can be applied in deposits with competent mineral and host rock.

Room-and-pillar method


Fig.: Room-and-pillar method. Source: Stoces

This mining method is characterized by the development of parallel headings which resemble long drifts in their form and dimensions. The width of the headings depends upon the competence of the host rock and can reach 10 meters; the height can total up to 3 meters.

The individual headings are laid out either parallel to each other, or either perpendicularly or diagonally crossing each other. Support pillars are left between the headings to support the roof. The roof and floor of the headings usually correlate with the hanging and foot walls of the vein being mined; in some cases, however, the mineralization may extend beyond the upper and lower heading boundaries.

This mining method can be applied in flat or slightly-inclined deposits with competent ore and country-rock.

Panel mining


Fig.: Panel mining. Source: Stoces

Within the deposits, only the narrow, long panels are mined, the valuable mineral contained in the support pillars between panels is left unmined. The deposit is normally developed by a main gallery from which other drifts branch off. These drifts are then widened into panels, leaving a stretch of unwidened drift between the main gallery and the panel for support reasons.

This method of mining is characterized by the construction of panels of regular, mostly rectangular shape. These panels are usually larger than headings, being developed according to preplanned, defined measurements.

Support pillars are left between the panels, consisting of either a solid wall (without cross-cuts), or a row of singular pillars (separated by cross-cuts connecting adjacent panels), depending on the method of ecavation employed.

In gently-dipping deposits, either the hanging wall and foot wall, or portions of the mineralized ore itself, form the roof and floor of the panels. In steeply-dipping or massive deposits, the mineralization can extend beyond the chamber boundaries in all directions. The panels can be mined by various methods, for example, a full advance to the final dimension, or with overhand or bench stoping, with or without backfilling or roof caving.

Panel mining can be applied in thick and massive deposits with competent mineral and host rock regardless of dip.

Shrinkage stoping

The blasting is performed from small chambers in the roof of the stope itself which are sunk from the overlying drifts.


Fig.: Shrinkage stope. Source: Stoces

With this procedure, the extracted ores are stored in the excavation chamber for the duration of mining of the individual slopes. The advantages of shrinkage stoping lie in the fact that no support measures are required and recovery is very high. Shrinkage stoping in small-scale mining in the Andean region is particularly suitable where local conditions permit only seasonal execution of certain processing steps; for example where there is a lack of processing water during the dry season, so that raw-ore beneficiation can only be performed in those months with sufficient rainfall.

Sub-level stoping

Sub-level stoping is an irregular form of panel mining.

This method is characterized by the blasting of large chambers, varying in size depending upon the structure and stability of the deposit and the host rock, and therefore, contrary to panel mining, not precisely defined prior to mining. The excavation chamber must be designed so that gravitational forces alone enable the blasted ore to slide down out of the chamber. Only in rare exceptions (for example, in particularly competent host rock) in only slightly inclined deposits, can a scraper be installed to assist in removing the blasted ore from the chamber.

The stoping, contrary to that in the panel stoping method, does not occur within the chamber itself, but rather at the chamber perimeter, either from horizontal sublevels or through long drillholes, since for safety reasons the chamber may not be entered.

The sublevel stoping can be performed either with roof-caving or with backfilling. It is applicable in steeply-diping deposits of lesser or greater thickness, and in flatter, more massive deposits where a required minimum stope height of around 15 meters can be realized.

A sufficient host-rock stability is important since the stopes can only be worked as long as they remain open. Due to the specified minimum sizes of the chambers and the corresponding greater degree of mechanization, sublevel stoping cannot be considered suitable for small-scale mining.


Fig.: Sublevel stoping. Source: Stoces.

Sublevel stoping (sublevel widening and sublevel caving). When competent ore is being mined from sublevel drifts, then mining from the lower sublevels can proceed.

Cut-and-fill stoping


Fig.: One-Sided cut-and-fill stoping of overhand faces with brace support. Source: Stoces.

This type of stoping is defined primarily according to the type of advance and not the shape of the excavated chamber. The overhand stope, which aside from bench stoping is the oldest form of mining, is characterized by the arrangement of the overhand-stope faces in a step-like pattern of advance whereby each stope cuts into the roof of the preceding stope. The floor of the stope generally is constructed with backfill' although in rare cases square sets are employed for chamber support.

Bench stoping (Underhand stoping)


Figure

Bench stoping is sometimes employed for mining smaller regions of deposits which lie below the haulage level where it would be uneconomical to develop additional levels.


Fig.: Bench (or underhand) stoping. Source: Stoces


Fig.: underground bench stoping or glory-hole mining in a steeply-dipplig coal mine in Checua Region, Cundinamarca, Colombia.

This mining method is the graphic opposite of overhand stoping. Here also, the type of development rather than cavity shape characterizes this mining method. The step-like stoping advances in such a manner that each face mines the floor of the preceding one.

In more massive deposits, the bench stoping develops into an underground glory-hole mining without backfill. It is applicable in deposits of smaller thickness and steep dip, and also as underground glory-hole mining in more massive deposits.

Inclined cut-and-fill mining is differentiated from the regular cut-and-fill method only by the inclined position of the face, which occurs as a result of applying this stoping method in steeply dipping deposits.

This method is only applied in steeply-dipping seamlike deposits of smaller thickness.

Inclined cut-and-fill mining


Fig.: Example of double-sided inclined cut-and-fill mining. Source: Stoces

Sub-level caving


Fig.: Sub-level caving. Source: Stoces

This form of stoping is characterized by the drifting of underground sub-levels, aligned underneath each other, separated by vertical distances of two to three times the height of the roadway. Mining progresses, as the name implies, from the top downwards, followed by caving which automatically also advances downward from sublevel to sub-level.

At each sublevel, the mineral is mined by a two-step form of "small panel mining" as follows:

advance mining involving the driving of individual parallel headings (similar to drifts in height and width), which is then immediately followed by retreat mining whereby the in-situ mineral above the sub-level is mined and the pillars between the drifts simultaneously weakened to the furthest extent possible. The stoping can be performed either sequentially, one sublevel after the next, or simultaneously with several staggered sublevels in deposits of sufficient thickness.

The sub-level caving method is predominantly applied in steeply inclined deposits, of smaller or greater thickness, or in rare cases in thick flat deposits.

A comparison of the various mining methods with regard to their technical and economic characteristics is presented below:

In any case, the application of a systematic mining method leads to a reduction in costs and improved mine saftey compared to the visual mining methods currently being used. The selection of one of the above-mentioned mining methods must give serious consideration according to the deposit characteristics.

Table: Compasion of the essential mining parameters of the major mining methods

Mining Costs:

Productivity per man:

(low)

panel mining

(high)

panel mining

­

pillar mining

­

pillar mining

|

abandoned pillar mining

|

abandoneeed pillar mining

|

shrinkage stoping

|

shrinkage stoping

|

overhand cut-and-fill

|

overhand cut-and-fill

|

bench stoping

|

sublevel caving

¯

sublevel caving

¯

inclined cut-and-fill

(high)

inclined cut-and-fill

(low)

bench stoping

Recovery

Preparation:

(high)

cut-and-fill mining

(low)

panel mining

­

shrinkage stoping

­

pillar mining

|

sublevel caving

|

abandoneeed pillar mining

|

pillar mining

|

bench stoping

|

abandoned pillar mining

|

cut-and-fill mining

|

panel mining

|

shrinkage stoping

¯


¯

sublevel caving

Timber Consumption:

Ore Dilution:

(low)

panel mining

(low)

panel mining

­

abandoned pillar mining

­

abandoned pillar mining

|

pillar mining

|

pillar mining

|

shrinkage stoping

|

shrinkage stoping

|

bench stoping

|

cut-and-fill mining

|

cut-and-fill mining

|

bench stoping

¯

inclined cut-and-fill mining.

¯

sublevel stoping(high)

(high)

sublevel caving

(high)

Number of drills


B.3.6 DEVELOPMENT OF FURTHER PORTIONS OF THE DEPOSIT

A factor worth considering for increasing the economically mineable reserves is the possibility of developing parallel mineable seams or areas of the deposit. In the small-scale mining industry in developing countries, exploration of the mined areas of the deposit is only performed where very massive seams or veins are being mined. Only in a few mines are the mine workings designed to accommodate mining of parallel seams or veins. This would be especially favorable, from an economic-geology point of view, for operations where steeply to moderately-inclined seams or veins are being mined, since the steep country-rock layers between the mineralized seams or veins could be penetrated by horizontal cross-cuts. Furthermore, cross-cuts could be driven through the country-rock simultaneously with the ongoing mining activities.

From a mining perspective, the development of parallel seams offers the following advantages:

- simplification of ventilation
- centralization of haulage
- reduction of exploration and extraction costs
- avoidance of water supply and drainage problems.

The mining of parallel seams or veins also permits a postponement of development at greater depths, which characteristically encounters substantial technical difficulties such as advancing into water-bearing levels, higher mining costs due to greater ground pressure, or higher transport costs due to longer haulage distances.

Without exception, the development of the mine should begin with the upper seams or veins, especially in flat or moderately-inclined strata. The mining of underlying seams occurs only after mining and caving of the upper seams has been completed. Only in this way can damage to overlying mineable seams be avoided, caused by fracturing or caving of the roof of the underlying mined seams which results in the overlying seams becoming incompetent and therefore unsuitable for mining. A fracturing and caving of the exposed rock surfaces also in large mined stopes as well can affect the competency of massive country-rock over a distance of several hundred meters. As a result, complete portions of the overlying veins or seams can fracture or cave, rendering them in any event unsuitable for mining. Given this fact, the mining of only one mineralization, for example the thickest seam, can under certain conditions cause major irreversible damage to the economy as a whole.

On the one hand, mine operators should be motivated through consulting efforts to design their mine workings to accommodate parallel mining activities, even if this results, under the circumstances, in temporary economic disadvantages such as postponement in the mining of explored sections. On the other hand, it remains to be investigated whether a small revolving fund with pre-financing capabilities for the purpose of developing the cross-cuts traversing the country-rock could offer sufficient support to the mines in their exploration activities.

B.4 Environmental and health aspects

Mining activities adversely affect the environment both underground and on the surface by polluting air and water.

a) Air Pollution: Contamination of the mine air in small-scale mining of non-iron metallic ores in developing countries is not, as a rule, due to natural causes. Radon emission from host rock and natural radioactivity which occurs, for example, in uranium mining, firedamp gas from methane emission which occurs in coal mining, or CO2 blow outs which occur in salt mining can be disregarded. The main causes of mine-air contamination are man-made, produced by gas emissions from mechanized diesel equipment and vehicles, by oil aerosols generated by direct oiling of compressed-air equipment, and also by blasting fumes. As a result of the explosive reaction of blasting materials, highly toxic nitrous gases are released. To solve these air-quality problems, artificial ventilation is employed, which in small-scale mines in developing countries is often employed insufficiently and operated inadequately. Standard values for minimum air volume should be incorporated here according to the specifications applicable in Europe:

6m³ / man × min

plus

3-6m³/ PS × min

for diesel equipment underground.

In addition, high dust levels further contaminate the mine-air. Quartz-containing country-rock is particularly problematic, in that the respirable quartz fines cause the lung disease silicosis. These respirable dusts are generated during drilling and blasting activities. Wet drilling, wearing of masks, and sprinkling of blasted muck are attempts to minimize these problems. In general, growing mechanization increases dust levels and the associated health hazards.

b) Water Pollution: Contrary to mine-air pollution underground, pollution of mine water directly affects the above-ground ecosystem. Almost without exception, the vein deposits in smaller non-ferrous metal ore mines contain more or less high proportions of sulphide ore minerals or other accompanying minerals. In permeable zones of the vein mineralization, soluble sulfate compounds are formed through oxidation processes (partially stimulated by microbial calatytic reactions); in combination with water these compounds form sulphuric-acidic mine water. The pH-value of this acidic water can reach levels below pH 2. Besides being acidic and containing high levels of sulfates, these waters form solutions containing high levels of heavy metals, some of which are toxic. Furthermore, these waters may also be contaminated with oil from diesel-operated equipment and lubrication of compressed-air machine-tools. One lifer of oil poisons one million lifers of water. This polluted water becomes hazardous when it ends up on the surface or when it comes into contact with the ground water. Serious impacts on unstable, vulnerable ecosystems, for example in the semi-arid high Andean region, cannot be ruled out. Surface water not only serves as processing water for mining and beneficiation, but is also used as a source for drinking water and for irrigation purposes.

Quantitative statements regarding the degree of environmental impact cannot be made since measurement values of pollution levels outside regions of greater population density in developing countries are not available. Measures to alleviate this deficiency are greatly needed.

In addition, general deficiencies are apparent in terms of work safety, namely:

- noise protection during drilling or other mining and transport activities is rare

- safety shoes and helmets (see photo) are not standard equipment

- no safety measures are provided during personnel transport

- safety measures during blasting operations (for example, detonating fuses are too short, etc.) are lacking

- lighting is inadequate (e.g. candles).

The cause for this deplorable state of affairs is not the negligence or mentality of the miners but rather the result of economic pressures.

Increased mine productivity and improvements in ore beneficiation should, above all, also place priority on the implementation and financing of miner health and safety measures.

c) Destruction of Trees and Forests: Lumbering for purposes is one of the major causes of massive destruction of forests in Latin America and elsewhere. This can be countered by application of cheaper, reusable support elements (individual props, such as railroad ties; see technical chapter).

CLOSE THIS BOOKTools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)
Technical Chapter 2: Safety Techniques
VIEW THE DOCUMENT(introduction...)
VIEW THE DOCUMENT2.1 Safety kit

Tools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)

Technical Chapter 2: Safety Techniques

TECHNIQUES APPLIED IN UNDERGROUND MINING

2.1 Safety kit

General Ore Mininig
Underground Mining Safety Technology

Mining and work safety, especially in small-scale mining in developing countries, are sensitive areas frequently characterized by major deficiencies due to cost factors or negligence. The following section presents the safety-equipment components for small-scale mining, categorized according to personnel equipment and general mine equipment. The personal safety equipment should ideally consist of the following:

Helmet - serves as the primary protection from head injuries caused, for example, by falling stones and debris, roof-falls or supports. Mining helmets are made of thermoplastic, such as PE, or fiber-reinforced synthetic resin and are predominantly produced in the developing countries. They have an adjustable inset mounted inside the helmet, with several centimeters of space left in between to accommodate a first-aid kit. The external helmet surface is affixed with a fastener for a cap lamp. The cost of one helmet ranges between 10 and 20 DM.

Safety shoes - with steel-reinforced cap and sole to protect against crushing of the toes or cutting of the foot from sharp objects. In dry working areas leather shoes are preferable, and rubber boots in wet or moist working areas. Locally-manufactured boots are available in most of the mining countries. The cost for one pair varies between 20 and 40 DM.

Ear protectors - against health-damaging noise levels such as those produced by pneumatic drilling. They are available either in the form of a head-piece with attached ear-covers, or in a simpler and cheaper form as absorptive foam-plastic ear plugs which are independently placed directly into the ear.

The following safety items are also necessary, depending upon the type of potential dangers present in the particular work-area:

Shinbone protector - protects against shinbone injuries. It consists of a hard plastic shield placed over the clothing on the shinbone and fastended with two straps.

Hand gloves - to protect hands and fingers from injury.

Protective goggles/glasses - to be worn when danger of eye injuries exists due to flying objects, stone splitters or other particles (e.g. dust from drilling or grinding activities).

Face Mask/Oxygen Mask - with replaceable filter which is placed over the mouth and nose. Especially dangerous is air-transmittable stone dust, which can cut the pulmonary alveolus in the lungs when inhaled. This disease, known as silicosis or "mal de mines", is the most common occupational disease in mining. Dry drilling, blasting and caving are activities which produce extreme amounts of stone dust, requiring not only the use of breathing masks for personal protection, but also sprinkling of the dust sources with water. In less dangerous working areas where smaller levels of dust are prevalent, a soft cloth tied over the mouth and nose frequently serves as a temporary protection.

Knee protectors/Knee shoes - these are only needed as protection in drifts of low roof height where longer stretches need to be travelled via crawling. Knee shoes are made of rubber (sometimes from parts of car tires) and fastened in place with an attached rubber belt.

Filter-Self-rescuer - In some branches of mining, particularly coal and certain salt deposits, dangers to the miner exist in the form of toxic or explosive gas emissions from the country-rock during mining underground. In salt deposits, especially those of tectonic or vulcanic origin, the accumulation of CO2-gas under conditions of high ground pressure can lead to a sudden explosion. CO2 is a toxic, odourless, respiration-inhibiting gas which is heavier than air and therefore collects in the deepest locations. Since the danger of gas explosion is the greatest when the country-rock is loosened by blasting, it is standard practice that blasting in underground salt mines occur during shift change in the absence of mining personnel. As a protection again these gases, every miner carries a filter-self-rescuer which allows him to escape from the toxic fumes to the surface in the event of an explosion. In coal mining, the occurrence of underground fires can likewise lead to the danger of high levels of CO and CO2 gas in the mine air, use of the filter-self-rescuer offers protection against these gases during escape as well. CO and methane gas, emitted from the seam or country-rock, are both explosive as fire damp in certain concentrations. In order to avoid mine gas explosions, flameproof electrical equipment, permissable explosives, continual measurement of the gas content in the mine air, and extensive ventilation of the gob are necessary. Coal dust can also become explosive when present in whirling air vortexes.

Gas Measuring Devices - to measure mine gas concentrations. Measuring appratuses are available on the market either as small rechargeable electrical meters for taking single or continual measurements, or as larger measuring devices equipped with a graduated pipe and bellow pump for taking single measurements.

For the first device, the investment costs are higher, whereas for the second, the operating costs are higher. For the Indirect measurement of methane gas, gasoline safety lamps can also be used (see 6.1).

The mine safety equipment should include the following items:

Personnel tags - small numbered metal tags which hang on a check-in/check-out board near the shaft or mine entrance. One side of the board holds the tokens for those workers currently in the mine, the other side for miners who are not in the mine at the time. Every miner has a tag with his own number or name, and personally hangs it on the appropriate board every time he enters or leaves the mine. In the event of an accident, or prior to blasting, this personnel-control system allows immediate determination of which workers are currently in the mine.

Scaling rods · a basic component of the safety equipment in underground mining, used to pry off loose rock pieces from the roof and headings caused by blasting or the effects of ground-pressure. Scaling rods, like crow bars, are applied by inserting the tip in the fracture between the loosened portion and the country-rock, and prying until the loose rock falls. Old drill-rods with a sharpened tip can be employed as scaling bars in small openings or drifts, whereas lighter, longer aluminum pipes with a chisel tip are used in larger cavities. Fundamentally, scaling should be performed after every blasting round before any other activity is undertaken. Thereby, the blasted debris provides easier access to the roof. These simple safety precautions significantly Increase work safety, decreasing the risk of accidents.

First-Aid Kit - with an assortment of medicines and adhesive plasters, bandages and splints for treatment of injuries.

Stretcher - to rescue injured miners.

Gas Protection Equipment - for use by the mine-rescue team in emergency situations, these are practical in small-scale mining In developing countries only if miners are trained in mine-rescue operations. This safety measure, however, is frequently not implemented by the individual mine operators in developing countries.

CLOSE THIS BOOKTools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)
Technical Chapter 3: Ventilation
VIEW THE DOCUMENT3.1 Bricked brattice, bricked duct
VIEW THE DOCUMENT3.2 Small blowers, manual fans
VIEW THE DOCUMENT3.3 Air-jet ventilator
VIEW THE DOCUMENT3.4 Hydro-compressor
VIEW THE DOCUMENT3.5 Ventilation oven
VIEW THE DOCUMENT3.6 Wind sail
VIEW THE DOCUMENT3.7 Box blower
VIEW THE DOCUMENT3.8 Bell blower baaders blower

Tools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)

Technical Chapter 3: Ventilation

3.1 Bricked brattice, bricked duct

Deep Mining in Solid Rock
Underground Mining Ventilation

germ.:

Streckenscheider, gemauerte Lutte

span.:

canal de ventilacion embovedado, huayrachina, huayracanyon

TECHNICAL DATA:


Dimensions:

air channel approx. 30 cm in width × 70 cm in height

Extent of Mechanization:

not mechanized

Form of Driving Energy:

differential air pressure and temperature

Alternative methods:

blowing or exhaust ventilation

Mode of Operation:

continuous

Operating Materials:

contruction material

Type:

rough rocks, loam

ECONOMIC DATA:


Investment Costs:

labor costs only

Operating Costs:

none

Related Costs:

none for mechanized ventilation fans

CONDITIONS OF APPLICATION:

Operating Expenditure:

low |————|———| high

Maintenance Expenditure:

low |———|————| high

Personnel Requirements:

none

Location Requirements:

none

Ore Requirements:

none

Host Rock Requirements:

Larger host-rock fragments should be generated during blasting for


use in constructing the duct (huayrachina), requiring that the mine's

drilling scheme be adjusted accordingly

Regional Distribution:

In earlier times, widely distributed in Latin America

Environmental Impact:

low |———|————| very high

Suitability for


Local Production:

very good |———|————| bad

Under What Conditions:

limited to construction of the duct (huayrachina)

Lifespan:

very long |———|————| very short

Bibliography, Source: Priester, Schauroth, Ponson, Winkelmann

OPERATING PRINCIPLE:

Huayrachina is a bricked duct erected on one side of the roadway floor. This method is suitable for ventilating mines with only one opening to the surface. On the surface, the huayrachina ends in a chimney or short ventilation raise in order to achieve the required pressure differential.

AREAS OF APPLICATION:

For ventilation of drifting or tunnelling operations. For ventilation of isolated activities in mines with natural ventilation.

REMARKS:

The natural mine ventilation is a natural air current which automatically replaces the mine air without human intervention. Natural ventilation is possible when a mine has at least two openings located at different topographic elevations. In special cases, natural ventilation can also temporarily occur in deep mines with two shaft or roadway openings of the same elevation. Natural ventilation results primarily from differences in temperature (and therefore air density), and secondarily from variations in humidity and air pressure, between the inside and outside air. Whereas in summer the air current normally flows In from the opening at the higher elevation through the mine to the lower opening, this flow pattern reverses direction In the winter months (see Fig. 3.2). The air current in deeper mines is stronger in winter than in summer.

The Huayrachina is suitable for blowing (forced) as well as exhaust ventilation.

Materials for constructing the wall are taken from the gob, which minimizes the transport distances required for the stones used to build the huayrachina and simultaneously reduces the volume of gob.

A disadvantage of this bricked brattice ventilation system is the inhomogeneity of cross-sectional areas and rough Inner surfaces of the huayrachina, resulting in high friction losses. In order to mechanize the ventilation, larger-capacity blower fans are therefore necessary.

A similar method of ventilation was applied already in the old Japanese gold mine of Sado, where two parallel drifts at an interval of approx. 0.5 m served to ventilate the mine.

SUITABILITY FOR SMALL-SCALE MINING:

Given the prerequisite of low labor costs, this method is appropriate even today, particularly for small-scale mining operations In Latin America. The ability to ventilate with exhaust fans, together with the almost unlimited lifespan and minimal cost of materials, fulfill the requirements for small-scale mining application.

3.2 Small blowers, manual fans

Deep Mining General
Underground Mining Ventilation

germ.:

Kleine Wetterlufter, Wetterrad, Facher, Facherceblase, Centrifugalgeblase, Windtrumel, Focher

span.:

pequeno ventilador manual, rueda pare ventilacion, abanico, fuelle abanico, fuelle centrifungal, ventilador manual

TECHNICAL DATA:


Dimensions:

approx. 0.5 × 0.5 × 0.5 m

Weight:

approx. 20 kg

Extent of Mechanization:

not mechanized or mechanized

Power Generated:

80 W or more

Form of Driving Energy:

manual, pedal or with a small electric, pneumatic or internal- combustion engine

Mode of Operation:

continuous

ECONOMIC DATA:


Investment Costs:

probably around 500 DM (estimated value) when locally manufactured

Operating Costs:

labor costs only

Related Costs:

ducts, huayrachina, etc.

CONDITIONS OF APPLICATION:

Operating Expenditure:


low |————|———| high

Maintenance Expenditure:

lubrication

low |———|————| high

Location Requirements:

independent of location


Mining Method Requirements:

due to the relatively small air-flow volume, should not be employed where larger open exacavation chambers exist to ensure a complete air exchange.

Replaces other Equipment:

Other mechanized types of ventilation blower-fans For mining activities.

Regional Distribution:

Earlier, generally widely distributed, today used only seldom for auxiliary ventilation.

Operating Experience:


very good |———|————| bad

Environmental Impact:


low |———|————| very high

Suitability for



Local Production:


very good |———|————| bad

Under What Conditions:

qualified metal workshops where the fan-rotors, gears, etc. can be manufactured.

Lifespan:


very long |———|————| very short

Bibliography, Source: Delius, Schauroth, DBM, v. Hauer, v. Humbolt

OPERATING PRINCIPLE:

Different types of centrifugal and axial-flow fans which circulate and displace the air by means of rotating blades. In centrifugal fans, air is drawn in near the blades' center of rotation where it is rotated, compressed and finally expelled outward due to inertia. With axial-flow fans, the air is tangentially accelerated by the rotating fan blades in an axial direction due to the generation of a pressure differential (higher pressure on the inner side of the blades where expelled air is compressed, and lower pressure at the suction side of the blades where the expelled air creates a vacuum).

AREAS OF APPLICATION:

Complete ventilation of mines.
Auxiliary ventilation.

REMARKS:

Manual fans are available from Delius (radial air compressor).

Manual fans were industrially produced in Germany until the beginning of this century (Pelzer, Wulf, Mortier) and were driven by means of cranks and gears up to velocities of 650 rpm.

SUGGESTIONS FOR DESIGN:

To serve as a gear drive, spur gears were placed at the rotor periphery. For pedal-driven fans, a chain-coupling would suffice, such as a bicycle chain.

SUITABILITY FOR SMALL-SCALE MINING:

For small-scale and minimally-mechanized operations, a manual or pedal-driven fan which is manufactured locally offers the possibility to ventilate artificially at low investment cost and without external energy input.


Fig.: Principle of natural ventilation (left, flow in winter; right, flow in summer). Source: Armstrong.


Fig.: Small fans: left a pneumatic fan, right an electric fan. Source: Armstrong


Fig.: A comparison of different fan types (in cross-section); high-pressure fan (above), equal-pressure fan (below)

3.3 Air-jet ventilator

Deep Mining General
Underground Mining Ventilation

engl.:

injector fan, venturi fan, air driver, venturi blower

germ.:

Luftstrahigeblase, Pneumatisches Strahlgeblase

span.:

ventilador neumatico de inyeccion

Producer:

Turmag

TECHNICAL DATA:


Dimensions:

diameter 200 mm, length 550 mm with 3 nozzles of 2-mm diameter

Extent of Mechanization:

fully mechanized

Form of Driving Energy:

compressed air, pneumatic

Mode of Operation:

continuous

Output/Performance:

air volume of 55 m³/min; fan type Altenkamp (1921) delivered 256.9 m³/min, intake fan: 0.667 m³/min

Technical Efficiency:

somewhat less than that of pneumatic turbofans

Operating Materials:


Type:

compressed air to 4 bar

Quantity:

1.6 m³/min

ECONOMIC DATA:


Investment Costs:

If locally made, estimated to be as low as 400 DM; for Turmag fan, 618 DM + sales tax

Operating Costs:

costs to compress air

Related Costs:

costs of ducts

CONDITIONS OF APPLICATION:

Operating Expenditure:

low |———|————| high

Maintenance Expenditure:

low |———|————| high

Location Requirements:

independent of location

Mining-


Method Requirements:

Due to the relatively small pressure gradient between the intake and exhaust sides of the fan, the length of the ducts is limited (maximum of 100 m for a 200 - 300 mm duct) therefore, the mining procedure must be so designed as to ensure that a fresh-air intake is within close proximity of the area to be ventilated.

Replaces other


Equipment:

other ventilators, manual as well as mechanized fans

Regional Distribution:

low

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |———|————| very high

Suitability for Local Production:

very good |———|————| bad

Under What Conditions:

requires qualified metal and welding workshops

Lifespan:

very long |———|————| very short

Bibliography, Source: DBM, manufacturer's information, Stout, Armstrong

OPERATING PRINCIPLE

Compressed air is blown through one or more small nozzles (2 - 3 mm 0 or larger) into an expansion chamber of the air driver. As the compressed air expands it draws additional air into the chamber, which has the form of a laval turbine. The ratio between compressed air and the quantity of air drawn in can reach 1 : 35.

AREAS OF APPLICATION:

Ventilation and auxiliary ventilation of mines, working faces or roadways with relatively short duct lengths.

REMARKS:

Air-drivers or infector fans are stable and have a long lifespan as a result of their simple design, which involves no driven moving parts. Therefore maintenance is minimal and potential repair work is simple.

SUITABILITY FOR SMALL-SCALE MINING:

For pneumatically-mechanized mining operations with small workings, locally-made air-drivers are superior to other pneumatic ventilators due to their stable design and maintenance-free operation.


Fig.: Design of an Air-driver. Source: Armstrong

3.4 Hydro-compressor

Deep Mining General
Underground Mining Ventilation

germ.:

Wassertrommel, Hydrokompressor, Althaus'Geblase

span.:

toner de aguacompresor, hidrocompresor fuelle de Althaus

TECHNICAL DATA:


Dimensions:

approx. 3 m × 1 m × 1 m (HWL)

Weight:

approx. 100 kg

Extent of Mechanization:

not mechanized

Form of Driving Energy:

hydromechanic

Mode of Operation:

continuous

Throughput/Performance:

small capacities

Technical Efficiency:

substantially higher than other compressors, 8 - 15 % for a simple hydro-compressor

Operating Materials:


Type:

water

Quantity:

relatively high

ECONOMIC DATA:


Investment Costs:

highly dependent on air pressure (higher pressure requires longer pipelines and better quality)

Operating Costs:

none

Related Costs:

for operation of compressor very high

CONDITIONS OF APPLICATION

Operating Expenditure:

low |———|————| high

Maintenance Expenditure:

low |———|————| high

Operator Experience:

little

Location Requirements:

requires water and a sufficient elevation difference

Mining Requirements:

A shaft is a prerequisite for the use of hydro-compressors.

Replaces other Equipment:

fan, small compressors

Regional Distribution:

No longer in use today; distributed throughout Central Europe earlier.

Operating Experience:

very good |———|————| bad

Environmental Impact:

low |———|————| very high

Suitability for Local Production:

very good |———|————| bad

Under What Conditions:

carpenter shop for fans, qualified metal workshop for compressors and fans

Lifespan:

very long |———|————| very short

Bibliography, Source: Calvor, v. Bernewitz, Slotta in Eckholdt, Delius, Kircher, v. Hauer, Cancrinus, Wagner

OPERATING PRINCIPLE:

The water falls into a closed barrel where it strikes a reflecting plate, separating it from the air which has been drawn along with the water; this air is then directed through a duct to the working face.

The air-collection system can be designed using a water-jet pump (injector pump) of tubular construction (Bernewitz).

AREAS OF APPLICATION:

Blowing (forced) ventilation of smaller mines.
As a small compressor for revolution of slurries, reagents etc. according to the air-lift pump principle.

SPECIAL AREAS OF APPLICATION:

As a compressor to produce compressed air for driving pneumatic motors.

REMARKS:

Hydro-compressors were in operation until the early 1980s in the Harz Mountains mining region in Germany, whereby the output capacity of around 11 m³/min or 16.3 m³/min was somewhat low. The air pressure sufficed, however, for pneumatic drive units.

When used to generate compressed air, the separating of the air must occur under pressure, which is created by means of a standpipe for the expelled water. The height of the standpipe determines the pressurization of the compressed air.

SUITABILITY FOR SMALL-SCALE MINING:

The hydro-compressor for ventilation is a simple, stable apparatus without moving parts; it is locally available and suitable for small-scale mining. Prerequisites for its use, without exception, are the presence of water and an elevation gradient.

Its use as a compressor to produce compressed air appears less suitable due to the high construction costs. In situations where conditions permit the construction of a hydro-compressor (water, sufficient elevation gradient), a turbine-driven conventional compressor is probably more economical than a hydro-compressor for generating compressed air.


Fig.: Waterdrum for ventilation porposes, by Cancrinus


Fig.: A Small hydro-compressor for operating a cirulating pump according to the air-lift-pump principle for circulation of agitation-leaching solution. Source: Bernewitz


Fig.: Working principle of a waterdrum for ventilation purposes, by Wabner


Fig.: A waterdrum for ventilation purpose. Source: Calv�r

3.5 Ventilation oven

Deep Mining General
Underground Mining Ventilation

engl.:

furnace ventilation

germ.:

Bewetterungsofen, Bartels Feuermaschine, Wetterofen

span.:

horno de ventilacion

TECHNICAL DATA:


Dimensions:

large oven-house or furnace with a chimney several meters high, or preferably underground oven in a by-pass with approx. 4 m hearth area

Extent of Mechanization:

not mechanized

Form of Driving Energy:

wood or coal-fired

Alternative Forms of Energy:

gas, oil

Mode of Operation:

semi-continual

Technical Efficiency:

20 - 80 % (in English mines)

Operating Materials:


Type:

wood or coal

Quantity:

large, 30 - 50 k9/PSuseable × h

ECONOMIC DATA:


Investment Costs:

high

Operating Costs:

high, due to high fuel costs

Related Costs:

intake ducts, huayrachinas when only one opening exists

CONDITIONS OF APPLICATION:

Operating Expenditure:

low |————|————| high

Maintenance Expenditure:

low |———|————| high

Location Requirements:

wood or coal fuel must be available in sufficient quantities

Deposit Requirements:

only suitable for small excavation areas due to the small intake capacity

Mining Requirements:

the mining procedure must be so designed that only small excavation chambers are created

Replaces other


Equipment:

fans

Regional Distribution:

historically used in Europe

Operator Experience:

very good |———|————| bad

Environmental Impact:

low |————|———| very high

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

adobe construction, metal hearth-grates

Lifespan:

very long |————|————| very short

Bibliography, Source: Henning Calvor, Delius, A. v. Humboldt, Schauroth, Wagner

OPERATING PRINCIPLE:

The fire in the oven heats the air which then escapes through the chimney, drawing mine-air along with it; ducts direct the mine-air into the oven. Based on convection principle.

AREAS OF APPLICATION:

Exhaust ventilation of small mines where sufficient coal or wood is available. Also suitable as supplementary support for natural ventilation.

REMARKS:

It remains to be investigated if the effects of convective flow could be achieved through the use of solar energy (e.g. air collectors).

Ventilation ovens of this type are suitable for non-coal mining only in regions of abundant vegetation; unsuitable for regions of higher elevation with low vegetation density.

Use of ventilation ovens is appropriate especially in coal mining, where even products of poor market quality (for example, coal with high ash contents or poor carbonization, etc.) can be employed for firing the ventilation ovens.

Ventilation ovens have not only been constructed on the surface, but also underground, where the entire shaft served as a chimney, making this type of ventilation significantly more effective. The ventilation oven was in this case installed in a by-pass In a slightly-ascending roadway, whereby the correct quantity of air needed for combustion was regulated by ventilation doors and gates. The heat loss from the ovens is predominantly dependent on the humidity of mining air, leading to fluctuations in the efficiency between 80% in dry ventilation shafts to 20% in wet shafts.

An alternative method was also investigated in which the heat generated by coal combustion was used to heat water and convert it to steam, which then flowed under high pressure into an injector fan (jet-stream fan by Korting), drawing mine air along with it. The effect of this arrangement was however only minimal (efficiency only 2 % that of the ventilation oven).

SUITABILITY FOR SMALL-SCALE MINING:

Ventilation ovens are not recommended for small-scale mining because of their detrimental impact on vegetation. In isolated cases, the use of ventilation ovens in coal mines may be appropriate, however the associated risk of mine fires must be taken Into consideration.


Fig.: Above-ground ventilation oven, by Wabner


Fig.: Installation of underground ventilation oven in by-pass roadway, by Wabner


Fig.: Elevation and section of ventilation oven constructed underground. Source: Wabner


Fig.: Ventilation oven or Bartel's Fire Machine. Source: Calv�r

3.6 Wind sail

Deep Mining General
Underground Mining Ventilation

germ.:

Bewetterungssegel, Windsegel, Machina Anemica, Windfang, Wetterhut

span.:

vela de ventilacion, vela de viento, machine anemica, cortaviento

TECHNICAL DATA:


Dimensions:

up to several m in diameter

Weight:

10 - 50 kg

Extent of Mechanization:

not mechanized

Form of Driving Energy:

wind

Mode of Operation:

intermittent

Throughput/Performance:

depends on resistance of the duct/huayrachina

Technical Efficiency:

high

ECONOMIC DATA:


Investment Costs:

very low

Operating Costs:

none

Related Costs:

an alternative ventilation system may be necessary; ducts or huayrachina must be installed

CONDITIONS OF APPLICATION:

Operating Expenditure:

low |————|————| high

Maintenance Expenditure:

low |————|————| high

Location Requirements:

locations of mine or shaft openings must be characterized by sufficiently strong daily and seasonal winds

Mining Requirements:

mine has to be designed for blowing (forced) ventilation

Replaces other Equipment:

mechanized types of fans, natural ventilation

Regional Distribution:

Australia

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

carpentry and/or other workshops where the manufacture of textile sails and wooden or metal frames can be combined

Lifespan:

very long |————|————| very short


given that the construction is storm-resistant

Bibliography, Source: Armstrong, Kircher, A. v. Humboldt, Loehneyss, Schauroth, Wagner

OPERATING PRINCIPLE:

A funnel-shaped extension of the duct is oriented with its opening toward the wind. The creation of a pressure head causes air to flow into the duct. The windsail is constructed of wind-permeable materials such as sail cloth, coated cotton or linen, or fiber-reinforced synthetic material. The wooden or metalic frame keeps the funnel open.

MODES OF OPERATION:

Ventilation of small mines where ducts or huayrachinas are present.

REMARKS:

During periods of insufficient winds, non-wind-dependent auxiliary ventilation equipment must be available.

Kircher describes a Machina Anemica, which is a wooden wind sail automatically aligned by use of a tail fin.

Schauroth indicates that combination blowing and exhaust ventilation sails have already been constructed, the simplest being at the opening of the shaft or drift, whereby the doors and gates were opened on the windward side for exhaust ventilation and on the leeward side for blowing ventilation.

Windsails are historically the oldest form of artificial mine ventilation.

Windsails of textile-construction, such as those currently used in small-scale mines in Australia, are preferable to those of wooden construction.

Aside from the mechanics for turning the opening toward the wind direction, windsails do not have moving parts and are therefore of sturdy construction. They should be designed to accommodate the strongest occurring winds.

In downcast ventilating shafts in dry locations, ventilation can be enhanced by cooling the intake air with a fine water mist which is sprayed Into the shaft. The evaporation effect cools the air flow; the higher the air temperature and the lower the relative humidity, the stronger the cooling effect.

SUITABILITY FOR SMALL-SCALE MINING:

The use of wind sails in Latin American small-scale mines is only practical where sufficient winds occur on a regular daily or seasonal basis near the shaft or mine entrances.


Fig.: Types of historical windsails applied primarily for bowing ventilation.

3.7 Box blower

Deep Mining General
Underground Mining Ventilation

germ.:

Kastengeblase

span.:

soplador de cajon

TECHNICAL DATA:


Dimensions:

e.g. 3 square pistons, 1 × 1 m surface area; box: 4 × 1.2 × 5 m LWH

Weight:

approx. 1,000 kg

Extent of Mechanization:

partly mechanized

Power:

starting at approx. 0.5 kW

Form of Driving Energy:

waterwheel (as for the box Freiberg) blower of above-mentioned dimensions in

Alternative Forms:

other slow-moving driving mechanisms

Mode of Operation:

semicontinual

Technical Efficiency

420 m³/h air volume with 450 mm water column pressure

Operating Materials:


Type:

lubricant

Quantity:

small quantities

ECONOMIC DATA:


Investment Costs:

approx. 2,000 DM

Operating Costs:

depends on drive-system, however generally very low

Related Costs:

drive-system, air channel system (ducts, etc.)

CONDITIONS OF APPLICATION:

Operating Expenditure:

low |————|————| high

Maintenance Expenditure:

low |————|————| high

Replaces other Equipment:

all other blower systems for auxiliary ventilation

Regional Distribution:

to date not distributed in the Latin American small-scale mining industry

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

as traditional wooden system, possibly also produceable as plastic, fiberglass-reinforced resin, etc; valves of leather and felt for sealing, possibly also of rubber.

Lifespan:

very long |————|————| very short

Bibliography, Source: Wagenbreth, Grube Alte Elisabeth/Freiberg

OPERATING PRINCIPLE:

Air contained in the compression chamber of the wooden box is compressed by tightly-fitting wooden pistons which work in two opposite directions. Each wooden box accordingly has an inlet and an outlet valve for each of the two compression chambers, which are separated by the piston in between. As the piston travels in one direction, the air in front of it is compressed and driven out through a simple flap valve. When the piston has reached the end of the stroke and reverses direction, the flap valve closes gravitationally and the suction valve opens due to the pressure drop behind the piston, letting fresh air into the chamber. In the other chamber, now in front of the piston, the air is compressed and then driven out the respective flap-valve in that chamber. With each piston stroke and corresponding direction change, air is alternately compressed and expelled from the one chamber while fresh air is drawn into the other. A cross head Joint assures that the pistons travel parallel to their axis. As an alternative, Watts' parallelogram system can be used in conjunction with a beam.

Box blowers are generally constructed in an upright position where the driving-axle is vertical; all other constructions have experienced significantly higher friction losses and sealing problems.

AREAS OF APPLICATION

Compressing of air for ventilation and forge furnaces

SUITABILITY FOR SMALL-SCALE MINING:

Box blowers are suitable for ventilation of small mines where waterwheels or slow moving drive-systems exist.


Fig.: Box blower for ventilation, driven by a steam engine with balancing beam and Watt's Parallelogram construction, by Wabner


Fig.: Horizontal box blower, by Wabner

3.8 Bell blower baaders blower

Deep Mining General
Underground Mining Ventilation

germ.:

Glockengeblase, Harzer Wettersatz, Baader'sches Geblase

span.:

soplador de campana, equipo pare ventilacion del Harz, soplador de Baader

TECHNICAL DATA:


Dimensions of one blower unit:

approx. 1 m in dia., 2 - 3 m in height

Driving Output:

100 W or more

Extent of Mechanization:

not or semi-mechanized

Form of Driving Energy:

manual or hydromechanic

Alternative Forms:

pedal drive, animal-powered gear

Mode of Operation:

intermittent

Throughput/Performance:

per stroke approx. 2 m³ air, frequency approx. 6 strokes/min

Technical Efficiency:

very high, due to low frictional losses

ECONOMIC DATA:


Investment Costs:

very low, < 550 DM

Operating Costs:

dependent upon extent of mechanization

Related Costs:

duct, conduit or huayrachina nessesary

CONDITIONS OF APPLICATION:

Operating Expenditure:

low |————————| high


depending upon extent of mechanization

Maintenance Expenditure:

low |————|————| high

Personnel Requirements:

low

Location Requirements:

none

Replaces other Equipment:

natural ventilation, blower

Regional Distribution:

historical only (Harz, Germany)

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

simple metal or wood manufacturers, leather or rubber valves

Lifespan:

very long |————|————| very short

Bibliography, Source: German Museum, Slotta in Eckhlodt, A. v. Humboldt, v. Hauer, Schauroth, Wagner, Treptow

OPERATING PRINCIPLE:

A small, bottomless bell-shaped or cylindrical container is continually moved up and down in a water bath within a larger open-topped container. This causes a constant increase or decrease of air space volume in the upper portion of the inside vessel, like a bellow. A pipe connecting the ventilation duct to the head of the inner container is equipped with valves to direct the air flow.

AREAS OF APPLICATION:

Ventilation and auxiliary ventilation in small mines and drifts.

REMARKS:

In the 18th century in the Harz mining region in Germany, drifts up to 3 km in length were ventilated with Baaders blowers (invented by Josef Baader, 1789). At that time, wooden ventilation ducts (hollowed out logs) were used which were connected and sealed with metal rings.

Depending on the valve type, exhaust or blowing (forced) ventilation is possible. The simultaneous operation of two Baader's blowers counterposed on a tilting beam can produce a continual air flow. Compared to all other designs of bellows, box blowers, etc., Baader's blower is distinguished by its very low friction losses and high performance efficiency.

It would be worth investigating to what extent Baader's blowers could be animal-powered.

SUITABILITY FOR SMALL-SCALE MINING:

Low investment costs, a simple operating principle and its suitability for local production make Baaders blower appropriate as one of the simplest method for artificial ventilation. Slowly-moving drive systems are most suitable.


Fig.: Design section of a bell-shaped blower. Source: Slotta, in: Eckhold


Fig.: Schematic diagram of a Baader's blower (Harzer Wettersatz). Source: Lempe

CLOSE THIS BOOKTools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)
Technical Chapter 4: Water supply and drainage
VIEW THE DOCUMENT4.1 Pneumatic positive-displacement pump
VIEW THE DOCUMENT4.2 Chinese liberation pump
VIEW THE DOCUMENT4.3 Water bag
VIEW THE DOCUMENT4.4 Bucket-chain conveyor
VIEW THE DOCUMENT4.5 Pneumatic high-pressure pump

Tools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)

Technical Chapter 4: Water supply and drainage

4.1 Pneumatic positive-displacement pump

Deep Mining General
Underground Mining Mine Drainage

engl.:

floating pump

germ.:

Druckluftgetriebene Verdrangungspumpe, Schwimmerpumpe

span.:

bomba neumatica de expulsion, bomba con flotador

TECHNICAL DATA:


Dimensions:

volumes ranging from a few lifers up to several 100 lifers

Weight:

the total weight of the pump's displacement chamber should be greater than that of the volume in lifers, so that the pump sinks down when it's empty

Extent of Mechanization:

semi-mechanized

Form of Driving Energy:

pneumatic

Mode of Operation:

intermittent

Technical Efficiency:

relatively low, due to the low efficiency of compressed air; furthermore, the intermittent operation results in a loss in the built-up air pressure relative to standard pressure

Operating Material:


Type:

compressed air

Quantity:

P = P hydrostat + (0.5 - 1.0) bar

ECONOMIC DATA:


Investment Costs:

very low, approx. 100 DM + pipe costs = f (height)

Operating Costs:

f (costs for compressed air)

Related Costs:

Compressed air system, compressor

CONDITIONS OF APPLICATION:

Operating Expenditure:

low |————|————| high

manually operated


Maintenance Expenditure:

low |————|————| high

Personnel Requirements:

low

Location Requirements:

theoretically, greater pumping depths are possible; in practice, the compressive strength of the material and the maximum compressed-air pressure limit the depth to 50 m.

Replaces other


Equipment:

other types of pumps for mine drainage, and for pumping of processing and mill water in smaller volumes but over greater heights.

Regional Distribution:

new technology, so far not distributed

Operating Experience:

low |————|————| very high


non-existent; only test operations performed in Landtechnik


Weihenstephan (Germany)

Environmental Impact:

low |————|————| very high


oil-contamination of water due to leaking oil from the compressed air system

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

metal workshop employing simple components, e.g. pipe sections, simple ball valves employing hard rubber balls.

Lifespan:

very long |————|————| very short

Bibliography, Source: Landtechnik Weihenstephan, Fritzsche

OPERATING PRINCIPLE:

The pump consists of a displacement chamber with two valves: an intake valve with protective sand filter and an outlet valve with an uptake on the delivery side of the pump. The intake and discharge are located at the bottom of the pump housing, where a standpipe serving as the outlet has proven to be best. The valves are designed as check-valves, e.g. as flap valves or ball valves. The latter for example, should be constructed with rubber balls of a density only slightly higher than water allowing them to open at even the smallest pressure increase on the intake side. A compressed-air line, externally-controlled by means of a three-way cock, is connected to the pump chamber. Water from the mine sump flows through the intake valve into the pump chamber, when the pump chamber is full, the three-way cock is turned to allow compressed air to flow into the chamber. The intake valve closes and the outlet (discharge) valve starts to open, whereby the compressed air drives the water out through the standpipe, outlet valve and uptake pipe. After all the water has been discharged, the three-way cock is switched open, the air pressure drops, the outlet valve closes, the intake valve begins to open and water again flows into the pump chamber. The manual three-way-cock pump control can be automated by means of floats.

ADVANTAGES:

+ can be self-made or locally-produced using inexpensive material

+ can be applied in narrow shafts, drill holes or pump sumps since the pump is suspended only by two flexible hoses, and perhaps additionally by a rope or cable

+ less susceptible to break-downs since, except for the valves, there are no moving parts

+ can be controlled manually in its simplest construction

DISADVANTAGES:

- lower efficiency than directly-driven piston or diaphragm pumps

Proposals for optimization: a three-way cock at the pump housing, controlled for example by a mechanical transmission, decreases the depressurization volume and therefore increases efficiency.

SUITABILITY FOR SMALL-SCALE MINING:

Suitable for handling small quantities of water, under the condition that a compressed-air system and compressor are already available; otherwise, robust pneumatic immersible pumps are superior.


Fig.: Float pump, Reuter


Fig.: Compressed-air pump, Landtechnik Weihenstephan (Germany)

4.2 Chinese liberation pump

Deep Mining General
Underground Mining Mine Drainage

germ.:

Seilpumpe, Heinzenkunst

span.:

bomba de mecate

Producer:

Campo Nuevo, FCAP-UMSS

TECHNICAL DATA:


Dimensions:

down to 15 m depth

Weight approx.:

150 kg

Extent of Mechanization:

not mechanized

Form of Driving Energy:

manual

Alternative Forms:

hydromechanic, pedal drive, animal-powered whim

Mode of Operation:

continuous

Throughput/Performance:

low output quantities, e.g. for 5 m 10 m³/h

Technical Efficiency:

approx. 75 %

ECONOMIC DATA:


Investment Costs:

approx. 200 DM

Operating Costs:

labor costs only

CONDITIONS OF APPLICATION:

Operating Expenditure:

one person

low |————|————| high

Maintenance Expenditure:


low |————|————| high

Personnel Requirements:

low


Location Requirements:

none


Mining Requirements:

water must be pre-clarified in a sump. Coarser suspended solids lead to excess wear of the standpipes.

Replaces other Equipment:

other pumps


Regional Distribution:

seldom used in Latin America, distributed worldwide in the agricultural industry

Operating Experience:


very good |————|————| bad

to date, the only experience is from the agricultural sector (for irrigation) and from conveyance of drinking water from wells

Environmental Impact:


low |————|————| very high

Suitability for Local Production:


very good |————|————| bad

Under What Conditions:

village workshops. Materials: PVC pipes, nylon rope, rubber

Lifespan:


very long |————————| very short

Bibliography, Source: PAAC, Fraenkel, Agricola, Cancrinus

OPERATING PRINCIPLE:

A rope with rubber disks runs around an upper drive pulley and a lower return pulley through the sump. The upward-travelling portion runs through a PVC pipe, carrying water with it between tightly-fitting rubber flaps.

Comparable to 'Heinzenkunst' by Agricola, one of the early forms of mine drainage pumps during the end of the Middle Ages. Rods were made of wood or iron chains and the water-transport vessels of leather.

AREAS OF APPLICATION:

Mine drainage at pump depths of 10 - 15 m.

SPECIAL AREAS OF APPLICATION:

Recirculation of plant water.

REMARKS:

For technical reasons due to excessive wear, Chinese Liberation Pumps or 'Heinzenkunste' have been displaced. Modern materials, however, such as PVC-pipes, etc., can produce long-lasting designs.

The efficiency of the pump decreases with increased transport distances as a result of increasing frictional losses and weakening of the seal in the cells. Therefore the maximal conveying distance is limited to approx. 15 m. The primary range of appilcation is to a depth of around 2 - 5 m.

SUITABILITY FOR SMALL-SCALE MINING:

'Heinzenkunst' can be applied most appropriately where energy is not available and wherever it is possible to pump intermittently over small heights. One area of application is the recirculation of plant water for beneficiation.


Fig.: 'Heinzenkunst' and other early types of drainage pumps. Sourece: Cancrinus, Part 6

4.3 Water bag

Deep Mining General
Underground Mining Mine Drainage

germ.:

Bulgen zur Wasserhaltung, Botas zur Wasserhaltung

span.:

botas de aro pare desague, botas de aro, botas de mano

TECHNICAL DATA:

Dimensions:

30 - 50 lifer leather bag for transporting water

Weight:

approx. 20 kg

Extent of Mechanization:

not or semi-mechanized

Form of Driving Energy:

pneumatic or electric engine on a winch

Alternative Forms:

animal-powered whim, animal drive, water wheel

Throughput/Performance:

1 - 5 m³/h up to approx. 30 m

Mode of Operation:

intermittent

ECONOMIC DATA:

Investment Costs:

approx. 100 DM, local production

Operating Costs:

dependent on type of drive

Related Costs:

winch, hoisting rig, hoisting rope or cable

CONDITIONS OF APPLICATION:

Operating Expenditure:

low |————|————| high

Maintenance Expenditure:

low |————|————| high

Personnel Requirements:

low

Location Requirements:

driving energy source is necessary

Replaces other Equipment:

drainage pumps


Regional Distribution:

rare; Bolivia, Colombia and Chile

Operating Experience:

very good |————|————| bad

Environmental Impact:

energy-intensive

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad


water bag, hoisting rig, and possibly drive-systems (e.g. hydromechanic)

Lifespan:

very long |————|————| very short

Bibliography, Source: Hentschel, Villefosse, Agricola, Treptow-Collection/Freiberg

OPERATING PRINCIPLE:

Intermittently-operating technology for water drainage and crude-ore transport by means of leather bags. For mine drainage, the filled leather bag is hoisted by a shaft winch to the surface, where it is emptied through a hose following the principle of interconnected containers (known through Villefosse from Mexico).

AREAS OF APPLICATION:

Water drainage for small quantities at shallow depths.

SPECIAL AREAS OF APPLICATION:

In addition to water drainage, this technique is still currently used in small-scale mining for crude-ore transport.

REMARKS:

The discontinuous operation is characterized by high energy demand, low efficiency, and low throughput. This could be improved by implementing a shuttle-service with two transport containers. In any case, the drive unit has to provide a controlled up and down movement, or reversal in direction. For a hydromechanic drive with a water wheel this can only be achieved only with a gear-drive unit or with a very complicated bull-wheel drive. In this case, an animal-powered drive is preferable.

As a whole, this technique is very labor intensive. At least three men are necessary for a drainage operation.

Drainage bags made of grass and coated with pitch are known to have been used in ancient Mazarron/Spain.

Water-bag transport is possible only in steep shafts. In ramps, small mines employ simple water wagons for mine drainage which are driven Into the mine sump where they are filled with water. In some places, water wagons are equipped with flap valves and ball valves attached to the bottom of the water tank which automatically open and close in the sump, thus avoiding the necessity for personnel for filling at the sump. At the surface, the wagons are emptied by means of tipping devices, siphons, etc.

SUITABILITY FOR SMALL-SCALE MINING:

Application is practical only under extreme conditions. This technique is highly labor and energy intensive and has a comparably low transport capacity.


Fig.: Types of water bags, by Agricola

4.4 Bucket-chain conveyor

Deep Mining General
Underground Mining Mine Drainage

engl.:

bucket elevator, chain pump

germ.:

Eimerkettenpumpe, Becherwerk, Kannenkunst, Paternosterpumpe

span.:

bomba de cangilones, bomba rosario

TECHNICAL DATA:


Dimensions:

up to 100 m depth

Weight:

depends on depth

Extent of Mechanization:

not mechanized

Form of Driving Energy:

slow moving (water wheel or animal-powered whim) or geared-down high-speed drives (engines, turbines)

Mode of Operation:

semicontinuous/continuous

Operating Materials:


Type:

lubricants

Quantity:

small amounts

ECONOMIC DATA:


Investment Costs:

starting at approx. 100 DM plus drive-system for approx.10m

Operating Costs:

mainly cost of energy

Related Costs:

dependent on type of drive

CONDITIONS OF APPLICATION:

Operating Expenditure:

low |————|————| high

Maintenance Expenditure:

low |————|————| high

Mining Requirements:

Bucket-chain pumps are designed only for steep shafts, and not for use in inclined shafts or ramps. They are widely used for pumping slurries in beneficiation operations (bucket elevators or hoisting wheels).

Replaces other Equipment:

other pumping systems

Regional Distribution:

Formerly a widely distributed technique, today used in Africa for purposes of conveying water.

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

Metal workshops handling wire ropes, metal chains, metal bands or rods, synthetic or natural-fiber ropes, and metal or wooden transport containers.

Lifespan:

very long |————|————| very short

Bibliography, Source: DBM, Cancrinus, Agricola

OPERATING PRINCIPLE:

The bucket-chain conveyor consists of conveyor vessels attached to two circulating ropes or chains. At the deepest point of the pump, these vessels submerge into the sump where they automatically fill with water. When the vessels reach the upper driving axle, they automatically empty into a discharge trough. As a result of the well-balanced weight distribution between the full transporting chain stringer and the empty return stringer, energy is needed only to overcome friction and to lift the weight of the water.

REMARKS:

Bucket-chain conveyor pumping systems were successfully used in mines in the the Harz region (Germany) and in the other central european mines up to depths of 150 m, and were typically driven by hydropower (water wheels).

Unlike the chinese liberation pump, the bucket conveyor pump does not empty out when the driving power is off.

The driving power required can be regulated by the number of vessels attached to the cable.

Bucket-chain conveyors are frequently employed in beneficiation processing where minor elevation differences are encountered because they can transport slurries with high solids contents without difficulties (still in operation today in tin beneficlation in Altenberg/Saxony, Germany).

SUITABILITY FOR SMALL-SCALE MINING:

Appropriate for transporting smaller quantities over greater lifting distances, a simple and practical drainage system which can be locally produced and can be powered by a slow drive-system.


Fig.: Different types of drainage apparatures, by Agricola: a) bucket-chain b) chinese liberation pump c) water bag d) piston pump. Source: Wagenbreth


Fig.: Bucket elevator in benefication processing, from Treptow.


Fig.: Vertical bucket elevator in bemeficiation processing, from Treptow

4.5 Pneumatic high-pressure pump

Deep Mining General
Underground Mining Mine Drainage

germ.:

Pneumatische Forder- und Hochdruckpumpe

span.:

bomba neumatica de transporte y de alta presion, bomba neumatica de alta presion

Producer:

Atlas Copco, Pleiger

TECHNICAL DATA:

Dimensions.

40 × 40 × 60 cm LWH

Weight:

25 - 50 kg

Form of Driving Energy:

pneumatic

Alternative Forms:

none

Mode of Operation:

centrifugal pump, diaphragm pump or multistage piston pump

Operating Materials:


Type:

compressed air (6 bar)

Quantity:

2 - 4 m³/min

ECONOMIC DATA:

Operating Costs:

mainly cost of energy

Related Costs:

compressed air feed line, transport line (fire hose or pipe)

CONDITIONS OF APPLICATION:

Operating Expenditure:

low |————|————| high

Maintenance Expenditure:

low |————|————| high

Location Requirements:

no restrictions, however pump selection must consider water quality: centrifugal pump and diaphragm pump for waste water; centrifugal pump for fresh water

Replaces other Equipment:

other pump and water conveying systems

Regional Distribution:

worldwide

Operating Experience:

very good |————|————| bad


due to low specific weight and non-susceptibility to malfunctions

Environmental Impact:

low |————|————| very high


minimal oil contamination from the air compressor

Suitability for Local Production:

very good |————|————| bad

Lifespan:

very long |————|————| very short

OPERATING PRINCIPLE:

For drainage in underground mines, a wide range of different pumps are available as pneumatic pumps which can be operated with the commonly used underground energy source compressed air.

Depending on the type of fluid to be conveyed and the transport distances and quantities, axial, radial, piston or diaphragm pumps can be employed. The first two of these pump types are fluid-flow engines, which transmit energy to the water through acceleration. The resulting lifting pressure is sufficient for only small to moderate lifting distances, the rate of flow is however relatively high. The positive-displacement pumps (piston and diaphragm pumps) expel the water from the pump chamber by decreasing the volume. High pressures are attainable especially with piston pumps.

AREAS OF APPLICATION:

Pneumatic pumps are employed both in underground and surface mining for drainage purposes, for the supply of hydraulic fluids, for pumping of gelatinous blasting explosives, etc.

REMARKS:

Fluid-flow engines serving as pumps are generally not equipped with check valves, so that the water in the transport line flows back down when the power is turned off. Piston pumps, on the other hand, are inherently designed with check-valves, so that the return flow of water through the pump is not possible.

Piston and diaphragm pumps can also function as suction pumps whereby the maximum suction head should not exceed 5 m.

In mines where a compressed air infrastructure does not exist (rendering pneumatic pumps infeasible), electric pumps and even pumps driven by internal-combustion engines are also available. They are, however, inferior to compressed air pumps in terms of operating safety.

SUITABILITY FOR SMALL-SCALE MINING:

For pneumatically mechanized mining operations, compressed air pumps are mobile and universally employable as a result of their high safety of operation, low specific weight and sturdy technology.


Fig.: Cross-section of a pneumatic immersion pump for drainage purposes. Source: Manufacture's information, Pleinger

CLOSE THIS BOOKTools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)
Technical Chapter 5: Support
VIEW THE DOCUMENT5.1 Rigid support in drifts and stopes
VIEW THE DOCUMENT5.2 Single mechanical prop
VIEW THE DOCUMENT5.3 Hydraulic prop support
VIEW THE DOCUMENT5.4 Rock bolts, rods, rock stabilizers

Tools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)

Technical Chapter 5: Support

5.1 Rigid support in drifts and stopes

Deep Mining General
Underground Mining Support

germ.:

Starrer Ausbau in Strecke und Abbau

span.:

entibacion rigida en galeria y explotacion, enmaderacion

TECHNICAL DATA:

Dimensions:

dependent upon roadway cross-section

Extent of Mechanization:

not mechanized

Alternative Forms:

possibly pneumatic chain saw to adjust roof bars and props, gas welding units for steel supports (for example from old railroad rails), cutting torch.

Operating Materials:


Type:

wood, possibly impregnation agents, e.g. common salt, iron or copper vitriol, mercury or zinc chloride.

Quantity:

large quantities

ECONOMIC DATA:

Investment Costs:

vary greatly depending on location of mining operation, cost of wood, cost of transportation, quality of wood, etc.

Related Costs:

possibly pneumatic chain saw (e.g. from Spitznas) for wooden supports, welding torch for steel supports.

CONDITIONS OF APPLICATION:

Operatig Expenditure:

low |————|————| high

Maintance Expenditure:

low |————|————| high

Replaces other Equipment:

all other types of support

Regional Distribution:

worlwide

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high


damage to vegetation due to use of wooden supports

Suitability for Local Production:

very good |————|————| bad

Lifespan:

very long |————|————| very short


steel frame-sets are reusable

OPERATING PRINCIPLE:

Framing or timbering support consists of two props and one roof bar made of wood or iron. Support capabilities vary depending upon the type of connection between the props and the roof bar.

The German framing method is characterized by the interlocking or scarfing of bars and props. The frame-set can then resist both shear forces as well as vertical compressive loading. Depending on the calculated ratio between these two loads, scarfing can be designed more for shearing forces or more for vertical compressive loading. To increase the compressive strength of the props, the props are installed with the thicker end toward the roof.

The Polish timbering method is characterized by a loose laying of the roof bar on top of the two grooved props. This method cannot counter shearing forces (lateral compression).

The 'Silesian' method includes a "soldier sprag" brace wedged between the props underneath the roof bar to reinforce the props against lateral compressive forces.

Frame-set supports are additionally braced by wedging struts between the props of adjacent sets to increase their stability. The spacing between sets ranges from a few centimeters up to 1,5 m depending on the compressive load. In Inclined formations, frame supports are installed with the props perpendicular to the stratification (dip).

REMARKS:

For mine support, a timber with a long fiber structure is always employed, such as spruce, fir, or other conifer wood, or eucalyptus. Timbers of these wood types shatter slowly when their loading capacity is exceeded and thus warn the miners through a definite creaking. Short-fibered timbers break without any prior, slowly-developing visible or audible indications. A dense, resinous, slow-growing wood type is always preferable for mine support purposes. For mining activities of longer duration, the timber should be cultivated by the mine operators themselves near the mine site.

Timber employed in moist or wet mines, especially for shaft construction in exhaust ventilation shafts or drifts in water-bearing strata, should be previously treated by a preservative. Timbers are impregnated by dipping them into special solutions, such as Roman-salt, copper sulphate, etc., either with or without pressure.

Timber support normally is not reuseable. The only exception is simple prop timbering for stoping which is sometimes recovered and the wood then reused for shorter props, head boards, breast timbers or wooden cribbing. In situations requiring excessive support, such as mining in incompetent rock, the cost off timbering becomes a significant factor in the economic analysis of the operation. Here the higher investment costs for friction prop support can result in a substantial savings In operation costs, since these support elements can be reused.

Timbering is the simplest roof support method in incompetent rock (e.g. in faulted zones) and contributes greatly to increasing mine safety. It is, however, disadvantageous for artificial mine ventilation in that it increases air resistance.

In addition to purely wooden supports, there are also systems which employ mixtures of wood and steel, as well as purely steel supports or arches and - also widely distributed - yielding arches made from steel channel sections.

An alternative method for supporting drifts is the construction of non-cemented or cemented brick arches. These are used to support longitudinal vault-like tunnels, requiring either expensive abutments on both sides (built into deep grooves in the floor or constructed as retaining walls) or as adjacent arches with span-widths of several meters which run along both sides of the vault parallel to its longitudinal axis. Bricked arch support is extremly expensive and is suitable only where galleries must remain open for longer durations. In areas of stoping activities, support is provided by individual props (see 5.2).

SUITABILITY FOR SMALL-SCALE MINING:

As an auxiliary support in stopes and drifts, timbering is a very sturdy support method which is quick and simple to install. The local availability of timber for the supports has a major effect on the costs. In areas of poor vegetation, timbering should not be employed In order to avoid destruction of forests.


Fig.: polish and Swedish timber sets. Source: Treptow.


Fig.: Timbering with individual props; left: a) simple prop, b) prop with head board and foot block; right: prop, wedged to counter lateral compression. Source: Treptow


Fig.: Joint between prop and roof bar of a Polish frame-set (left) and scarf joint between the prop and roof bar of a German frame-set (right). Source: Treptow


Fig.: Different types of simple timbering for various deposit and strata conditions. Source: Treprow


German frame-set timbering with breast timbers, typical roof lagging and latticed lagging of the stopes. Fig.: Laggin in German timbering support in a drift. Source: Treptow

5.2 Single mechanical prop

Deep Mining, General (Coal)
Underground Mining Support

germ.:

Einzelstempelausbau/mechanisch

span.:

estemple individual mecanico

TECHNICAL DATA:

Dimensions:

from 0,63 - 3,15 m

Weight:

approx. 10 - 50 kg

Extent of Mechanization:

not mechanized

Form of Driving Energy:

manual

Mode of Operation:

intermittent

ECONOMIC DATA:

Investment Costs:

dependent on material

Operating Costs:

low

Related Costs:

none, requires only hammers for installation; bars of wood or steel rails.

CONDITIONS OF APPLICATION:

Operating Expenditure:

low |————|————| high

Maintenance Expenditure:

low |————|————| high

Personnel Requirements:

low

Location Requirements:

suitable for areas of low timber availability

Replaces other Equipment:

wooden timbering, etc.

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

meetal workshop

Lifespan:

very long |————|————| very short

Bibliography, Source: Bansen, Fritzsche, Woodruff

OPERATING PRINCIPLE:

A single mechanical prop consists of encased prop sections which are mechanically telescoped outward for wedging the prop between the floor and the roof or roof bar. Rigid props are differentiated from yielding props according to the operating principle: rigid props, for example threaded and nonius-props, can only react to increased compressive loads when a wooden bar permits deformation, otherwise they collapse when the maximum load is exceeded. Yielding props, on the other hand, telescope together when the maximum load is exceeded. This can be achieved either by friction systems (friction prop) or by inserting compressible elements (e.g. peat prop).

REMARKS:

Flexible due to unlimited reapplication possibilities.

Different types:

- nonius-prop / temporary prop


- friction prop


- threaded prop / temporary prop

can possibly be made out of scrap, e.g. railroad rails.

A common problem is that single mechanical props can only be installed with a low setting load. Various mechanical setting devices make the setting process easier.

The less the props are extended, the better they can withstand loading without bending and will therefore last longer.

Problems arise in employing mechanical prop supports in mines which are characterized by highly fluctuating deposit thicknesses, in that a precise assessment is required in advance to determine the appropriate long-term prop length. This greatly limits their suitability for small-scale mining.

SUITABILITY FOR SMALL-SCALE MINING:

A mechanical prop support is a suitable reuseable support method in mining of deposit zones where relatively low compressive loads are encountered. The low setting load is a major disadvantage of this technique, which -- particularly when a large quantity of props are employed -- is technically inferior to hydraulic prods.


Fig.: (above): Simple yielding props with compressible insets. (right, of peat; left. of wood). Source: Bansen


Fig.: Types of props with compressible elements made of wood. Source: Bansen


Fig.: Nonius-prop, in which the nonius serves to increase the setting load of the otherwise rigid prop. Source: Bansen


Fig.: Friction elements of modern friction props. Source: Woodruff


Fig.: Cross-section of a duplex prop, the top part with threads and the bootom part with friction element.Source: Reuther


Fig.: Profile (left) and section view (right) of a wedged prop. Source: Reuther


Fig.: Various types of German-made friction props. Source: Woodruff

5.3 Hydraulic prop support

Deep Mining General
Underground Mining Support

germ.:

Einzelstempelausbau/hydraulisch

span.:

estemple individual hidraulico

Producer:

Salzgitter, DeBeSa

TECHNICAL DATA:


Dimensions:

650 - 3600 mm collapsed, 675 - 5000 mm extended

Weight.

steel: 42 - 240 kg/prop + 4 - 18 kg extension pieces, light alloy: 25 - 65 kg

Extent of Mechanization:

fully-mechanized when serviced by a central pumping and distribution system for hydraulic fluid; not mechanized when serviced by a manual pumping system (internal or external)

Form of Driving Energy:

electric or pneumatic pump for producing hydraulic pressure

Throughput/Performance:

10 - 15 sec. setting time Operating Materials:

Type:

oil in water-emulsion pure water (DeBeSa)

Quantity:

2 - 4 % oil in H2O, pH 5 - 8, dH up to 15

ECONOMIC DATA:


Investment Costs:

approx. 1.2 - 4 times the cost of friction props (see 5.2)

Operating Costs:

approx. 50 % of the costs for traditional timbering

Related Costs:

hydraulic high-pressure pump (approx. 200 bar) with setting gun, roof bars.

CONDITIONS OF APPLICATION:

Operating Expenditure:

low |————|————| high

Maintenance Expenditure:

low |————|————| high

Mining Requirements:

hydraulic props are primarily employed in slightly or partly mechanized coal mines, but are also found in ore mines, industrial mineral mines, etc.Even in fully-mechanized mines hydraulic props are still in use for special support, for example in areas of geological faults, at the ends of the face, face-roadway intersections, etc. due to their flexibility and versatility.

Replaces other Equipment:

timbering, friction props

Regional Distribution:

worldwide, especially in coal mining

Operating Experience:

very |————|————| good bad

Environmental Impact:

low |————————| very high


With conventional props, high pollution of mine water and drainage ways due to use of oil-in-water emulsion for hydraulic fluid. Glued - joint steel pipe props from DeBeSa use pure water as hydraulic fluid and thereby contribute to environmental protection.

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

Assembly and repair of the glueable DeBeSa hydraulic props is possible in comparably simple manufacturing workshops.

Lifespan:

very long |————|————| very short


The long lifespan and suitability for reuse, in conjuction with the capability to replace defective components, ensure longlasting employment.

Bibliography, Source: Salzgitter Company information, DeBeSa Company information, Fritzsche,
Woodruff

OPERATING PRINCIPLE:

Hydraulic props consist of a sealed working cylinder with two valves, one for intake (setting valve) and the other for discharge (release valve, working valve) of hydraulic fluid. For increased stability the hydraulic props are equipped with a claw at the upper head-end and a base at the bottom. The function of the props is to stabilize incompetent roof or hanging wall. The positioned prop is telescopically extended by highly-pressurized hydraulic fluid injected by means of a setting gun and wedged into place with a specific setting load adjusted according to the respective compressive rock load. When the rated load is reached during installation or by subsequent strata movement, the working valve engages and opens the cylinder. This yielding prevents damage to the support from increasing compressive loading. The optimal support is attained when the props are installed in combination with articulated bars which distribute the forces over a wider hanging-wall or roof surface. During prop recovery, the release valve is opened with a key, allowing the hydraulic fluid to escape and the prop, equipped with a spring, to recede. The prop is then available for reuse.

AREAS OF APPLICATION:

Use of hydraulic single prop supports is only practical and economic where incompetent roof or hanging wall require a support method which can be adjusted to meet rapidly changing conditions. Hydraulic prop supports are appropriate for short-term installations involving frequent changes of location due to rapid face advance, or where high prop-setting loads are desireable. Such conditions arise in coal mining with roof caving or backfilling, in longwall mining, in room and pillar mining, as well as in ore mining by overhand stoping. In addition, single hydraulic props are suitable for support of all special mining activites such as support of fault-zones or roof-fall areas, machine rooms, and face-roadway intersections.

REMARKS:

The use of single hydraulic props in the situations listed above can contribute significantly to protecting valuable natural resources by substituting for traditional timbering methods. Replacing the normally non-reuseable support timbers (e.g. in Turkey, totalling more than 1 m³/20 t of useable output) with re-usable props can also result in decreased operating costs.

The limited working length of the hydraulic prop, like mechanical friction props, is disadvantageous in mines with fluctuating seam or vein thickness.
Due to the high setting load achievable with hydraulic props, capable of supporting areas 5 to 10 times larger than mechanical props, the prop density can be reduced.

The DeBeSa Company is striving to adapt their products (individual props and articulated bars) to meet the demands of small-scale mining in developing countries:

- assembly and repair can be performed by local labor. The costs for an assembly and repair shop amount to only around 10 % of the costs of commonly manufactured parts.

- the approx. 30 % net product arising from local production preserves the country's foreign exchange position.

- cost savings of more than 50 % can be realized compared to the widely-used wood timbering.

- the capital investment for a highly developed and complex support system is not required.

- the use of glueable Joints in this modular system permits the replacement of damaged parts, therefore increasing the lifespan of the remaining components.

- storage costs are reduced by around 70 % as inventory can be limited to only a few standardized parts.

Disadvantages of hydraulic props include high consequential or related costs for producing and distributing high-pressure fluids (pneumatic or electric high-pressure pump, liquid storage tank, high-pressure hoses, setting guns, etc.).

This disadvantage can be overcome by employing props which are set with manually-operated pumps. Such props were employed earlier in Germany, and are still used today in Anglo-Saxon countries. They function by using a hand pump to force the hydraulic fluid from the upper cylinder (storage cylinder) into the lower cylinder (working cylinder), analogous to a hydraulic automobile jack.

SUITABILITY FOR SMALL-SCALE MINING:

The type of prop system employed affects the consequential costs. Simple manually-operated props offer an alternative to timbering in small-scale mines. The investment for single hydraulic props with an external pump system can only be recovered when large quantities are employed to offset the higher costs for the necessary auxiliary installation devices.


Fig.: Telescoping, setting and drawing (recovery) of hydraulic individual props with manual pump (left, from top to bottom) and cross-section of a hydraulic prop. Source: Woodruff


Fig.: Sketch of a hydraulic prop, supplied externally with hydraulic fluid. Source: Manufacturer's information, Salzgitter

5.4 Rock bolts, rods, rock stabilizers

Deep Mining in Competent Rock
Underground Mining Support

germ.:

Felsanker

span.:

barras, pernos de anclaje, pernos pare hormigon

Producer:

Atlas Copco, Grauvogel, Lenoir et merrier, GHH, Becorit, Gebr. Windgassen, Ingersoll-Rand

TECHNICAL DATA:

Dimensions:

800 mm - 4,000 mm length, 16 - 42 mm for drilling hole 32 - 76 mm

Weight:

1 - 25 kg

Extent of Mechanization:

not/partly mechanized

Mode of Operation:

intermittent

Capacity/Throughput:

5 - 100 t pulling force

Technical Efficiency:

30 - 40 min/bolt inserting time in low mechanized mines, density of bolts up to 1 per m²

ECONOMICAL DATA:

Investment Cost:

approx. 20 DM/piece

Consequential Cost


through Coupling Effects:

jack-hammer with drill steel of same length as bolt, spanner or roof bolting drilling and setting machine

CONDITIONS DE APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Experience:

low |————|————| high

Mining Requirements

bolts have to be preloaded whose intensity is difficult to assess manually. Pneumatic impact wrench or setting winch is therefore preferred.

Replaceable Equipment:

other support methods in solid rock excavations

Regional Distribution:

worldwide

Experience of Operators:

very good |————|————| bad

Environmental Impacts:

low |————|————| very high


deecreasing demand for wood in mines

Suitability for Local Production:

rod anchor

very good |————|————| bad

Under what Conditions:

metal manufacture

Lifespan:

very long |————|————| very short

Bibliography, Source: Fritzsche, Company Info, Woodruff, Ruther

OPERATING PRINCIPLE:

Bolt support is being applied to fix rock strata which are slacking off due to a decreasing pressure of strata in the area of mining excavations at the stable rock mass. This is being done by inserting a bolt into a drilling hole that is then either wedged mechanically or along the whole length or sections cemented or pasted together with the adjoining rock. The anchor bolt transmits the tension to the screwed roof-bolt head.

AREAS OF APPLICATION:

To support mining excavations and roadways of underground mines. Bolt support can be an alternative to timbering which is what is commonly used in the developing countries.

In hard rock mining, bolts are used where larger excavations in stable rock are supposed to last long, e.g., storage bunkers, crushers, chambers, draw points.

Various types of bolts that are used can be classified as follows:

Mechanical bolts:

- slot-and-wedge bolt*


- expansion anchor as expansion shell bolt*


- expansion wedge bolt* and wedge shell bolt*


- split set and folding bolt

Mortar bolts:

- cement bolts


- resin-based mortar bolts

Combination bolts:

- end-cemented expansion bolt or split set


- cemented press bolt

*such types of anchors need the lowest extension of mechanical equipment

REMARKS:

Bolted support shall be applied, where nonrelaxed rock is stable. Bolted support would be the wrong method in faulted zones.

Advantages of bolted support are the fast insertion and that no space requirements are needed.

Blasting tremors can affect the bracing of mechanical bolts.

Different bolts for mechanical bracing in stable and semi-stable rock are available. Semi-stable and loose rock necessitates cemented bolts. Expansion bolts are usually braced with half its yield stress.

Besides washers and bolting plates with or without angular compensation, bolted support is being applied by lagging screen wire, steel belts etc. The lagging keeps back the broken rock and directs stress to the bolts.

For the optimal functioning of bolted support, it is necessary to insert the bolt in the direction of the expected pulling force. Specific geological knowledge (stratification, foliated structure) is therefore necessary.

Besides metallic bolts, wooden slot-and-wedge anchors were applied in the U.S.A. mainly in places with soft hanging such as argillaceous and quarzitic shalestone. Its dimensions were 5 cm, 125 cm length, 6 × 6 cm head, turned on a lathe with fresh, wet pine or spruce wood, two wedges 1 7/8 × 1 × 16" and one 30" in anchor plate. The cost approx. 0.5 US$/plece. The advantages were, high retaining force in loose adjoining rock, the possible production at the mine site, and high corrosion resistance. Such anchors have been produced locally with output of some 500 pieces/man-shift and setting capacity of some 100 pieces/ms.

SUITABILITY FOR SMALL-SCALE MINING:

Bolted support is advisable only for pneumatic mechanized mines with semi-stable adjoining rock as roof support.


Figs.: Different types of expansion bolts, Reuther.


Fig.: Wooden bolted support in Dayrock Mine, USE, by Woodruff

mechanic bolts

expanding anchors

friction pipe bolts


Figure

mortar bolt

cement mortar bolt

synthetic resin-based mortar bolt


Figure

combinations of mechanic and mortar bolt partely filled at bottom with mortar

completly filled with mortar

expanding anchor with resin-based mortar


Figure

Fig.: Different types of bolt systems, Reuther

CLOSE THIS BOOKTools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)
Technical Chapter 6: Lighting
VIEW THE DOCUMENT6.1 Underground lighting equipment

Tools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)

Technical Chapter 6: Lighting

6.1 Underground lighting equipment

Deep Mining General
Underground Mining Lighting Equipment

germ.:

Geleucht fur unter Tage

span.:

lluminacion pare interior mine

Producer:

Northern Light, CEAG, Friemann + Wolf

TECHNICAL DATA:

Mode of Operation:

continuous

Throughput/Capacity:

approx. 260 - 300 1 acetylene/kg CaC2 for calcium carbide lamps

Technical Efficiency:

0.7 - 1.1 I C2H2/cd. for calcium carbide lamps, 10 - 17.5 W/cd. for electric lamps

Operating Materials:


Which:

calcium carbide + water gasoline (benzene) possibly battery acid

Quantity:

approx. 250 g + 250 g/MS approx. 100 g/MS

ECONOMICAL DATA:

Investment Cost:

1. calcium carbide lamp: 50 to 80 DM; 2. gasoline safety lamp: 200 DM, 3. cap lamp: 350 to 400 DM

Operating Cost:

fuel cost for 1. and 2., Energy cost for 3.

Consequential Cost through Coupling Effects:

charging station and energy supply for electric lamps

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————|high


calcium carbide lamp

Maintenance Experience:

low |————|————|high


battery lamp

Location Requirements:

All open or naked-light lamps should be used only at explosion proofed locations. The danger of foul air whose oxygen content decreases perilously cannot be determined by the use of carbide lamps.

Replaceable Equipment:

other types of lighting equipment, e.g. candles, open or naked-light


oil or grease lamps

Regional Distribution:

calcium carbide lamps worldwide, gasoline lamps in Latin America, electric cap lamps worldwide

Environmental Impacts:

low |————|————|very high

Suitability for Local Production:

very good |————|————|bad


a photovoltaic battery charging station can be assembled from easily available components calcium carbide lamp

Lifespan:

very long |————|————|very short


electric cap lamp

Bibliography, Source: Fritzsche, Company Information, Information from Mining Pits

OPERATING PRINCIPLE:

As source of lighting for underground mining, diferent types of lamps are here being distinguished:

Calcium carbide lamps:

A calcium carbide lamp is composed of a double container, the upper vessel of which is filled with water dripping under control of a cock into the lower vessel filled with calcium carbide (CaC2). Through the water impact, acetylene (C2H2), a burnable gas results, which is then sprayed under pressure through the burner jet. The gas is flamed at the external opening of the Jet. A reflector is installed behind the flame.

The bright and continually shining light is a remarkable quality of calcium carbide lamps. The consumption of calcium carbide and Water average approx. 250 9/8 furs. The total weight of a filled lamp is approx. 1 - 1.2 kg. Calcium carbide lamps are made out of either metal (iron, steel or brass) or plastic. Beside hand lamps, cap lamps are used in which an approx. 1 m long hose combines gas producing unit with jet. The gas producing unit can then be carried at the belt, whereas the Jet with reflector can be carried at the helmet Besides, there are calcium carbide lamps of smaller size that can be fixed directly at the helmet.

Gasoline lamps:

Today, gasoline lamps are still widely distributed in Latin American mines. They are composed of a gasoline tank, a wick system, a burning chamber isolated with glass, and an open wire basket. When explosive gas develops, the wire basket avoids an outbreak of flame into the atmospheric weather by cooling flame temperature. At the same time, gas concentration of mine air in a particular weather can be determined by comparing the flame cap (aureole) with known values. Weight is approx. 1 kg.

Electric lamps:

Electric cap lamps with a battery unit carried at the belt and a supply cord connected to the cap lamp weigh between 1.4 and 2 kg and are shining up to approx. 10.5 to 12 hours. The cap lamp is equipped with a double filament bulb which allows different luminescences and operating periods.
The use of electric lamps is problematic where supply of electricity does not exist.

In areas with high radiation intensity and long periods of sunshine, it is possible to charge battery lamps by photovoltaic method. Two scenarios should be taken in mind. In the first case, direct charging of batteries is done during day time per solar cells, and In the second case, charging of batteries is done by interconnected storage batteries. The volt regulation of charging voltage, however, has turned out to be a problem. If it drops below 5 volts, operation period of the lamp and the amount of possible charging cycles decrease. Normally, an electric lamp can be charged and discharged up to 1000 times. Northern Light Company offers simple charging stations operated by car batteries which, most probably could be applied for charging with solar cells. The cost of a charging unit with direct current of 12 volt ranges between 100 and 120 US$. Cost of electric cap lamps with a capacity of 7 to 14 h are approx. 350 to 400 DM.

Finally, compressed air lamps can be used for stationary lighting. Here, an alternating current generator is driven by compressed air with working pressure between 3 and 6 bar, and consumption of compressed air between 5 and 20 m³/h. As source of light, either a high-pressure mercury lamp (approx. 80W), a halogen lamp (50 - 70W) or fluorescent lamp (20 - 40 W) is used. The weight of these stationary lamps is between 10 and 15 kg.


Fig.: Shape and size of a gasoline lamp flame in correlation to the gas content of mine air. Source: Fritzsche


Fig.: A calcium carbide lamp as hand carrier lamp. Above, water tank; calcium carbide container. Source: Fritzsche


Fig.: A gasoline lamp. 1) upper frame pannel, 2) wire baskets, 3) ring, 4) lower frame pannel, 5) magnetic lock ring, 6) number plate, 7) hard glass cylinder, 8) heat plug, 9) ring, 10) lamp vesel. Source: Fritzsche


Fig.: Electric cap lamp. Source: Frieman & Wolf, Company Information


Fig.: Cross-section of an electromagnetic compressed air lamp from CEAG. Source: Fritzsche

CLOSE THIS BOOKTools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)
Technical Chapter 7: Stoping
VIEW THE DOCUMENT7.1 Pneumatic jack hammer, drilling stand, jackleg
VIEW THE DOCUMENT7.2 Gasoline hammer drill
VIEW THE DOCUMENT7.3 Wedge ram
VIEW THE DOCUMENT7.4 Electric hammer drill with stand Y D Z
VIEW THE DOCUMENT7.5 Manual mining methods
VIEW THE DOCUMENT7.6 Pneumatic charging machine for explosives

Tools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)

Technical Chapter 7: Stoping

7.1 Pneumatic jack hammer, drilling stand, jackleg

Stable Rock Deep Mining, Stable Rock Open-Pit
Underground Mining, Extraction Mining

germ.:

Pneumatischer Bohrhammer, Bohrstutze, Teleskopstutze

span.:

perforadora neumatica, pie de apoyo, apoyo telescopico

Producer:

Atlas Copco, Montabert, SIG, Bohler, Tamrock, Mannesmann Demag, Barrenos: Barrenos Sandvik SA, ADESUR, Fagersta Secoroc de Peru

DATOS TECNICOS:


middle weight lack-h

light weight lack-h

drilling stands

Weight:

22 - 29 kg

9.5 kg

13.5 kg

Length:

60 - 70 cm

approx:50 cm

800 - 1.650 mm

Piston �:

58 - 90 mm

66 - 75 mm


Stroke length:

45 - 70 mm

750 - 2.000 mm


Single strike energy:

48 - 150 Nm



Number of strokes:

2.200 - 3.400 min-1

3.500 min-1


Strike capacity:

1.9 - 5.5 Kw



R.P.M.:

160 - 240 min-1

280 min-1


Rotation angle:

20° - 30°



Torque:

100 - 150 Nm



Compressed air consumtion:

2.4 - 5.6 m3/min


1.4 m3/min

Drill hole �:

27/41 - 34/5 mm



Max. Iength of drill hole:

4 - 6.5 m



Working pressure:

3 - 7 bar

3 - 7 bar


Opt. working pressure:

5 - 6 bar

5.5 bar

5 - 6 bar

Rate of drilling progress:

up to 35 - 100 cm/min



Drilling equipment:

monobloc drilling rods with male end hexagonal 22 mm (7/8 inch) × 108 mm working length of:


800 mm with 34 mm diameter and 3.0 kg weight


1600 mm with 33 mm diameter and 5.4 kg weight


2400 mm with 32 mm diameter and 7.9 kg weight


as well as lengths in-between according to the supplier

Operating Materials:




Which:

oil

water

Pwater= Pair-1 (bar)

Quantity:

small amount as lubricant

drilling water 3/4" supply


ECONOMICAL DATE:

Investment Cost:

2500 DM - 6000 DM jack-hammer; approx. 4000 DM/piece (used) incl. stand; drilling stand approx. 2000 - 3000 DM/piece

Consequential Cost through Coupling Effects:

cost of compressed air supply

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————|high

Maintenance Experience:

low |————|————|high

Personnel Requirements:

low for handling

Adjoining Rock Requirements:

Almost without exemption, all adjoining rock can be drilled in; in cases of very soft adjoining rock, rotating or rotating-percussion drilling is applied to that drill cuttings or debris can be removed easily.

Regional Distribution:

worldwide

Experience of Operators:

very good |————|————|bad

Environmental Impacts:

low |————|————|very high


Especially in cases of insufficient water or air circulation, dangerous dust pollution occurs: Silicosis

Suitability for Local Production:

very good |————|————|bad

Lifespan:

very long |————|————|very short

Bibliography. Source: AC-Handbook, Stout, Fritzsche, Reuther, Roschlau

WORKING PRINCIPLE:

The pneumatic Jack-hammer works with a centrifugal piston driven by compressed air with strokes ranging between 1,800 and 3,500 min-1 in reciprocating motion and is controlled by a flutter valve. After a forward motion, when the admission strike reaches the bigger cylindrical chamber, the centrifugal piston hits the male end of the drilling rod. As the strike reverses, the male end is rotated by spinning grooves at the centrifugal piston. The rotation device with a pawl and ratchet mechanism allows rotation only in one direction. Thus, the cutting edge of drilling steel always hits another sector of the bottom hole. A central water supply leads through the centrifugal piston and male end to the flush. The flushing fluid then cools the drilling steel, removes drill cuttings or debris, and binds possible silicone dusts.

Drilling stands guide the percussion bit into the hole and transmit the thrust to the hammer. Such drilling stands composed of pneumatic telescoping cylinders, are fed with compressed air and fixed in an inclined position at the bottom hole. Depending upon the design, air pressure and therefore the thrust can be controlled either directly at the hammer or at the stand. A pneumatic device withdraws the hammer.

In drilling rise heading and vertical holes in upward designed mining, such as in steep vein ore deposits, the so called stop-hammers are used which are fixed at the stand.

Repeated sharpening of drilling bits or steel is very important for the drilling progress as well as for a long-lasting drilling equipment. This can be done by small compressed air driven grinding machines fixed on a tripod and equipped with a vice to fix the drilling bits. The most important standards for carbide bits, e.g., wedge angle, cutting edge curve, coefficient of wear and lateral angle are controlled by pattern. The standing time of drilling bits until they have to be sharpened are in correlation to the wearing hardness of drilled rock. The following table shows after what rate of penetration sharpening becomes necessary

Kind of rock

Drilling meterage

Sandstone

8 - 16

Sandy shale

20 - 30

Shalestone

50 - 100

Gneiss, granite

3 - 6

Older rock salt

30 - 36

Carnalitite

40 - 50

Hard salt

22 - 100

REMARKS:

Percussion and rotating-percussion hammers need high thrust.

It should be taken in mind to avail of small jack hammers with stand such as the Tll of Montabert weighing 9.5 kg and consuming 1.4 m³/min compressed air. The low capacity could be amended by higher explosives. Additional cost for this should be taken In relation to the lower cost of compressed air supply.

Instead of supplying water in a costly pipe system, water can be carried by mobile tanks, in which the resuming space is filled with compressed air.

Cost of percussion drilling:

Jack hammer

approx. 50 %


Compressed air

approx. 10 %


Percussion drill bit

approx. 40 %

In pneumatic drilling, the degree of efficiency with the corresponding applied energy is very low considering the losses in the production of compressed air and lies between 1 to 10%, depending upon the parameters used. Aside from losses during the production and distribution of compressed air, losses also occur during transmission of power in percussion, sound insulation, friction at the drilling hole wall as well as during reflexion of percussion energy into the drilling rod.

A further source of losses is in the connection of drilling rod, bit, and possibly of extension rods. Power loss of each connection is approx. 5 %. To avoid such losses, using monobloc drilling machines and avoiding extension rods can be done.

Since jack-hammers are usually delivered with a left turning rotation, they should be ordered with a right turning rotation for anchor setting, so that the anchor nut can be tightened with the hammer which is equipped with a special device.

The thrust which needs a medium-sized hand hammer, ranges between about 60 to 120 kg. Of this, only an average of approx. 5 kg can be done by the hammer manually or without any mechanical aid. Heavier dead weights lower the backward thrust of hand-held percussion drilling machines.

In order to be able to distribute the needed high thrust, an optimal angle of attack of the stand has to be selected. It should be always smaller then 40.

After a distance of 5 - 10 cm and starting with a low thrust, more power can then be applied.

Instead of a pneumatic drilling stand, the mexican method and a system comprising of two ladders and one slide board can be used for light weight hammers.

Before assembly of the drilling system begins, hoses have to be blown out in order to avoid water hammer destroying the drilling machine.

Pneumatic mining hammers are used for minerals that don't require drilling and blasting due to their low degree of hardness. Only a forward and backward motion is transmitted by the centrifugal piston to the striking bit. Rotation and flushing of water are excluded.

SUITABILITY FOR SMALL-SCALE MINING:

Pneumatic jack hammers are suitable for all drilling purposes in underground and open-pit mining due to their low weight and high stability, however, they need expensive power supply.


Fig.: Jack-Hammer with water jet, 1) jet, 2) feed line for compressed air, 3) feed line for water supply. Source: Roschlau.

Multiplers to detrmine the air consumption of rock and drills at various altitudes


Number of drills

Altitude

1

2

3

4

5

6


Multipliers

ft.







0

1.0

0.9

0.9

0.85

0.82

0.8

1.000

1.0

0.95

0.93

0.87

0.84

0.83

2.000

1.1

0.97

0.95

0.92

0.88

0.86

3.000

1.1

1.0

1.0

0.95

0.92

0.9

4.000

1.1

1.05

1.03

0.97

0.94

0.93

5.000

1.2

1.1

1.07

1.02

0.98

0.96


Fig.: A drilling stand. Source: Fritzsche


Fig.: Quality control of drilling bit sharpening, a) wearing control, b) control of wedge angle, c) control of open angle curve. Source: Roschlau.


Fig.: Cross-section of a jack-hammer. Source: Reuther.

1.

compressed air adapter

10.

behind cylinder room

18.

canal

2.

free room inside the cylinder head

11.

cover

19.

cylinder

3.

valve chatter

12.

cover room

20.

piston shaft

4,5.

canal

13.

canal

21.

twist nut

6.

front cylinder room

14.

exhaust arris

22.

leader nut

7.

percussion piston

15.

front piston arris

23.

drill sleeve

8.

behind piston arris

16.

arris at the piston shaft

24.

shank

9.

exhaust arris

17.

wearing box

25.

drill sleeve





26.

ratchet wheel


Fig.: Design of a jack-hammer with stand, a) for thrust, b) stop-hammer. Source: Armstrong.


Fig.: Composition of a complete drilling system for pneumatic drilling with stand. Source: Atlas Copco Company Information.

1. jack-hammer
2. coupling
3. stand
4. extension for stand
5. flush water hoses with claw coupling
6. compressed air hoses with claw coupling
7. oil lubricator
8. water separator


Fig.: Drilling bits for percussion drilling, 1) hard metal tip 2) flush hole 3) bit neck 4) hard metal pins. Source: Roschlau

7.2 Gasoline hammer drill

Stable Rock Deep Mining Stable Rock Open-Pit
Underground Mining Drilling Mining

germ.:

Benzingetriebener Bohrhammer, "Cobra", "Pionjar", Brennkrafthammer

span.:

motoperforadora, camera de combustion

Producer:

Atlas Copco

TECHNICAL DATA:

Dimensions:

75 × 50 × 35 cm HWL



Weight:

25 or 23 kg /26 kg



Extent of Mechanization:

fully mechanized



Form of Driving Energy:

eternal combustion engine 185 cm3/2500-2700 R.P.M.

Mode of Operation:

semi-continuous

Throughput/Capacity:

250 - 300 mm/min thrust in granite

Operating Materials:


90/100 Pionjar:


Which:

gasoline

80/100 octane, also lead free

oil/SAE 40

Quantity:

approx. 1.5 I/h

1: 12 (8 %) pionjar

1: 20 (5 %)

ECONOMICAL DATA:

Investment Cost:

approx. 5000 DM



Operating Cost:

high cost of fuel



Consequential Cost through Coupling Effects:

special sucking ventilation for underground operations is necessary

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Experience:

low |————————| high

Mining Requirements:

Gasoline driven jack-hammer can only drill in horizontal or downward approach, but in exceptional cases, up to 45° upward. The reasons for that is the direct coupling of engine and carburetor. Advantages are mining methods which lead downward and so allow bench drilling.

Replaceable Equipment

compressed air hammer drill

Availability of Technique:

import is necessary

Regional Distribution:

so far unknown in small-scale mining in Latin America

Experience of Operators:

very good |————|————| bad

Environmental Impacts:

low |————|————| very high


contamination of the environment with exhaust and used oil

Suitability for Local Production:

very good |————|————| bad

Lifespan:

very long |————————| very short

Bibliography, Source: AC-Handbook

OPERATING PRINCIPLE:

Gasoline hammer drills operate with a twin-piston internal combustion engine. One part of the piston is a centrifugal piston which functions as a striking piston, whereas the other part is used for the transmission of drilling rods and compression air in order to blow clean the drilling hole.

AREAS OF APPLICATION:

Drilling of downward and possibly horizontally aligned blasting holes of underground and open-pit mining with hard or solid rock.

REMARKS:

Grinding machines with bending shaft and centrifugal pump are available as auxiliary equipment to drive gasoline fed hammer drills.

Very problematic are the following:

- somewhat heavy weight is specially when working at or near a hanging wall

- exhaust with high CO content. Special ventilation is absolutely necessary. Long hose for exhaust lowers efficiency

- reduced efficiency of up to 50 % in high altitudes of Latin American small-scale mines

- pulling of drill rods without extra equipment is often difficult or impossible

- drilling is dry resulting to enormous dust development.

General internal combustion engines are dangerous in underground mines and need special ventilation due to high CO-content in the exhaust. The use of such machines is not advisable especially in small-scale underground mining which often lack sufficient ventilation. The advantage of being independent from an underground power supply system is being neutralized by the expenses for a special sucking ventilation.

There is a high danger of silicosis development when working in hard or solid rock where quartz stones are drilled.

Pionjar is more suitable for high altitudes in developing countries than the Cobra. On one hand, the needle carburetor can be adjusted to a higher altitude, on the other hand, its design is simpler than the diaphragm carburetor of the Cobra

Already used in Afghanistan in blasting short tunnels for storage rooms. There they were used with slides on stands.

Analogous to pneumatic mining hammer, gasoline driven mining hammers are available for easily exploitable minerals such as coal.

SUITABILITY FOR SMALL-SCALE MINING:

Not suitable for application in running underground operations due to environmental and safety problems. Application or use seems right only for special works without compressed air infrastructure and in open-pit mining for hard sediments.


Fig.: Cross-sectional sketch of a Cobra gasoline hammer. Source: Atlas Copco company Information

7.3 Wedge ram

Stable Rock Deep Mining Stable Rock Open-Pit
Underground Mining Extraction Mining

germ.:

Rammkeil, Gesteinsbrecher nach Francois

span.:

rompedor de rocas, segun Fran,cois

TECHNICAL DATA:

Dimensions:

length about 4 m

Weight:

approx. 30 kg + 45 kg driving ram

Extent of Mechanization:

not mechanized

Form of Driving Energy:

manual

Mode of Operation:

intermittent

Operating Materials:

none

ECONOMICAL DATA:

Investment Cost:

self-made: 250 - 500 DM

Operating Cost:

exclusively labor cost

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Experience:

low |————|————| high

Mining Requirements:

no breakings can be cut by wedge ramming, which means full work is not possible with wedge ram

Replaceable Equipment:

blasting explosives

Regional Distribution:

mostly replaced by blasting explosives, application where ram or blast effects have to be controlled, e.g., in natural stone mining, marble quarries etc.

Environmental Impacts:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under what Conditions:

good metal manufacture with good welding technique and can operate with tenacious steel

Lifespan:

very long |————|————| very short

Bibliography, Source: Lengemann

OPERATING PRINCIPLE:

Four springs are inserted Into the drilling hole. The wedge which leads to a quadratic area for the ram is then being rammed into the remaining space. The four roles being integrated into the ram lower the friction. The ram is pulled with a pulling rope over a pulley against the inset.

AREAS OF APPLICATION:

Extraction of coarse debris in hand tramming works in the mine heading. Application in mining of natural stones.

REMARKS:

Due to insufficient crushing, problems in transporting coarse debris occur. The use or application of wedge ram is right in friable bedrock or in open-pit mining where possibly large blocs have to be extracted ( e.g. marble).

Cut or sawed marble yield higher prices than blasted marble for sculpting purposes. The latter contains fine micro splits which can lead to a sudden breakage of other parts during treatment.

SUITABILITY FOR SMALL-SCALE MINING:

For underground ore mining, this technique has only a limited application but it is quite suitable for open-pit mining.


Fig.: Design and work principle of a wedge ram. Source: Lengemann Fig. 4: Wedge ram by A and J. Francois. The 4 springs a, a', a, a', are being inserted into the drill hole and if necessary the spring e in-between a and a'. In the remaining space o (compare fig. 4b) the wedge b is rammed In that has backward a quadratic guide f for the quadratic hole of 45 mm width of ram R. The 4 roles r that are let in the latter are minimizing friction. The shackle 9 serves to fix pulling rope Z through pulley v (compare fig. 4b). The ram can also being moved by a tin iron rod with handle, which is fixed at shackle g. K locking pin to limit the ram lifting.

7.4 Electric hammer drill with stand Y D Z

Stable Rock Deep Mining, Stable Rock Open-Pit
Underground Mining Extraction Mining

germ.:

Elektrischer Bohrhammer auf Stutze

span.:

perforadora electrica sobre apoyo

Producer:

China Mining Technology Consultant Centre

TECHNICAL DATA:

Dimensions:

610 × 335 × 220 mm + stand

Weight:

30 kg + drilling rod, supply cord, water hose

Extent of Mechanization:

fully mechanized

Driving Output

2 kw

Form of Driving Energy:

electric: 3 phases, 127 V, 15,7 A, 50 Hz

Mode of Operation:

semi-continuous

Throughput/Capacity:

> 3 kg × m hammer impulse, > 150 kg × cm rotation impulse, 2640 min-1, holes up to 4 m � 34 - 43 mm, drilling rods 22 or 25 mm, hexagonal with central flush

Technical Efficiency:

65 %

ECONOMICAL DATA:

Consequential Cost through Coupling Effects: power supply

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|———| high

Maintenance Experience:

low |————|————|high

Location Requirements:

none, machine is explosion proofed

Mining Requirements:

power supply needed up to the mine heading

Repleaceable Equipment

pneumatic hammer drills

Regional Distribution:

China

Environmental Impacts:

low |————|————| very high

low oil consumption in comparison with compressed air

Suitability for


Local Production:

very good |————|————| bad

Lifespan:

very long |————————| very short

Bibliography, Source: Company information

OPERATING PRINCIPLE:

With 3-phases-alternating current driven percussion hammer drill with stand and external water coolant and flush.

AREAS OF APPLICATION:

Drilling in heading and winning of mechanized small-scale mines with power supply for all rock types.

REMARKS:

Efficiency of electrical systems is significantly higher than that of pneumatic systems, which means, it requires less input for primary energy.

The performance of electrical systems is dependent of external air, which means efficient operation can be done also in greater heights.

The environmental impact (oil suspension, noise pollution, etc.) of electric hammer drills is comparably low or not existing at all.

In the case of lifespan and maintenance, doubts still remain as there has been no experience on these yet. Particularly for drilling equipment, small-scale mining maintains high standards for stability and lifespan. So far, pneumatic systems rank first under these aspects.

Besides electric hammer drills, electric mining hammers ( without rotation and flush) for cutting bits are also being marketed. They are used mainly in coal mining.

Electric Systems are only advisable if transmission from a public power supply net is available. Disadvantages of an electric mechanization in underground mining are the results of:

- sensitive technique especially of the percussion device of hammer drills
- safety problems
- low marketability.

SUITABILITY FOR SMALL-SCALE MINING:

The electric hammer should be considered as an alternative to pneumatic systems in small mines with only few working places. Its low Input of primary energy needed and environmental soundness are marks of the electric hammer, however, high cost of installation of electric power supply should be considered in the case that it is not available.

7.5 Manual mining methods

Deep Mining in Soft Rock
Underground Mining Extraction

germ.:

Manuelle Gewinnungstechniken

span.:

tecnicas de explotacion manual

TECHNICAL DATA:


Extent of Mechanization:

not mechanized

Form of Driving Energy:

manual

Mode of Operation:

intermittent

Throughput/Capacity:

capacity is very low compared with winning capacity of fully mechanized working units

Operating Materials:

none

ECONOMICAL DATA:


Investment Cost:

low

Operating Cost:

predominantly labor cost, additionally cost of wearing parts (drill bits, drill steels)

Consequential Cost through Coupling Effects:

none

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Experience:

low |————|————| high

Ore Requirements:

soft rock

Adjoining Rock Requirements:

most favorable deposits are those with stable adjoining rock and comparably soft or loose material to be mined, e.g., that of some oxidation zones, coal seams, etc.

Replaceable Equipment:

mechanized mining

Regional Distribution:

worldwide

Experience of Operators:

very good |————|————| bad


extremely high physical stress, wherever exploitation of hard raw materials is required

Environmental Impacts:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under what Conditions:

hammers, picks, chisels bits, eventually drill rods can be produced bylocal small scale industry, and probably simple hand drilling machines, in metal manufactures

Bibliography, Source: Fritzeche, Roschlau

OPERATING PRINCIPLE:

Manual mining techniques are mostly applied in soft rock in underground and open-pit mining. To be distinguished are the following:

1. Manual working with pick and shovel. Predominantly in coal mining but also in extraction of ore from residual zones and consolidated loose material, such as in gold mining wherein extracted ore is cut with a pick.

The miner often uses the method of "undermining" by drifting a split into the wall face near the bottom and cutting upward by making use of gravity.

First and foremost, this technique is common in an artisan coal mining.

2. Manual drilling by rotation and blasting. In small-scale mining more solid materials can be cut with manual rotating drills (such as Lisbeths hand rotary drill) and by blasting. These include such materials as coal, salt, sulfa, shale, gypsum, etc The drilling machines are hand driven, have a manual thrust, are guided by a stand braced at the drilling hole and operate with a percussion drill but without a flush. An auger bit removes the drill cut of the hole. The objective of any drilling is to adjust the thrust so that the chips are cut off with the maximum size in order to guaranty the lowest possible work effort for cutting. The lifespan of hand drill drilling rod is very high and lies within a minimum of 3,000 m. Attached to the drilling rods are exchangeable symmetrical or asymmetrical slot-and-cut bits with hard facing. The time duration between each sharpening is equivalent to 30 - 150 meterage, the total lifespan after about 15 - 25 sharpenings is approx. 2,000 meterage. The stands for hand driven drills are comprised of a telescoping double-tube frame which is braced with an adjusting screw at the fixing point and to the hanging wall.

3. Hard rock materials can be broken by manual percussion drilling of blasting holes and by blasting. This is a technique which is widely applied up to now in small-scale mining for high quality ore, such as gold ore, tungsten, tin and precious stones. The advancing distance per round here is shorter than in mechanized mining and is on the average of about 30 cm. A main problem is the discharging of drill cuttings or debris from the drilling holes. Most suitable therefore are small scrapers with flattened bended end. They are placed into the drill hole to scrap out drill cuttings.

Here, productivity is seen as the volume of cuttings per shift and is about 3 - 5 times as high as that of the hammer and chisel or manual minining without blasting.

AREAS OF APPLICATION:

Manual winning or extraction of raw materials in underground and open-pit mining, mainly for soft and medium soft rock.

SUITABILITY FOR SMALL-SCALE MINING:

Manual extraction In small-scale mines of the developing countries is important where no mechanization of underground work is being planned.


Fig.: Mining tools. Source: Trptow.


Fig.: A Lisbeth hand drill. Source: Treptow.


Fig.: Mining tools. Source: Lengemann

Fig. 1 - 5 double-pointed picks, fig. 1 - 3 with removable blades and fig. 1 - 2 retaining flanch on helmet by using fig. 3 a wedge following the Acmes method. Fig. 6 and 7 simple pick. Fig. 8 simple pick with removable blade. Fig. 9 and 10 pick with detachable bits. Fig. 11 cutting pick. Fig. 12 double-pointed cutting pick. Fig. 13 - 15 Belgium cutting pick. Fig. 16 acute hammer.

7.6 Pneumatic charging machine for explosives

Deep Mining General Open-Pit Mining General
Underground Mining Extraction

germ.:

Pneumatische Sprengstoffpumpe, Injektorpumpe

span.:

bomba neumatica pare explosivos, bomba inyectora

TECHNICAL DATA:

Dimensions:

70 × 70 × 100 cm LWH including tank for blasting explosives

Weight:

approx. 50 kg

Extent of Mechanization:

partly mechanized

Form of Driving Energy.

pneumatic

Mode of Operation:

semi-continuous

Throughput/Capacity:

several 100 kg explosives/hour

ECONOMICAL DATA:

Investment Cost:

not known

Operating Cost:

cost of compressed air and labor

Consequential Cost through Coupling Effects:

cost of supply of compressed air

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Experience:

low |————|————| high

Deposit Requirements:

in coal deposits with methae emission and, in all cases where electric detonation is used, non static hoses have to be applied

Regional Distribution:

wherever prilled explosives are being used

Experience of Operators:

very good |————|————| bad

Environmental Impacts:

low |————|————| very high


mining air pollution by gas and dust blown out by explosives

Suitability for Local Production:

very good |————|————| bad

Under what Conditions:

good metal manufacture with lathe

Lifespan:

very long |————|————| very short

Bibliography, Source: Roschlau

OPERATING PRINCIPLE:

Pneumatic charging machines serve as filling device to insert blasting explosives into the drill hole. Fed by compressed air line or tank, compressed air flows through a venturi Jet. The smaller the cross-section of the Jet is, the higher is the speed of streaming air. In or shortly before the Jet becomes narrowest, granulated explosive is poured into the air stream. The explosive is then transported through a conveying hose into the drill hole.

Another way is to fill a storage tank with explosives and compressed air and discharge at the bottom of the tank. This conveying system is more careful, causes less abrasion and little fine dust particles of the explosive.

In non-mechanized mines, cartridged blasting explosive can be charged with a tamping stick.

AREAS OF APPLICATION:

Charging of prilled explosives in blasting drill holes by using compressed air.

REMARKS:

Charging of drill holes with explosives is being done through the following
steps:

1. Blowing the drill hole clean so that the remaining water caused by drilling flush or influx of crack water is removed. Wet explosive can hardly be fired and occasionally leads to a missed hole. Subsequently, this results to either large size debris or breaking away of the round. To clean the hole, a conveyor hose is placed at the drill bottom to blow compressed air Into the hole which then carries the water out. The control panel should therefore be so designed so as to allow switching of air mix from explosive compressed air to pure air, alternatively.

2. Charging the drill hole with a high explosive blasting cartridge and detonator with electric ignition or ignitor fuse, by using a tamping stick or charging machine. This charging of cartridged explosive serves as the primer detonation. During insertion of the cartridge with detonator, care should be taken that electrical wires are carefully inserted into the bottom of the hole so as not to damage them.

3. Prepared safety explosive (ANC, ANO, ANFO, ANDEX), a mixture of ammonium nitrate (94 %) and oil (6 %) is inserted with the above-mentioned charging machine through the charging hose.

4. Filling of drill holes with clay, small stones or cotters.

Important for a good blasting effect is the correct use of energy which is released during the chemical reaction of explosive. This can be achieved mainly by a complete filling of drill hole with blasting explosive or with explosive components.

SUITABILITY FOR SMALL-SCALE MINING:

Pneumatic charging machines are suitable for local production, very simple and cheap remedies, which allow the use of cheaper ANO explosive.


Fig.: Schematic sketches of the general methods of compressed air charging. Source: Roschlau.


a) Jet stream transport,
b) Transporter with belt betcher,
c) Transporter with porous bottom,
d) Pressure tank transporter.

CLOSE THIS BOOKTools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)
Technical Chapter 8: Loading
VIEW THE DOCUMENT8.1 Mucking sheet
VIEW THE DOCUMENT8.2 Hand scraper and tray
VIEW THE DOCUMENT8.3 Scraper loader
VIEW THE DOCUMENT8.4 Pneumatic overhead loader
VIEW THE DOCUMENT8.5 Chute, charging hopper

Tools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)

Technical Chapter 8: Loading

8.1 Mucking sheet

Deep Mining General
Underground Mining Loading

germ.:

Blechboden als Ladehilfe

span.:

Piso de plancha como ayuda pare la carga

TECHNICAL DATA:

Dimensions:

approx. 2 × 1 m ( several pieces), 5 mm thick

Weight:

approx. 50 kg

Extent of Mechanization:

not mechanized

Mode of Operation:

intermittent

Throughput/Capacity:

for increasing efficiency of manual loading

ECONOMICAL DATA:

Investment Cost:

if scrap, then very low, approx. 100 DM

Operating Cost:

none

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Experience:

low |————|————| high

Location Requirements:

sufficient space should be available or sheets should be cut into


sizes according to space available.

Mining Requirements:

Mucking sheets should be used if loading has to be made manually without a scraper, overhead shovel loader or other mechanical loading equipment. Mucking sheets are not bound or dependent upon certain locations since they are also used or applied for cutting and filling, for abandoned workings etc. and avoid muck losses or crushing.

Regional Distribution:

used or applied in some places in Latin America

Experience of Operators:

very good |————|————| bad

Environmental Impacts:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under what Conditions:

appplication of scrap or simple cuttings of sheet steel

Lifespan:

very long |————|————| very short

Bibliography, Source: Stout, Treptow

OPERATING PRINCIPLE:

The mucking sheets are spread out at the bottom completely before cutting. The cut material is then thrown mostly on the sheets by the blasting or manual cutting. Manual loading becomes easier with mucking sheets, because the shovel can be pushed under the cut materials with less friction. The sheets are then tipped up after loading.

AREAS OF APPLICATION:

Loading device for drifting, for cutting, for shaft sinking and at reloading places where materials are loaded by hand.

REMARKS:

Mucking sheets are long lasting, very simple and effective. Before blasting, some materials should be placed on the sheets to serve as weight.

SUITABILITY FOR SMALL-SCALE MINING:

Summery of suitability

Mucking sheets are the right loading remedies for non-mechanized small-scale mining operations. With very low Investment cost, high increases In efficiency can be realized without technical modification and changes of mining method.


Fig.: Shovels for loading. a) Coal shovel, b) Muck shovel. Source: Boki.

8.2 Hand scraper and tray

Deep Mining General (vein ore mining)
Underground Mining Loading

germ.:

Kratze und Trog

span.:

Rastrillo y pale pequena

TECHNICAL DATA:

Dimensions:scraper:

1 m handle, triangular pick, tray approx. 70 × 50 × 20 cm

Weight:

together approx 15 kg

Extent of Mechanization:

not mechanized

Form of Driving Energy:

manual

Throughput/Capacity:

10 :/MS with simultaneous hand-picking

Technical Efficiency:

improves loading efficiency of manual loading

ECONOMICAL DATA:

Investment Cost:

< 100 DM

Operating Cost:

none

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Experience:

low |————|————| high

Location Requirements:

manual loading with scraper and tray is the right technique only where mine cars or kibbles are loaded.

Regional Distribution:

not known in Latin America

Experience of Operators:

very good |————|————| bad

Environmental Impacts:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under what Conditions:

simple metal manufacture

Lifespan:

very long |————|————| very short


approx. 300 shifts × 8 h

Bibliography, Source: Gerth, Salzmann, Gaetzschmann, Treptow, Freiberg Grube Alte Elisabeth

OPERATING PRINCIPLE:

Scraper and tray are supposed to ease loading and increase efficiency. Instead of loading directly everytime into the mining car using the shovel with small loading quantities involving a lot of movement, the material is scraped from the muck or heap into the Iying tray, which, when filled up, is emptied out into the car.

AREAS OF APPLICATION:

Manual loading in small-scale mining, increase in efficiency possible with such simplest remedies.

REMARKS:

Before mechanized loading was invented, scraper and tray were widely known in European ore mining during the Middle Ages. Up to this century, they are still used or applied for mining in Harz.

Gaetzschmann distinguishes a scraper with crescent-shaped concave forged head with a width of 6 - 8", and triangular scraps.

To ease or smooth pulling work, about half the length of a nose should stand out at the handle.

Scraping is particularly suitable in mines with very limited space where otherwise shovels with short handles would be used.

SUITABILITY FOR SMALL-SCALE MINING:

Well-suited remedy to increase loading efficiency with less work effort and less investment in manual small-scale mining In Latin America.


Fig.: Different forms of scrapers, Source: Gaetzschmann.

8.3 Scraper loader

Deep Mining General
Underground Mining Loading

germ.:

Schrapper, Schrapplader

span.:

trailla cargadora, cuchara de arrastre

Producer:

Wolff, MAD (2. hand)

TECHNICAL DATA:

Dimensions:

engine and loading platform 7 m × 2,2 m; also smaller units available

Weight:

several tones

Extent of Mechanization:

partly mechanized

Driving Capacity:

11 kW

Form of Driving Energy:

electric/only compressed air motor

Mode of Operation:

intermittent

Throughput/Capacity

1350 kg pulling force approx. 10 m³/h

Operating Materials:


Which:

lubricants

ECONOMICAL DATA:

Investment Cost (DM):

New:


Used:


drum (double)

18.900

without motor

7.000 - 8.000

motor 11 kW

1.410

motor

2.000

rope

680

loading platform

5.000

bucket 0,2 m³

3.400

approx.

15.000

pulley

670



rope anchor

70



loading platform

15.000




40.130



Operating Cost:

labor cost, power cost and cost of wearing parts, especially ropes

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Experience:

low |————|————| high

Location Requirements:

Due to immobility of the large and heavy loading platform, the chosen mining method should allow loading of as much material as possible from one location.

Deposit Requirements:

only applicable, where relative thick veins or gentle inclined deposits are mined

Replaceable Equipment:

trackbound intermediate conveying, Cavo-loader, overhead loader

Regional Distribution:

worldwide

Experience of Operators:

very good |————|————| bad

Environmental Impacts:

low |————|————| very high


only through energy supply

Suitability for Local Production:

very good |————|————| bad

Under what Conditions:

loading eventually can be locally produced

Lifespan:

very long |————|————| very short

Bibliography, Source: J. Siegert, Stout, Fritsche

WORKING PRINCIPLE:

A double hoist at the loading and transfer point moves both the cable with scraper bucket and empty cable through a pulley fixed at the face of heading. The scraper bucket, which is open at the end facing conveying direction is automatically loaded by scrapping through the material like a prow, and is pulled by the haulage cable up to the loading platform to be emptied into a mining car.

AREAS OF APPLICATION:

A scraper loader is used for haulage in horizontal gently steep and trackless roadways with stable ground ( not consolidated back fill, abandoned workings, etc.) as, e.g., in drifting, transport to chute, cutting of sills etc..

REMARKS:

Scraper loader was widely known and used in all types of small, medium and large-scale mining operations in Europe until the middle of this century. Special advantages have been the reliability as well as stability of such machines. Old scraper loaders are always offered at the second hand market as a mining equipment

The simplest construction of a scraper loader is the manual hoist which is economically sound for smaller quantities and shorter transports. The manual hoist works completely without a backward pulling device and pulley. Backward pulling and guiding are done by hand. One man operates the scraper bucket while a second one operates the coupling and detaching of hoist and motor. Motor capacity is approx. 1.5 - 5 kW, scrapping capacity is more than 10 t/h for a transport distance of 15 · 20 m.

If scrapers are driven from the surface, other forms of drive can also move the scraper bucket. For example, auto engines were used in small-scale fluorspar mining in Stulln/F.R.Germany.

SUITABILITY FOR SMALL-SCALE MINING:

For larger small-scale mines that are already mechanized and have adequate geological deposit conditions, the scraper lader is an appropriate remedy for mechanizing the loading despite its somewhat high cost of investment and operation.


Fig.: Sketch of a scraper loader; left, With a track-bound loading platform; right, A three-drum scraper loader. Source: Fritzsche.

8.4 Pneumatic overhead loader

Deep Mining General
Underground Mining Loading

germ.:

Wurfschaufellader

span.:

pale cargadora

Producer:

Salzgitter MAD (2. hand), Atlas Copco

TECHNICAL DATA:


SALZGITTER HL 221 T/TSL Type N

Dimension:

1.56 × 1.05 × 2.44 × m HWL, roadway height min. 2.5 m

Weight:

3.600 kg

Extent of Mechanization:

partly mechanized

Driving Capacity:

5 - 7 m³/min compressed air, 50 mm feed line

Form of Driving Energy:

pneumatic

Mode of Operation:

intermittent/semi-continuous

Throughput/Capacity:

60 - 100 t/h with 160 I bucket content

Operating Materials:


Which:

lubricants

ECONOMICAL DATA:

Investment Cost:

used 5000 to 10.000 DM

Operating Cost:

low

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Experience:

low |————|————| high

Personnel Requirements:

low

Location Requirements:

track gauge 450 - 900 mm, compressed air

Ore Requirements:

none

Replaceable Equipment:

loading by hand

Regional Distribution:

worldwide

Experience of Operators:

very good |————|————| bad

Environmental Impacts:

low |————|————| very high


only by energy supply

Suitability for Local Production:

very good |————|————| bad

Lifespan:

very long |————|————| very short

Bibliography Source: Siegert, Salzgitter, companies brochure, AC-Handbook

OPERATING PRINCIPLE:

Pneumatic overhead loader is controlled while running or from a platform. The bucket is being filled during forward driving and emptied into a mining car located at the back by turning the bucket over the whole machine.

AREAS OF APPLICATION:

loading in drifting loading in ramps loading in haulage way under chutes clean up/loading at special working places under loading in cross-cuts draw points

REMARKS:

For decades, this type of overhead loader was widely known in small-scale ore mining both in Europe and Latin America and also in other mining countries. It made itself known by its stability, simplicity and long lasting quality.

Overhead loaders are also available for operating in ramps with an angle of deviation of 25 goniometer.

Overhead loader operate as track bound or as trackless machines. For the latter, it would need more inside roadway diameter.

SUITABILITY FOR SMALL-SCALE MINING:

The right application for overhead loaders is, where an already mechanized efficient drilling system and conveying installations exist. Likewise, the existing compressed air system should be adjusted to the comparably high energy consumption of an overhead loader. Under these conditions, overhead loaders can do the loading work economically and efficiently.


Fig.: An overheadloader PPN-1s. a) side view; b) front view. Source: Roschlau

1) bucket
2) protective grating
3) control panel
4) machine platform
5) drive system
6) footboard
7) spray device
8) driving motor
9) lifting motor


Fig.: An overhead loader. Source: Salzgitter Company Information.

8.5 Chute, charging hopper

Deep Mining General (steep formation)
Underground Mining Loading

germ.:

Bunkerschurre, Ladekasten

span.:

tolva de buzon, cajon pare cargar

TECHNICAL DATA:

Dimensions:

approx. 2 × 2 × 2 m

Extent of Mechanization:

not mechanized

Form of Driving Energy:

loading remedy using gravity

Mode of Operation:

intermittent

Other Opportunities:

pneumatic cylinders for opening

Operating Materials:

none

ECONOMICAL DATA:

Investment Cost:

if constructed with wood, very low cost of material

Operating Cost:

none

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Experience:

low |————|————| high

Deposit Requirements:

inclined or especially steep ore vein deposits, where the vertical interval can be used for loading. Particularly suitable in mines with roadways in which daydrifting is placed under work facings.

Mining Requirements:

all mining methods that lead upwards and allow partly material storage

Replaceable Equipment:

loader as overhead loader under chute

Regional Distribution:

widely known in medium-scale mining but unknown in small scale mining

Experience of Operators:

very good |————|————| bad

Environmental Impacts:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under what Conditions:

simple wooden constructions

Lifespan:

very long |————|————| very short

Bibliography, Source: Stout, Fritsche, Armstrong

OPERATING PRINCIPLE:

The chutes that are placed under cavities caused by the extraction under drop-holes or bunker, are designed to hold the material above the loading height of mining cars. By opening the chute, the material falls into the mining car which is loaded by gravity.

AREAS OF APPLICATION:

Material storage and loading of mining cars in haulage road.

REMARKS:

Sticky muck becomes a problem when it muds off and badly affects the transport by gravity. To Increase the lifespan of chutes, the material storage should show a certain minimum filling requirement, to avoid direct impact of material on the feed gate.

SUITABILITY FOR SMALL-SCALE MINING:

Under suitable conditions (deposit geology, mining method), reloading can then often be avoided and gravity can be used for loading purposes. Thus, chutes are very suitable for application in small-scale mines which are low mechanized.


Fig.: Charging hopper. Source: Stout.


Fig.: Charging hopper. Source: Stout.


Fig.: Chutes with compressed air drive, left from below, Closing gate; right from above, Closing gate. Source: Fritzsche


Fig.: Chute; left, longitudinal section; right, general view. Source: Armstrong


Fig.: Chute; left, side view; right, perspective view. Source: ITDG.

CLOSE THIS BOOKTools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)
Technical Chapter 9: Hauling
VIEW THE DOCUMENT9.1 Manual winch
VIEW THE DOCUMENT9.2 Motor cars as hauling machines, depth indicators
VIEW THE DOCUMENT9.3 Block and pulley
VIEW THE DOCUMENT9.4 Trackless and track bound haulage
VIEW THE DOCUMENT9.5 Passenger lifting moving ladder

Tools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)

Technical Chapter 9: Hauling

9.1 Manual winch

Deep Mining General Open-Pit Mining General
Underground Mining Hauling

germ.:

Handhaspel, Winde

span.:

guinche manual, malacate, torno

Producer:

INCOMAQ, COMESA, DERENA, FIMA, Metal Callao, E.P.S.

TECHNICAL DATA:

Dimensions:

approx. 2 × 1.5 × 1 m WLH

Weight:

approx. 10 kg

Extent of Mechanization:

not mechanized

Driving Capacity:

0.3 - 0.6 kW in 2 man operation

Form of Driving Energy:

manual

Other Opportunities:

winch (animal power gear), hydromechanic with water wheel

Mode of Operation:

intermittent

Throughput/Capacity:

depth up to approx. 45 m, max. 100 m with 0.1 - 0.2 m/s hauling speed

Technical Efficiency:

very high if friction is low

ECONOMICAL DATA:

Investment Cost:

approx. 200 DM if locally produced with wood

Operating Cost:

exclusively labor cost

Consequential Cost through Coupling Effects:

cable (rope), bucket 0.05 - 0.2 m³ content

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Experience:

low |————|————| high

Location Requirements:

shaft or blind shaft with hoist chamber at the upper end of conveying distance or drift

Replaceable Equipment:

leather bag hauling with rope pulled by hand, which is typical for small-scale mining

Regional Distribution:

also known in small-scale mining in Latin America

Experience of Operators:

very good |————|————| bad

Environmental Impacts:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under what Conditions:

wood or metal manufacture

Lifespan:

very long |————|————| very short

Bibliography, Source: Agricola, Delius, Hartmann, Hentschel, Wagenbreth, Slotta

OPERATING PRINCIPLE:

With one or two handles the conveying rope is wound up by hand on a direct coupled drum.

AREAS OF APPLICATION:

Ore and material conveyance also water transport and passenger lift in shafts and roadways of small-scale mines.

REMARKS:

Winch suspension with counter weight and counter rope to lower the necessary leverage. To equalize the static load moment tapered cable drums were invented. If the bucket hangs deep within the shaft, the load is higher due to the weight of rope. The load moment of hoist is then minimized by the small drum diameter, while the stronger the load is wound up, the weight of the hanging rope is smaller and the drum diameter increases. In case of static load, the following formula is used:

Mstat. = rdrum × (actual load + weight of material + rope weight)

which calculates the conical angle of drum.

For the purpose of personnel lifting it is important to use safety dogs and breaks.

The integration of anti-friction bearings decreases friction losses.

SUITABILITY FOR SMALL-SCALE MINING:

In comparison to the simple form of conveying by leather bag hooked on a rope, the manual winch which is especially used as double drum system with good ball bearings, makes work considerably easier. On the surface, it is however preferred to use animal power.


Fig.: Windlass with break. Source: Armstrong


Fig.: Tapered drum of winch to equalize cable weight as double cable operation. Source: Ponson.


Fig.: Manual winch. Source: Agricola

9.2 Motor cars as hauling machines, depth indicators

Deep Mining General, Open-Pit Mining General
Underground Mining Hauling

germ.:

Fordermaschinen mit PKW-Chassis, Teufenstandsanzeiger fur Schachtforderung

span.:

maquina de extraccion con chasis de auto, indicador de profundidad pare el transporte en el pozo

TECHNICAL DATA:

Weight:

500 - 800 kg

Extent of Mechanization:

fully mechanized

Driving Capacity:

30 - 100 kW

Form of Driving Energy:

internal combustion engine

Other Opportunities:

none

Mode of Operation:

intermittent

Operating Materials:


Which:

lubricants

fuels

water for

Quantity:

approx. 1 I/10 hours operation 5 - 15 I/hours operation cooling

ECONOMICAL DATA:

Investment Cost:

if a second-hand car chassis is used, approx. 2000 DM

Operating Cost:

high fuel cost

Consequential Cost through Coupling Effects:

hauling cable, bucket

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Experience:

low |————|————| high

Mining Requirements:

mine design should allow shaft hoisting and inclined shaft hoisting from surface

Replaceable Equipment:

animal power gear, winch etc.

Regional Distribution:

known in Colombian mines, but also used to drive a ski lift at Chacaltaya, Bolivia

Experience of Operators:

very good |————|————| bad

Environmental Impacts:

low |———————| very high


pollution through used oil and exhaust gas

Suitability for Local Production:

very good |————|————| bad

Under what Conditions:

old cars redesigned by auto mechanics

Lifespan:

very long |————|————| very short

Bibliography, Source: Hentschel, Priester

OPERATING PRINCIPLE:

The small-scale mining industry uses car chassis as a simple hauling system of which engine, clutch, gear, differential and drive axle are still in operation. One side of the drive is put away and at the other side, the cable is wound up by the remaining rim used as drum. The radiator is replaced by an open barrel to serve as water tank for a closed cooling circuit. The haulage is controlled by forward and backward shifting.

A depth indicator which reflects the location of the bucket on a well displayed board, substantially helps in controlling the shaft hoist, especially if rope marking fails due to foul rope. Simple designs of depth indicators are:

- string indicators, which wind up a string on a screw bolt at the axle of the hauling machine or the rope drum along the thread. The exact position of the bucket is indicated or shown on a weighted or gauged scale by a clean thread and a nonelastic string guided through a pulley and suspended by a weight at the string end.

- thread indicator comprised of a thread coupled with an axle of the cable drum or hoist and drives a nut holed by a pin avoiding the nuts rotation.

For the correct performance of string indicators it is necessary that the cable is equally wound up.

Beside depth indicators, signal systems like for example curb bells (see 1st photo, Technique 4.3), are most practical. Even in inclined shafts, mechanized curb bells can be operated over several hundred meters by moving the tongue of the bell placed at the opening with a loosely distributed wire. In shafts which are used simultaneously for hauling and personnel lifting, operation of signal bells should be possible from any point for safety reasons.

REMARKS:

Advantages are, the widely known auto techniques and therefore repairs can be done by local technicians, easy procurement of wearing spare parts, and their comparably low cost.

To avoid abrasion of cable or rope in inclined shafts, it is important to install pulleys by which the rope is free-wheeling. Under no circumstances should it drag along the floor. At the same time, to avoid corrosion, the wire should be oiled or greased. This can multiply the hauling cable's lifespan several times.

SUITABILITY FOR SMALL-SCALE MINING:

Car chassis is very suitable for hauling due to their availability everywhere at reasonable prices especially for second hand units. Another advantage is also the availability of very good repair and maintenance knowledge.

Development of hauling machines for deep shafts, respectively with steam engine or electric motor drive. Small rope drum for shafts of low depth was enlarged for deep shafts - was redesigned into a spiral basket to get a small load arm for huge loads (hoisting cage in the depth + weight of rope) - was redesigned into bobbin with the same principle such as that of spiral basket- changed into the new principle of band wheel (Koepe wheel): both hoisting cages are on a common rope (weight equalization by under-rope in shaft).


Fig.: Tipping bucket for inclined haulage. Source: Fritzsche.


Fig.: Development of a rope drum. Source: Wagenbreth

Development of hauling machines for deep shafts, respectively with steam engine or electronic motor drive. Small rope drum for shafts of low depth - was enlarged for deep shafts - was redesigned into a spiral basket to get a small load arm for huge loads (hoisting cage in the depth + weight of rope) - was redesigned into bobbin with the same principle such as that of spiral basket - changed into the new principle of band wheel (Koepe wheel): both hoisting cages are on a common rope (weight equalization by under-rope in shaft).


Fig.: Hauling systems. Source: Stout.


Fig.: Double spindle depth indicator. Source: Hoffmann


Fig.: Break, depth indicator, end release. Source: Hoffmann

9.3 Block and pulley

Deep Mining General, Open-Pit Mining
Underground Mining Hauling

germ.:

Flaschenzug

span.:

polipasto, aparejo

TECHNICAL DATA:

Dimensions:

several pulleys, dimension depends on the weight of material being handled

Weight:

few kg

Form of Driving Energy:

manual, animals, electric, hydromechanic, pneumatic

Other Opportunities:

pedal drive

Mode of Operation:

intermittent

Technical Efficiency:

mechanical remedy for conveying and lifting material

ECONOMICAL DATA:

Investment Cost:

< 200 DM with pulleys which are available in the market

Operating Cost:

none

Consequential Cost through Coupling Effects:

rope and bucket should be available

CONDITIONS OF APPLICATION:


manual

Operating Expenditures:

low |————|————| high


mechanized

Maintenance Experience:

low |————|————| high

Regional Distribution:

not applied for haulage in small-scale mining

Environmental Impacts:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

woood or metal manufacture

Lifespan:

very long |————|————| very short

Bibliography, Source: Born

OPERATING PRINCIPLE:

With several pulleys, the weight of the bucket is distributed into several rope units.

AREAS OF APPLICATION:

Remedy to make such works as haulage and transport easier.

REMARKS:

Block and pulley demand an increased length of rope since the pulling distance doubles with each pulley causing respectively half the tension. Still, the use of block and pulley is meaningful in adjusting the cycle of the winding period and haulage capacity to the operating cycle of loading and unloading.

In ecuadorian mining of aluvial gold deposits, large stones are pulled up into the surface with block and pulley with simple tripod during shaft sinking.

SUITABILITY FOR SMALL-SCALE MINING:

Suitable for the small-scale mining industry as an auxiliary equipment. Also contributes to a continuous operation in haulage work.


Fig.: Block and pulley. Source: Born.

9.4 Trackless and track bound haulage

Deep Mining General Open-Pit Mining General
Underground Mining Hauling

germ.:

Gleislose und gleisgebundene Frderung unter Tage

span.:

Transporte en interior mine sobre y sin rieles, aparejo

Producer:

Buena Fortuna, COMESA, DERENA, Eduardo, FAHENA, FAMESA, Famia Ind., FIMA, Fundicion Callao, FUNSA, FUNVESA, H.M., IAA, INCOHEC, inc. Met. Van Dam, Krug, M.M. Soriano, MAENSA, MAEPSA, MAGENSA, MEPSA, Metal Callao, E.P.S.: Metalurgica Lacha, PROPER, Volcan

TECHNICAL DATA:

Extent of Mechanization:

not mechanized

Form of Driving Energy:

gravity and muscular strength

Other Opportunities:

roof switch: probably pneumatic tension reel, battery locomotive, compressed air locomotive

Mode of Operation:

intermittent

Throughput/Capacity:

efficiency of hand pushed wagons on properly made laying of rail track inclusive of way back approx. 1800 - 2000 kg × km/mh

ECONOMICAL DATA:

Investment Cost:

mine car: 500 DM/piece (used); steel rails and switches, type S 10: 30 DM/m (used)

Consequential Cost through Coupling Effects:

steel rails and switches: Jim-Crow (Santiago), track gauge, slope rate

Bibliography, Source: Siegert, Bernewitz, Stout, Villefosse, Delius, Goschen, Gerth/Salzmann, Treptow, Bergbaumuseum Eisenerz Steiermark, VOEST, Hutte

OPERATING PRINCIPLE:

For transporting in underground mining, trackless and track bound haulage are to be distinguished:

Trackless haulage:

This can be done without mechanized remedies by back-pack over a short distance for hand picked and high-grade, selective mine ore, or by wheelbarrow or carts with rubber wheels. The shuttle-belt conveying method originating from the mining at Mansfeld's thin copper shales where the workable thickness has only 90 cm, is also known for immediate transporting to the main galleries. Therefore, a hoist pulls a piece of conveying belt where the ore is piled on to the main conveying system. This method makes sense where conveying belts are in operation and sufficient construction material is available. The wheelbarrow is designed to lead the load weight to the wheels by arranging the axles position in front of the center of gravity. The miner handles the steering and driving.

Biaxial mine cars work analogously. Trackless hauling needs a properly cleaned, balanced and stable ground to guaranty transporting without friction as much as possible. Boards are lined along the bottom as support on which cars run with or without track nail. This leads to the so-called track bound haulage.

Track bound haulage:

If laying of rails is made properly, track bound haulage guaranties friction-free transporting of loaded cars even without locomotives. Still, comparably high expenditures for infrastructure of rail tracking becomes inevitable. On the other hand, keeping the tracks clean is easy and they allow transporting of heavy tools, machines as well as construction materials.

The rails could be made of wood or metal: wooden rails are less expensive, resistant against acidic water, but allow less axle load in comparison to steel rails and mouldering appears fast in a humid environment.

Steel rails and switches (riel de coville, linea decauville) are comprised of:

rails

steel

fishplates and screws


sleepers

wood, steel

screws, wing plates


switches

steel

crossings

steel

turn sheets

steel

Mining cars:

Mining cars are composed of a drive system, normally with four equally sized wheels and coupling devices with buffers as well as a container. Unloading of mining cars is done by dumping devices or gates to be opened forward, backward or to the side. Rigid and closed cars can be unloaded by a rotary car dumper.

The most common way to move mining cars in small-scale mines is to push them forward by hand, wherein the loaded car almost runs alone by itself along the track, and the empty one has to be pushed slightly upwards.

If the roadway cross-section is wide enough in main roads, mining car transport can be supported by horses. Mining horses can pull 6 - 10 fully loaded cars if rail track laying is made properly. Until the beginning of this century, this kind of transporting was done in Central Europe.

For haulage in long and straight roadways, mining cars can be driven by a revolving rope on which clamping devices fasten the cars. The circulating haulage cable or chains can run along the roof or bottom and are guided by track carrier rollers.

Finally, mining cars are pulled by locomotives which operate with an electric drive as trolley or battery locomotives, with compressed air and, as an exception, driven by diesel engines. All locomotives are very costly, heavy and involving much expense in technique, maintenance and repair, etc.

Turn sheets:

To change direction, the mining car is pushed on a turntable which is comprised either of a flat conical disc or of a plate With adopted rails. If the car stands on the plate, it is turned around by hand and the car is pushed on the railway to a new direction.

Vertical switch:

Vertical switches are used to connect ramps with floors or sublevels which can be tipped up or down to let cars go under. Thus, the use of mining cars for roadway haulage as containers for ramp or inclined shaft haulage, is possible without reloading. The haulage cable has to be hooked at the mining car with a safety hook.

Roof shunts:

Roof shunts are used in vein ore small-scale mines, where only one railway goes to the heading. To handle two or more cars coming in and going out, it should be possible to put an empty car at the side if the car at face is loaded. The roof shunt now offers an opportunity to hook the empty car and lift it up from the rails with block and pulley or by a pneumatic hoist and switch it sideways. In case the loaded car has already passed, the lifted car is then put back on track.

Haulage in ramps and shafts is done either trackless or track bound analogously. In a trackless haulage, a mine car either simply runs on proper ground (only short distance) or a haulage container slides along wooden bars. In a track bound haulage, the rails are laid within the ramp. In steep ramps, the track system, especially the rail sleepers also as a manway. What is important is to install passing places in case miners have to pass by the mine cars. The mine car then runs along the railway pulled by a hauling cable.

REMARKS:

Mining cars:

Villefosse introduces an English mine car without its own dumping device that can be opened at the backside and dumped at the unloading point. Counter weights with right dimensions simplify the handling. The car has brakes.

For mines with shaft haulage, mine cars can also be designed so that the kibble can be carried on its chassis thus, avoiding multiple reloading.

With rail nail, two big wheels under the center of gravity plus two small ones. Driving is done on two wheels.

For hauling in ramps and slopes and in case the hauling cable or rope breaks, it is proposed to install fishing hooks or gripping devices which fall int o the bottom or in front of sleepers to apply brakes or derail the car, thus avoiding its speeding down.

Steel rails and switches:

For haulage wih cars pushed by hand without drive, the right falling gradient should be > 0.5° to the opening. The same also applies for water supply and drainage.

Falling gradients of railways for full mine cars (by Gerth, Salzmann):

straight railway

1.2 %

curves

1.8 %

switches

1.8 %

switches in curves

2.0 %

Track gauge: normal 600 mm

In roadways with 1.5° to 3° falling gradient, haulage without driving machines can be done by stopping the cars with brake billet or brake devices. Higher gradients even make difficult the upward movement of empty cars.

To manage higher gradients in slopes, counterweights or shuttle operation are appropriate to pull up empty cars by using the weight of loaded cars running downward.

Roof shunts:

Roof shunts need a very small space. They can be used wherever the width of gallery allows without making changes in the railway.

Haulage in working:

Haulage by hand trams with 1/3 - 1/4 of the capacity of that of mining cars in 3 - 30 falling ways along the bottom or on wooden tramways which can also be moistened to reduce friction. Trammed by a shoulder belt.

Haulage in steeper roadways (15° - 40°): application or use of chutes made of wood or of iron plates.

In galleries or rise drifts with > 45° falling, gradient materials will fall along roller tracks.


Fig.: Hauling with a cycling ground rope. Source: Lengemann.

Fig. 1 and 2 clamping device. Fig. 3 demonstrates, how to handle the clamping devices shown in fig. 1 and 2. Fig. 4 operators car with clamping device by Ramsay. The rope can be clamped between jaws a, b and d with the hand wheel h (Fig. 4a,4b,4c), if lever c is in the position 1 (fig.4a). The rope is being disconnected, if the lever c is brought into position 2 and 3; the lower jaw a, b that is designed as a lever looses its support and goes back into the position shown in Fig. 4e and Fig. 4f. Fig. 5 operators car with clamping device of mine Ironstone of Tredegar corporation in Wales. The screw spindle s that is rotated by hand crank c clamps or disconnects the rope. Fig. 6 clamping device by Hanson is fixed at the iron rods bb' of operators car. The clamping of the rope is done with wedge k that is guided by bolts in the slots e and handled with lever c. At the clamping devices shown in Fig. 4 and 5 an automatic disconnection from the rope can be realized by placing barriers at the ends of the track which hit lever c or the handle of crank c. Since an operator is not needed anymore seats are useless. The hooks shown in Fig. 7 are to connect the rope with the clamping devices that are shown in Fig. 4 - 6.


Fig.: Mining cars; above rocker dump truck; below, end dump truck. Source: Armstrong


Fig.: End dumping truck; left, back view; right, side view. Source: Bernewitz


Fig.: Mining car with fishing hook. Source: Treptow


Figures

Fig.: Wings rails, common shape. Source: Fritzsche.
Fig.: Gauge for rail laying. Source: Frtizsche.


Figure

Fig.: Attachment device composing of three elements; Scheidt Company, Essen-Kettwig. Source: Fritzsche
Fig.: A hammer head nail. Source: Fritzsche.


Fig.: Swiches and rails. Source: Stout.

Above left:

rigid turning device for mining cars;

Above right:

simple turntable;

Below left:

track extension in face;

Below right:

retailer.

9.5 Passenger lifting moving ladder

Deep Mining
Underground Mining Hauling

germ.:

Fahrkunst

span.:

ascensor rosario en vaiven

TECHNICAL DATA:

Dimensions:

up to 800 m depth (Samson Mine in Harz)

Weight:

very high

Driving Capacity:

for example 5 kW for more then 200 m depth in Samson Mine

Form of Driving Energy:

electric or mechanic ( very low R.P.M. needed, e.g. water wheel)

Throughput/Capacity:

frequency: 6/min

Operating Materials:


Which:

lubricants

ECONOMICAL DATA:

Investment Cost:

high

Consequential Cost through Coupling Effects:

aggregates for power supply

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————|high

Maintenance Experience:

low |————|————|high

Replaceable Equipment:

all hoisting systems for passengers

Regional Distribution:

historical technique, today only in Samson Mine in Harz, in Samson-Museum

Experience of Operators:

very good |————|————|bad

Environmental Impacts:

low |————|————|very high


only from energy supply

Suitability for Local Production:

verry good |————|————|bad

Under what Conditions:

wood manufacture

Lifespan:

very long |————|————|very short

Bibliography, Source: Samson-Museum, St. Andreasberg, Treptow, Gentz,H., Die Fahrkunst des Oberharzer Bergbaus in Bergbau-Rundschau, Jg. 7, 83 ff.

OPERATING PRINCIPLE:

Passenger lifting moving ladder is a system of hauling passengers in a vertical or inclined shaft. Two pairs of ropes or rods (wood, steel) are driven counter wise up and down by an approx. 1.5 - 2 m wheel. Frequency is very low (approx. 5 - 10 min-1). Foot boards and handles are attached on the rope pairs every 3 - 4 meters. At the moment the movement reverses, foot boards of both rope pairs are facing each other in one level due to the counter movement. Upward or downward haulage is then possible by transferring systematically from one pair to the other. Ropes lead through intermediate platforms in the shaft which serve as safety installations. Every 30 - 50 m, a catch fork secures the rope pairs against falling by broken rope. In inclined shafts, rope pairs are guided over slide boards or rollers.

REMARKS:

In deep mining in the Harz region, the introduction of the moving ladder considerably reduced travelling and therefore contributed to increased efficiency in mining operations. Invented by Drell in Zellerfeld/Harz in 1833.

In vein ore mining, haulage shafts usually are drifted in ore. Only moving ladders allow a mechanized passenger lifting in these shafts where falling gradient often changes.

The balanced weight of both rope pairs of the moving ladder has its real advantage of having to overpower only friction, the weight of travelling miners, and weight of 3 · 4 m rope. The driving energy may remain low.

In Harz, the ropes were preserved with a mixture of grease and beeswax. This mixture gave a more than 50 years of protection from corrosion.

Wire cables were designed so as to reduce into a smaller diameter downwards. This reduced the weight of the ropes.

SUITABILITY FOR SMALL-SCALE MINING:

Moving ladder is the right mechanized passenger lifting system for deeper shafts, but needs the installation of a haulage system for materials in a parallel shaft.

Schematic draw of function of a moving ladder during miners going out of the shaft W crankshaft, driven by water wheel or steam engine, G1G2 both, the up and down moving rods of the ladder, 1 and 3 dead centers of rod movement: The miners step over to then upwarts going rod or they step out at surface, 2 the left rod is lifted with miners, 4 the right rod is lifted with miners. Additionally for protection in the passinger lifting shafts ladders have been installed.


Fig.: Moving ladder. Source: Wagenbreth.

Schematic draw of function of a moving ladder during miners going out of the shaft W crankshaft, driven by water wheel or steam engine, G1G2 both, the up and down moving rods of the ladder, 1 and 3 dead centers of rod movement: The miners step over to then upwarts going rod or they step out at surface, 2 the left rod is lifted with miners, 4 the right rod is lifted with miners. Additionally for protection in the passinger lifting shafts ladder have been installed.

CLOSE THIS BOOKTools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)
C. Surface mining
VIEW THE DOCUMENTC.1. Definition
VIEW THE DOCUMENTC.2. Initial conditions and problem areas
VIEW THE DOCUMENTC.3. Factors related to environment and health
VIEW THE DOCUMENTC.4. Pit and quarry industry

Tools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)

C. Surface mining

C.1. Definition

Like underground mining, surface mining involves the production of mineral raw materials. In the latter, production takes place at surface. Surface mining processes solid rock, loose rock and alluvial deposits. Production takes place on the land surface as well as in rivers and seas, free of deep sea mining. The production activities in surface mining particularly alluvial deposits with heavy and precious metals, entails mainly the processing of products although here an attempt is made to contribute to an improved system through a strict separation of areas of activities. In the areas of production and hauling, and in draining, various techniques are applied which are used as well in underground mining. A renewed discussion of these devices will not be undertaken in this section.

C.2. Initial conditions and problem areas

A number of different types of deposits are found even in the limited field of alluvial precious metal deposits. This brings about various problems in mining production, particularly in processing.

The following are the most important of those alluvial deposits which have exploitable deposits of gold, as well as tin and tungsten, zircon and sand and gravel minerals and which are appropriate for small-scale mining:

- recent fluviatile sediments in riverbed areas. This type of deposits is common in the Andes. The high morphodynamic in this mountainous region with its erosion and sedimentation, accounts for a recent genesis of rich precious metal deposits. These unconsolidated loose sediments either are exploited under water using dredges or suction dredges operating directly from the river. During the dry season, or when the riverbed is generally dry as a result of the diversion of the river, these are mined manually or mechanically with shovels, wheel loaders etc. Examples are the riverbed alluvial deposits of eastern scarp of Bolivia's Andes such as the Rio Tipuani, Rio Mapiri, and Rio Kaka. Analogous to the above mentioned gold deposits, recent fluviatile alluvial tin deposits are exploited, e.g. on the Rio Huanuni, Dept. Oruro, Bolivia. After 500 years of mining history, these deposits additionally exhibit anthropogenetic characteristics 1(natural erosions from anthropogenous forms such as waste deposits, tailing ponds).

- fluviatile fossil placers and terrace deposits. Being older geological formations, these Palo- frenches (sediment filled old V valleys) and graded terraces are often already solidified. Due to the high mobility of cementing minerals as a result of the climatic conditions of the tropics, even recent accumulations are already solidified. This causes difficulty in mining, and particularly in processing when only liberated feed may be worked upon. Fossil placers of this kind are frequently overlapped with more recent sediments which marks the transition to underground mining. Provided that sufficient quantities of water are available, these alluvial deposits are exploited either hydromechanically by monitors, manually or mechanically. Examples are the gold deposits in the Cangalli series, e.g. Molleterio, Dept. La Paz, Bolivia.

- glacial und fluvioglacial alluvial deposits, moraines and sediments in the pleistocene, that is, recent glaciation of the Andes. Being sediments which have been exposed only to a short and purely mechanical transport devoid of a natural concentration through separation or chemical re- grouping, these alluvial deposits usually contain relatively marginal tin and tungsten deposit. As a result of the negligible natural size reduction to which the material has been exposed, the ores are extensively unliberated. Accordingly, the processing of ores of this kind must also involve crushing and grinding. Otherwise the sediment is usually unconsolidated and is mined using manual or mechanized methods of open-pit mining Example: El Rodeo, Cord. Quimsa Cruz, Dept. La Paz, Bolivia.

- mineral bearing rock slides, llamperas. Inferior forms of heavy mineral alluvial deposits exhibit mineral bearing fell rocks which, analogous to glacial alluvial deposits, are unliberated and partly in huge blocks. After it is produced using a mining method (drilling and
blasting), the material is processed in a manner similar to an ore exploited underground. The tungsten bearing fell rocks of the Cerro Chicote Grande, Dept. Oruro, Bolivia, which is mined by the Cooperative Minera Taminani, provide an example.

- anthropogenous deposits such as waste stockpiles, heaps, tailing ponds originating from old production and processing plants. This group of deposits offer a huge potential not only for large scale but also for small scale mining operations.

The following are the reasons behind the wide range of valuable contents of waste deposits:

- the negligible recovery of the processing plants not only of large-scale operations e.g. the COMIBOL in Bolivia with its current output at 40% of the metals but also of small-scale operations,

- the mining of previously rich deposits for centuries for which have left behind comparatively rich waste deposits,

- the mining economy of colonial Latin America which concentrated on precious metals such as gold and silver dumped by-products such as tin, tungsten, among other base metals.

- the sophisticated improved processing techniques which today is capable of, for instance, producing precious metals out of pyrites, led to the conversion of previous waste deposits into new minable deposits.

Today the above-mentioned alluvial deposits constitute an important field of activity in small-scale mining. The significance of these reserves for the national mining industry, and with it small-scale mining, will definitely increase.

Low costs of production, previously crushed material and a reserve situation which, comparatively, can be estimated with certainty, combined with a negligible investment risk, are factors which make these deposits appear predestined for small-scale mining.

Regardless of location, water usually creates crucial problems. In the case of production from a riverbed, besides the high costs of pumping and drying, excess water creates extremely difficult and dangerous working conditions.

To dry it out, the flow of the river is redirected by constructing of flanking dams on one side of the riverbed so that the other side is left to dry and is thus made available for mining.

The yearly turnus of precipitation in the alternating dry and humid tropics characterised by a marked dry and wet season, causes huge fluctuations in the water level: special characteristics of the mesoclimatic specifications in high mountain regions and local precipitations in the catchment area may cause an extreme rise of the river's water level within a short time. The planning of mining is thus influenced significantly by this unpredictable factor.

In the case of production in a dry location, the supply of industrial water requirements of mine and processing plants is particularly a problem. This is especially so when huge quantities of water are necessitated by hydraulic mining methods using monitoring. Such hydraulic mining is often necessary in places where partly a consolidation of materials of alluvial deposits has occurred. These places are usually located high above the draining level and hence difficult to supply with industrial water.

Otherwise, the technical deficiencies of small-scale mining in open-pit mining are significantly lesser compared to those in underground mining. The bigger space requirements of modern technology is not a problem at surface. Production and loading techniques are also available in the countries along the Andes and maybe utilized for the production of raw materials at surface.

As in underground mining, the degree of mechanization of operations dictates production capacity in open-pit mining. The ratio of production of manual-primitive mining to fully mechanized loading and haulage lies at present over 1: 100. In open-pit mining, huge amounts of materials may have to be produced and hauled for negligible raw ore grades. Only through a consequential, step by step partial mechanization is it possible to progress from the subsistence mining of the individual gold digger, from the margins of the subsistence level to a secure existence.

In partial mechanization, the bottlenecks are found in the provision of an energy supply which is reasonably priced and is appropriate rather than in the availability of mining methods (the technology of mining and transport in mining of alluvial deposits is definitely simpler compared to that of the underground mining).

Although it is difficult to draw a distinction between mining and processing in the field of open-pit production, it must be emphasized that critical problems in mining of alluvial deposits in the small and in the smallest scales may be found in the processing. Hence the present work puts emphasis on processing techniques.

C.3. Factors related to environment and health

In many ways, production activities of surface mining have placed a strain on the ecosystem. Apart from the dangers to the environment posed by equipment and vehicles run by internal combustion which produces

- exhaust fumes
- waste oil, and
- noise

open-pit mining disturbs the ecological balance by destroying vegetations and pollution of rivers.

- Pollution of rivers. Huge quantities of water are contaminated with mud as a result particularly of the open-pit production of alluvial deposit materials from recent riverbeds and the hydraulic mining of alluvial deposits. Usually no purification of the water follows. The effects of the suspended sediment burden endures. In some places, this may extend up to a distance of over 300 km down the river. In irrigated agriculture, the sediment burden renders cultivation difficult. In the dry season, the sludge concentration is especially high and therefore, has serious consequences for people living in areas down the river. On one hand, the quality of drinking water, which particularly in lowlands is taken directly from rivers, suffers. Filtration procedures are generally not known. On the other hand, the river fauna is altered or is exterminated as a result of changes in the aquatic environment of the rivers. The consequences are felt not only by fishermen. It is also felt in the supply of food containing animal protein. The river system Rio Tipuani, Rio Mapiri and Rio Kaka in Bolivia presents an example. It can be seen at first glance in which river gold production is being undertaken.

- Dissappearance of vegetation. The huge space requirements of open-pit mining can mean the extensive destruction of vegetation. In the humid tropics that is the climatic region of the eastern scarp of Andes, this has led to the well-known phenomenon of soil erosion (slope sliding, soil flushing, further sediment burden of rivers).

C.4. Pit and quarry industry

Among the raw materials of pit and quarry industry are various minerals and rocks, which are found in the most varied forms of deposits, used in the most varied ways, and which among other things, have extremely differing price values. The nature of mining production, depends on these and other parameters - whether this takes place on the surface or underground - the processing method, the manner of trading, the market and particularly, whether the raw material can be transported. For instance, while highly valued refractory raw materials can pay for their transport worldwide, the construction raw materials can only be marketed within a closeby region due to their low value.

The following overview according to Schneiderhhn lists the main applications of non-metallic raw materials and indicates which raw material can be exploited mainly in open-pit mining (bold and italic):

Light metal ores

Metal ores: Aluminum, Magnesium, Cesium, Rubidium, Potassium, Sodium, Lithium, Strontium, Beryllium, Calcium, Silicon.

Precious stones, gem stones

Salts and fertilizing minerals
Mineral Salt, Potassium Salt, Leucite, Alunite, Saltpeter, Limestone, Gypsum, Anhydrite, Apatite, Phosphate.

Minerals for chemical industry
Sulphur, Halite, Potassium Salt, Limestone, Fluorite, Manganese minerals serving besides of combustibles for producing the basic materials for the large scale chemical industry (Sulphuric Acid, Nitric Acid, Hydrochloric Acid, Fluohydric Acid, Hydroxydes, Ammonia, etc.).

Mineral colors, pen minerals and textile minerals
Iron oxide and hydroxide, Manganese, Cinnabar, Gypsum, Rutile, Baryte, Mica, Graphite, Chalk, Scapstone, Greenstone, Brown Coal.

Lubrication and polished minerals
Graphite, Talc, Pyrophyllit.

Refractory minerals
Quartz, Quartz sands, Graphite, Chromite, Bauxite, Dolomite, Magnesite, Asbestos, Andalusite, Olivine, Cyanite, Dumortierite, Soapstone, Zircon.

Flux minerals
Quartz, Fluorite, Greenland Spar, Apatite, Limestone, Dolomite.

Minerals for electric and thermal insolation
Asbestos minerals, Talc, Serpentine, Sea Foam, Soapstone, Mica, Amber.

Grinding and polishinq minerals
Diamond, Corundum, Emery, Garnet, Quartz, Honestonequartzite, Grindstone-Rock, Red Iron Ore, Diatomaceous earth, Triplit.

Optical minerals
Halite or Mineral Salt, Fluorite, Double Spar, Quartz Cristalls.

Bleaching and absorbent minerals
Allophan, Bolus, Bentonite, Fullers Earth, Diatomaceous Earth.

Minerals for ceramics, cement and glass industry
Kaolin, Clay, Quartz, Feldspar, Talc, Soapstone, Boron Minerals, Rare Earth
Minerals, Chalk, Marl, Gypsum, Sand, Gravel Stone, Volcanic Sinter, Chips of Rock.

Building material
Eruptive Rock, Tuffs, Sandstone and other, Building Stone Slates, Clay Slate, Chalk, Marble, Serpentine, Alabaster, Stones for Road Construction, Auxiliary Material for Road Construction, Building Sands and Additives to Artificial Stones.

Basic minerals for building materials and their application are listed below due to their importance for regional development.

Application:

Therefore suitable stones:

Split Gravel (Ballast

Quartzporphyry, Basalt, Diabase

for roads and rail

Gabbro, Granite, Syenite, Gneiss,

tracks):

Phonolite, Quartzite, Graywacke

Pavement:

Granite, Syenite, Gabbro, Basalt, Diabase, Quartzporphyry, Graywacke

Kerb, stairs,

Granite, Syenite, Gabbro, Sand

sidewalks

stone, Graywacke, Limestone, Quartzite

Interior decoration:

Granite, Syenit, Marble, Serpentine

Monuments:

Granite, Syenit, Marble, Dolomite, Sandstone

Building

Granite, Syenit, Gabbro, Sand-

foundations:

stone, Limestone, Dolomite, Gneiss

Residence rooms:

Tuffite, Sandstone, Limestone

Roofing slate:

Slate, Platy Limestone

Basically, the technique of mining of non-metallic raw materials does not differ from that of the mining techniques described earlier. Solid rock are obtained by drilling and blasting. Only special decorative stones, e.g. marble are produced by sawing using diamond saws. The bigger the blocks to be obtained, the more protective should be the blasting during mining. This can be done by selecting the correct drilling scheme and particularly through the choice of the appropriate explosive. Through the expansion or dilution of granulated and gelatinous explosives with non explosive components or through the selection of explosive medium which are less powerful, the miner can obtain a huge heap of broken material. Thus the mining of shale for roof tiles for example, uses black powder for the production of large slate blocks. The special techniques of producing blocks of stones and their processing however should not be the concern of the present work especially because these techniques are described accurately in the following recently published work.

STONE. An Introduction. Asher Shadmon. Intermediate Technology Publications. LONDON 1989 [ISBN 0946688 08 7 (UK); ISBN 0942850 15 7 (USA)]

Relative to the mining techniques for metallic raw materials and fuel minerals (coal, lignite, peat, asphalt, bituminous shale), the specific quantities of exploited raw materials are usually greater. Surface mining of construction materials, particularly, is a mass production due to the minimal value of the product already mentioned above. The problem lies mainly in the haulage and the transport to the market. Usually, cost intensive transport systems as truck/wheel loader, etc. are required by means of which operations located on the deposits of these raw materials already land in the range of medium-scale mining. On the other hand, mining activities aiming at highly-valued products, e.g. graphite, diatomite, or other industrial minerals, or mining work which has a big share of manual work or activity which can not be mechanized easily, can definitely be undertaken by the usual small-scale operations using partially mechanized or improvised method.

CLOSE THIS BOOKTools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)
Technical Chapter 10: Surface Mining Equipment
VIEW THE DOCUMENT(introduction...)
VIEW THE DOCUMENT10.1 Aerial cable-way by gravity
VIEW THE DOCUMENT10.2 Cable tool drill
VIEW THE DOCUMENT10.3 Suction dredge
VIEW THE DOCUMENT10.4 Hydram, hydraulic ram pump, rife ram
VIEW THE DOCUMENT10.5 Noria
VIEW THE DOCUMENT10.6 Tyre pump
VIEW THE DOCUMENT10.7 Archimedian screw
VIEW THE DOCUMENT10.8 Boat mill
VIEW THE DOCUMENT10.9 Hydraulic mining gravel pump mining

Tools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)

Technical Chapter 10: Surface Mining Equipment

SPECIFIC SURFACE MINING TECHNIQUES

10.1 Aerial cable-way by gravity

Pit Banks for Deep Mines and Open-Pit Mines
Surface Mining Equipment

germ.:

Einfache Schwerkraftseilbahn

span.:

teleferico simple por gravedad, cablevia por contrapeso, andarivel por contrapeso

quechua:

hualaycho

TECHNICAL DATA:

Dimensions:

depends on vertical deviation as transport distance

Form of Driving Energy:

technique without external drive

Operating Materials:


Which:

lubricants

Quantity:

small quantity

ECONOMICAL DATA:

Investment Cost:

somewhat low, pulleys, cable, container

Operating Cost:

very low

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Experience:

low |————|————| high

Location Requirements:

extensive difference in topographic level is needed to overpower the friction only by weight of material

Mining Requirements:

the mine or production is above topographic level of beneficiation or further processing

Replaceable Equipment:

roads with transport of mined ore by truck to beneficiation or reloading place

Regional Distribution:

worldwide applied, not only for mining

Experience of Operators:

very good |————|————| bad

Environmental Impacts:

low |————|————| very high


eventually avoids roads and their consequences (erosion, etc.)

Suitability for Local Production:

very good |————|————| bad

Under what Conditions:

construction of foundations for pulley piles, probably installation of stretching device

Lifespan:

very long |————|————| very short

Bibliography, Source: Priester, Hentschel

OPERATING PRINCIPLE:

Aerial cable-way by gravity is comprised of a circulating cable guided by two pulleys, one at the upper loading level, and the other at the lower unloading level. The buckets which are hitched on the cable are driven by the difference in weights of loaded or non loaded material.

Thus, the loaded bucket is driven along the cable downward by gravity and pulls the empty one upwards for the next hauling procedure. To control speed, one pulley (preferably the upper one) has a brake, e.g. band brake or shoe brake. An automatic unloading device can contribute to make haulage easier. One pulley should allow cable tension or stretch to vary.

REMARKS:

As an alternative, the simple gravity aerial cable-way can be equipped with separate rail ropes and pull ropes or brake ropes. Two parallel stretched cables serve as rail ropes. They are usually made of mashed wire steel. Along the cables, rollers run which carry suspended buckets. The pull or brake rope that leads over a pulley and put on the brake, connects the two buckets. These are equipped with bottom gates which open automatically while passing a ripper.

Aerial cable-ways driven by gravity are used where ore is to be transported from a mine at the mountain side toe a processing plant located in the valley. Often, processing is bound at the river side to avail of huge quantities of water for Industrial purposes including for hydromechanic driven machines.

SUITABILITY FOR SMALL-SCALE MINING:

Following the chutes, gravity driven aerial cable ways are the simplest and cheapest systems for transporting in vertical distances.

10.2 Cable tool drill

Open-Pit Mining, Well Drilling probably Deep Mining
Surface Mining Equipment

germ.:

Seilbohren

span.:

perforacion a cable

TECHNICAL DATA:

Dimensions:

pennsylvanian drilling

drilling in China


lift 500 - 1000 mm

striking height of bit


frequency approx. 30 min-1

up to about 12 cm

Driving Capacity:

12 - 15 strikes per minute

Mode of operation:

continuous

Throughput/Capacity:

2 - 5 years for 1000 m deep drillings in China

Technical Efficiency:

at 250 mm (above) - 125 mm (below) 0 0.5 - 1.2 m/d

ECONOMICAL DATA:

Operating Cost:

very low drilling cost, partly high rope wear

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Experience:

low |————————| high

Deposit Requirements:

brine and natural gas were already found (before Christ) while drilling with a cable tool drill, where sandstone rocks, soft sandstones, limestones, claystones, generally non sturdy, cohesive loose rocks were drilled out but are not supposed to break back andshould not show much Joining or big cavities, such as karst.

Replaceable Equipment:

bench drilling machines, probably in quarries

Environmental Impacts:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under what Conditions:

cable tool drilling, for example with wooden drilling rigs and wooden or metallic drilling beam can be produced locally

Lifespan:

very long |————|————| very short


a problem is the short lifespan of rope

Bibliography, Source: Feldhaus, Arnold, Treptow, Schmiedchen

OPERATING PRINCIPLE:

In China, cable tool drilling was used with a four-leg rig made of bamboo bundles, above which a drilling tool bit hanging on a rope was being moved. The movement was caused either by a seesaw, e.g. a one side tipping wooden beam on which one or two persons bounced Up and down' or directly by pulling the rope. This then lifted the drill bit a little above the drill bottom and fell down consequently due to its own weight. By twisting the rope, the drilling bit could be moved or turned. Once the drill bottom was filled with drill cuttings, these loose materials were taken out or excavated into the surface by a simple bailer pulled by the rope. In the mounting and dismantling of the bit and the bailer, a hoist is being used. Bamboo rods served as casings which are partly sealed off with bitumen, resin and linen rags. Water bearing strata could be filled up with mud or clay and resin and could be penetrated again. The Pennsylvanian cable tool drilling method follows the principle of this chinese cable free falling drilling.

AREAS OF APPLICATION:

for drilling of vertical deep blasting holes in open-pit mining
for sampilag
for putting down ventilation holes with 100 - 150 mm diameter

REMARKS:

Cable tool drilling is known in China since more then 2000 years in boring for salt brine sources.

Disadvantages of cable tool drilling are:


- difficult assessment of rope lift due to rope twisting
- aperiodic rotation due to twisting of rope
- no possibility to apply water circulation or flushing
- difficulties in fishing out lost bit if rope breaks, usually a system of rods has to be available

Advantages of cable tool drilling are:


- low weight of needed drilling equipment
- fast installation of drill device
- very straight, exact vertical holes

Rope elasticity is being used in drilling, which means the rope is still stretched as it reaches the drill bottom. Otherwise it will be compressed which leads to breaking of the rope near the bit joint. The Pennsylvanian cable drilling method avoids this rope compression by using drilling jars in the drilling tool.

SUITABILITY FOR SMALL=SCALE MINING:

Cable tool drilling is a suitable technique of putting down deep vertical drill holes without the use of external energy. However, drilling efficiency is comparably low.


Fig.: The chinese method of putting down a deep well. Source: Feldhaus.


Fig.: Deep drilling installation in China. Source: Arnold.


Fig.: Drilling instalation in China with percussion device in ca. 600 before Chr. Source: Arnold.


Fig.: Piping or pipe installation in a Chinese deep drilling in ca. 600 before Chr. Source: Arnold.


Fig.: Schematic diagram of the Pennsylvanian cable drilling method. Source: Schmiedchen.

10.3 Suction dredge

Aluvial Mining in Open-Pit on River
Surface Mining Level Equipment

germ.:

Saugbaggerflo�e

span.:

dragalina de succion, draga aspirante, draga de succion

Producer:

Keene, HG (Colombia), Humphreys Mineral Ind., Mining Equipment Inc., Dopke, COMESA, IAA

TECHNICAL DATA:


Dimensions:

approx. 2 × 3 m area

Weight:

from 20 - 350 kg weight of machines (engine, pump, chutes)

Extent of Mechanization:

fully mechanized

Form of Driving Energy:

approx. up to 10 PS internal combustion engine

Technical Efficiency:

Other Opportunities: probably drive type "Schiffsmuhle" (see 10.8)

Mode of Operation:

semi-continuous/continuous

Throughput/Capacity:

from 7.5 m³/d to approx. 220 m³/d

Operating Materials:


Which:

gasoline

Quantity:

0.3 - 1.0 I/m3 sediment

ECONOMICAL DATA:


Investment Cost:

approx. 7500 to 20.000 DM

Operating Cost:

fuel cost

Consequential Cost through Coupling Effects:

eventually outboard motor

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————————| high

two man crew, one diver


Maintenance Experience:

low |————|————| high

Location Requirements:

river with depth of < 10 m

Ore Requirements:

relatively high amount of large sized material

Deposit Requirements:

alluvial, not cemented, loose sandy sediment

Adjoining Rock Requirements:

low clay content

Mining Requirements:

significant locations for mining are places where natural strips or barriers at the river bed traps for gold particles have been formed

Regional Distribution:

Bolivia, Brazil, Ecuador, Colombia, Venezuela, etc.

Experience of Operators:

very good |————|————| bad

Environmental Impacts:

low |————|————| very high


exhaust, fumes, used oil, river contamination by muddy waste which flow back into the river

Suitability for Local Production:

very good |————|————| bad


if components are imported such as motor and pump

Lifespan:

very long |————|————| very short

Bibliography, Source: Dahlberg

OPERATING PRINCIPLE:

The whole machinery unit (e.g. suction pump, engine, beneficiation) is installed on a floating boat anchored at river banks or controlled by an outboard motor. The motor drives a centrifugal pump. Water is injected by a pressure hose near the suction nozzle into the suction hose and carries water and sediments through this suction hose. This mud flow reaches the float and on a mostly simple gravimetric separation with screening off of large sized fractions and various types of through washers. The remaining pre-concentrate will then be sorted out later by batea, and finally, will either be sorted by hand or amalgamated.

AREAS OF APPLICATION:

Suction dredges are applied or used for mining of alluvial gold in riverbeds. Between 0.75 and 22.5 m³/h sediment is being pumped from a depth of 2 - 10 m with a suction nozzle diameter of between 15" and 8", and is then processed.

REMARKS:

Due to the mostly simple processing with through washers, only large sized gold particles are won. Thus, fine gold is lost. It is to be investigated if fine gold extractions can be recovered by spiral separator or centrifuge. It would be advantageous if the material would have been completely suspended already.

The smallest suction dredges are transportable and are weighing only about 25 kg including the float. In this case, floats are made of truck tyres. Bigger floats have an uplift mechanism, for instance, by the use of barrels.

Bigger floats are equipped with compressed air supply for the divers who will then guide the suction nozzle directly along the river bed or ground.

SUITABILITY FOR SMALL-SCALE MINING:

Not considering the somewhat high amount of investment and operation cost, suction dredges are quite suitable for small-scale recent fluviatile alluvial gold mining with relatively large size particles. Thus, deposits can be mined which otherwise cannot be extracted with manual rustic mining methods.


Fig.: Schematic diagram of a suction dredge. Source: Dahlberg.

10.4 Hydram, hydraulic ram pump, rife ram

Pit Banks for Deep/Open-Pit Mining General
Surface Mining Equipment

germ.:

Wasserschlagpumpe, hydraulischer Widder, Sto�heber, Druckstopumpe, Wassersto�er

span.:

bomba a golpe de ariete, ariete hidraulico, bomba de impulso a presion, impulsor de ague

Producer:

WAMA, Campo Nuevo, Pfister & Langhans, Gebr. Abt, Schlumpf AG, Ch, J. Blake, Las Gaviotas, Rife Hydraulic Engine Man., Cyphelly & Cie, Inteco

TECHNICAL DATA:

Dimensions:

from 3 - 12 1/min (3/4") drive water, 320 mm height to 280 - 600 1/min (6") 1400 mm

Weight:

18 - 427 kg

Extent of Mechanization:

partly mechanized

Form of Driving Energy:

energy of drive water

Mode of Operation:

semi-continuous

Throughput/Capacity:

quantity of pump water depends on conveying distance: head of drive water 40 % (2 : 1 ) - 1.25 % (20 : 1 ) up to 250 m conveying distance

Technical Efficiency:

30 - 60 %

Operating Materials:


Which:

drive water

Quantity:

depends on conveyance discharge and head of water (minimum 0.5 m)

ECONOMICAL DATA:

Investment Cost:

brand new, fob Grafing 1400 to 2.000 DM; Campo Nuevo approx. 250 to 550 US$

Operating Cost:

very low, low maintenance, very low wearing

Consequential Cost through Coupling Effects:

delivery pipe, hydraulic engineering works

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Experience:

low |————|————| high

Personnel Requirements:

very few, only a periodic control of air content in the air chamber is important

Location Requirements:

water and relief necessary

Mining Requirements:

typical application is in alluvial mining in flood-plain terraces which lie above the drainage level

Replaceable Equipment:

all kinds of pneumatic, mechanical and electrical pumps

Regional Distribution:

earlier worldwide, replaced by electrical systems

Experience of Operators:

very good |————|————| bad

Environmental Impacts:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under what Conditions:

metal manufacture, construction material: standardized pipes

Lifespan:

very long |————|————| very short

Bibliography, Source: Fracokel, Meyer, Monninghoff, companies inforation

OPERATING PRINCIPLE:

Drive water flows through the lower part of widder and is released through the open waste valve with accelerating speed. If the speed exceeds a certain limit, the waste valve is automatically closed by the streaming water. A pressure peak occurs caused by this inertia which opens the delivery valve to the air chamber. The backwater is being pressed into the air chamber until the accumulated pressure falls below the internal pressure of the air chamber. Here, the delivery valve then closes while the waste valve opens again.

The procedure as described above reiterates itself periodically. Water that is inside the air chamber is then conveyed through internal pressure to the end user by a delivery pipe.

AREAS OF APPLICATION:

Hydraulic ram pump can always be applied where huge quantities of water with low falling gradient are available and where simultaneously, water is needed above water level for mining, beneficiation, water supply or for other purposes.

REMARKS:

This pump was invented by the Montgolfier Brothers who were awarded with a related patent in France In 1797, and called It hydraulic ram pump or hydram.

Hydraulic ram pumps are suitable for local production if qualified metal manufacture shops are available. As a result, the pumps components can be manufactured with simple pipes, etc. and allows savings in the cost of material and complicated welding works.

A very important source of failure in the operation of the hydram lies with the fact that air cushion in the air chamber can dissolve in (drive) water. If this happens, huge pressure peaks occur in all parts of the hydram thus stopping delivery. As a counteraction, a hole can be drilled into the drive water pipe near the hydram entrance to let fresh air enter into the air chamber, using the principle of the jet pump.

Of further importance is the length of drive water pipe which influences pressure distribution by the closing and opening of valves. Length of the pipe should be preferably between 5 - 12 times of the water gradient or inclination.

Drive water should be free of suspended materials and sediments as much as possible.

It is necessary that the water drive pipe is made of metal since flexible materials, such as PE or PVC usually yield to pressure peaks which then leads to falling pressure and decreased efficiency in the conveyance. The delivery pipe can be made of plastic and can be connected with adhesives, welding seams, or clamping devices.

SUITABILITY FOR SMALL-SCALE MINING:

Hydrams are very suitable for mining purposes if infrastructure for energy supply is lacking, but sufficient water and water level differences are available. The pumps are very reasonably priced, they are stable and are suitable for local production.


Fig.: Function of a hydraulic ram pump. Source: Fraenkel.


Fig.: Different types of hydrams. Source: Fraenkel. Above left: Traditional European type (Blakes); Above right: South-East-Asian type; Below: Hydram made of pipes.

Table: Falling and efficiency gradients for a hydraulic ramp pump. Source: Schlumpf Company Information.

Pumped quality as a percent of the water volume pumped throught the hydraulic ram:


Table

10.5 Noria

Pit Banks for Deep/Open-Pit Mining General, Open-Pit Mining General
Surface Mining Equipment Hauling

germ.:

Schopfrad, Hesselrad

span.:

noria, rueda elevadora

Producer:

M. Impler

TECHNICAL DATA:

Dimensions:

diameter 2.5 m and bigger, 0.7 m wide

Weight:

700 - 800 kg

Form of Driving Energy:

hydromechanic

Mode of Operation:

continuous

Throughput/Capacity:

1 I/sec, head of water approx. 1.5 m

Technical Efficiency:

up to 60 %

Operating Materials:


Which:

water

Quantity:

very low vertical interval, but high flowing speeds

ECONOMICAL DATA:

Investment Cost:

14.000 DM, substantially lower if locally produced

Operating Cost:

very low

Consequential Cost through Coupling Effects:

few water engineering works, flood protection

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Experience:

low |————|————| high

Personnel Requirements:

low

Location Requirements:

water with streaming speed needed

Mining Requirements:

water demand should be relatively near above the river level since water head ranges only between ca 50 to 60 % of wheel diameter such as for beneficiation of raw ore mined from gravel terraces at river banks.

Replaceable Equipment:

smaller pumps, hydraulic ram pump

Regional Distribution:

historically, widely known; until today, still used in the agricultural industry in Asia and Africa

Experience of Operators:

very good |————|————| bad

Environmental Impacts:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under what Conditions:

wood manufacture

Lifespan:

very long |————|————| very short

Bibliography, Source: M. Impler, Eckholdt, Meyer, Cancrinus, Fraenkel

OPERATING PRINCIPLE:

Noria is an undershot (Zuppinger-) water wheel with lateral attached buckets. It draws water from the river level and empties out automatically at the upper dead point into a draining chute. Needed is a relatively high streaming or flowing speed but a low falling gradient.

AREAS OF APPLICATION:

Water wheels are used for water haulage from large rivers to a level which is a little higher, such as for operating through washers, wet screening, etc. near a river.

REMARKS:

Wooden water wheels can also be designed so that components can be disassembled and allow its transporting even in remote areas.

Local manufacture with local materials can be implemented easily per instructions and leads to substantial cost savings.

A problem for the operation of water wheels are fluctuating levels of the water surface. If the water level rises to the height of axis, the water wheel could be damaged. Here, flood protection is indispensable. Besides, efficiency declines by a rising water surface level.

Water wheels were built with a diameter of 10 m (Syria) but were less efficient and needed more construction efforts than the other systems.

SUITABILITY FOR SMALL-SCALE MINING:

Only suitable in rivers with less daily or yearly fluctuating water levels and short conveying distance or low head of water.


Fig.: A water wheel in North Bavaria. Source: Eckhold.


Fig.: Lifting wheel. Source: Treptow.


Fig.: Early types of water conveying machines. Source: Cancrinus.

10.6 Tyre pump

Pit Banks for Deep/Open-Pit Mining General
Surface Mining Equipment

germ.:

Reifenpumpe

span.:

bomba con llanta como membrane

TECHNICAL DATA:

Dimensions:

approx. 1 m × 1 m × 0.5 m + rods

Weight:

approx. 30 kg

Extent of Mechanization:

not mechanized/partly mechanized

Form of Driving Energy:

mechanical, for example, energy from wind and water

Other Opportunities:

manual drive, pedal drive

Mode of Operation:

intermittent

Operating Materials:

none

ECONOMICAL DATA:

Investment Cost:

approx. 250 DM if locally produced

Operating Cost:

only labor cost

Consequential Cost through Coupling Effects:

driving system, leverage system

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high


depends on form of drive

Maintenance Experience:

low |————|————| high

Location Requirements:

low suction and pressure heights

Replaceable Equipment:

other types of diaphragm or piston pump

Experience of Operators:

very good |————|————| bad

Environmental Impacts:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under what Conditions:

simple metal manufacture

Lifespan:

very long |————|————| very short

Bibliography, Source: Landtechnik Weihenstephan, Fraenkel

OPERATING PRINCIPLE:

A tyre pump is a simple diaphragm pump. The pump room inside the tyres enlarges and becomes smaller alternatively, as the space between the casings of the tyre increases and decreases pulsatingly. The check valves in the feed and discharge line control the inflow and outflow of water.

AREAS OF APPLICATION:

To convey huge quantities of water with small head of water.

REMARKS:

Tyre pump is one of the most simple forms of pumps driven by a pulsating connecting rod and works simultaneously with low pulse code (even < 100 min-1).

High forces appear to be a problem. A car tyre with 400 mm diameter has a working area of 0.126 m². Such area needs 1.230 N/m pressure height, which means for a 3 m diameter, this is approximately 3,7 N or 376 kg force of connecting rod. All in all, tremendous forces occur at the rods.

SUITABILITY FOR SMALL-SCALE MINING:

Tyre pump is the simplest design to pump water with slow R.P.M. of drive and high torque. It conveys large quantities of water with small head of water which is often used in alluvial gold mining.


Fig.: Schematic diagram of a tyre pump with eccentric tumbling rod. Source: Landtechnik Weihenstephan.

10.7 Archimedian screw

Alluvial Mining Open-Pit and Quarry Industry
Underground Mining Open-Pit Mining/Drainage

germ.:

Archimedische Spirale, Wasserschnecke, Tonnenmuhle, Wasserschraube

span.:

Espiral de arquimides, espiral pare desague

TECHNICAL DATA:

R.P.M.:

40 min-1 (min.) - 70 - 80 min-1 (max.); 20 min-1 (min.) - 40 - 50 min-1 (max.)

Angle of Inclination:

open: max. 30°, closed: max. 45°

Dimensions:

covered conveying screw 300 - 700 mm up to max. 12 m length, open screws: 500 - 900 mm

Extent of Mechanization:

not mechanized

Driving Capacity:

depends on head of water: 0.25 - 0.3 kW/m³/min × m h; open screws 0.2 - 0.3 kW/m³/min × m h

Form of Driving Energy:

manual or pedal driven (- 0.6 m h)

Other Opportunities:

in combination with wind wheel, animal power gear

Throughput/Capacity:

- 10 m³/min up to max. 6 m h

Technical Efficiency:

approx. 30 % (wooden traditional closed conveying screws) 60 - 70 % (steel screws in open concrete coverage)

Operating Materials:

none

ECONOMICAL DATA:

Operating Cost:

energy cost

Consequential Cost through Coupling Effects:

eventually a driving system

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|—| high


depends on form of drive

Maintenance Experience:

low |————|————| high

Replaceable Equipment:

pumps with comparably high conveying rate for low head of water, e.g.,water wheel

Regional Distribution:

peat mining in Germany

Experience of Operators:

very good |————|————| bad

Environmental Impacts:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under what Conditions:

wood manufacture

Lifespan:

very long |————|————| very short

Bibliography, Source: Fraenkel, Hausding, Rittinger

OPERATING PRINCIPLE:

The archimedian screw is comprised of a strong shaft which is twined by a spiral shaped surface thread. To be distinguished are open and closed conveying screws. The open screws rotate with tow tolerance within a fixed half cylindrical channel. The closed screws are completely covered by a cylinder which rotates with the screw. Water is being enclosed by plunging in of screw threads at the lower end of the archimedian screw. The slight inclined screw displaces water along the cylindrical cover upwards until it flows out at the upper end of the screw.

AREAS OF APPLICATION:

Draining of peat digging, water utilization with very low vertical interval, e.g. in open-pit mining within ground water.

SPECIAL AREAS OF APPLICATION:

Water conveyance with low head of water, recirculation of water in arid regions

REMARKS:

The archimedian screw is one of the oldest water lifting systems. It has been in use since about 200 B.C. in the silver mines In Spain.

Water screws are very stable against suspended solids and other impurisation of water to be conveyed.

Failure in operation of water screws are very seldom and can be easily repaired by an experienced technician locally.

Water screw is most efficient if the filling end is dipped by 50 - 65 % of its diameter into the water and decreases rapidly as the filling end is under water. For fluctuating water levels, a lifting device is recommended.

Only drives of low specific rpm are adequate in order to mechanize archimedian screws otherwise high losses in efficiency caused by shifting have to be put up with. "animal power gear" or wind wheels would be appropriate as drives.

The pitch of a water screw is mostly identical or a little smaller as the external diameter. The screw is often designed as double or tripple screw.

SUITABILITY FOR SMALL-SCALE MINING:

As manual pumps, archimedian screws are to be used for large conveyance quantities and low lifting height. Due to their simple design and high efficiency, archimedian screws are suitable for use as draining equipment in open-pit mines and for lifting industrial water.


Fig.: A cross-section of an open archimedian screw. Source: Fraenkel.


Fig.: A waterscrew. Source: Hausding.


Fig.: A manual driven archimedian screw. Source: Fraenkel.


Fig.: A archimedian screw, animal-driven by car axis. Source: Fraenkel.

10.8 Boat mill

Open-Pit Mining at River Level
Surface Mining Machinery

germ.:

Schiffsmuble

span.:

barco con ruedas hidraulicas pare generar energia, barco o ponton con ruedas de ague pare generar enegia

TECHNICAL DATA:

Dimensions:

approx. 15 × 5 m

Extent of Mechanization:

partly mechanized

Form of Driving Energy:

hydromechanical, hydraulic energy

Mode of Operation:

continuous

Throughput/Capacity:

up to approx. 10 kW

Technical Efficiency:

equal to a"Zuppinger" wheel: 65 - 70 % (see 19.6)

Operating Materials:


Which:

water

Quantity:

bigger river with strong rapids

ECONOMICAL DATA:

Investment Cost:

30.000 to 50.000 DM including water wheels

Operating Cost:

extremely low

Consequential Cost through Coupling Effects:

anchorage

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Experience:

low |————|————| high

Location Requirements:

river with strong rapids

Regional Distribution:

today almost unknown

Experience of Operators:

very good |————|————| bad

Environmental Impacts:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad


but requires too much time and very expensive

Under what Conditions:

experienced wood manufacture, metal manufacture

Lifespan:

very long |————|————| very short

Bibliography, Source: Kur, Mager, Meyer, Muller 1939, v. Konig 1985

OPERATING PRINCIPLE:

Boat mills are stationarily anchored pontoons, floats or boats in river streams equipped with one, two or several undershot water wheels. They are similar to paddle steamers. However, the water wheels are not used as the driving unit, but used exclusively for the production of energy.

The mechanical energy can either be used directly for pumping, beneficiation or for other purposes, or can be converted into electrical energy by a generator (see below).

REMARKS:

A big advantage of the boat mill is its simple control and there's no need for water engineering works. The water wheels are always equally submerged deep into the streaming water, so that during both high and low tides equal forces are applied at the wheels at the same rate of rapid or streaming speed.

Thus, energy can be easily produced from large rivers with heavily fluctuating water levels, such as rivers in tropical climatic zones.

The conversion of energy into electrical power is difficult due to very low rpm of the driving axis of the boat mill. Beforehand, generators should be converted into slow moving generators by rewinding with long and fine wires. Only in this way can the necessary voltage be attained.

Likewise, a gear has to be placed between the driving axis and the generator.

Boat mills are very old forms in utilizing water energy or hydro power. Their invention could be traced back to 536 A D. and were found to have been used already in mining.

Boat mills were designed in two different models:

- with one water wheel between the main boat and the outrigger boat; and

- with two laterally attached, directly coupled or unattached undershot water wheels and only one boat or ship.

The second model is the one that is more suitable for production of energy and for mining purposes.

SUITABILITY FOR SMALL-SCALE MINING:

A good investment if utilized and financed collectively, such as by cooperatives under appropriate environmental conditions (isolated locations in large rivers). Main advantages are the multi-purpose utilization and there is no need for supply of operating materials and equipment.


Fig.: A boat mill with an outrigger boat and a main boat; left, side view; right, top view. Source: Kur.

10.9 Hydraulic mining gravel pump mining

Open-Pit Mining of Heavy Mineral and Precious
Surface Mining Extraction Metal Alluvial Deposits

germ.:

Kiespumpenabbau

span.:

explotacion con bomba de grave

Manufacturer:

Brauer (Mammutpumpe), Warman Dopke, Met. Lacha, Volcan Buena Fortuna

TECHNICAL DATA:

Dimensions:

10 - 50 m head of water, 6 - 12" delivery pipe, 50 - 600 m length (conveying distance)

Power required:

100 - 600 kW drive for gravel pump, less for water pumps for monitors

Form of Driving Energy:

diesel or electric motors

Alternative Forms:

none

Throughput/Capacity:

20 - 100 m³/h

Technical Efficiency:

about 0.45 for gravel pump, manufacturer's figures for new pump approx. 60 % by optimal operation

Operating Materials:


Type:

water

Quantity:

about 20 times the volume of conveyed material with additional auxiliary equipment about 10 times the material volume, up to approx. 65 % (by weight) solids (limestone) and 30 - 40 % (by weight) sand can be pumped

ECONOMIC DATA:

Investment Costs:

comparably low especially if locally produced. Gravel pump locally manufactured (Malaysia), 8 × 10", approx. 2000 DM without motor; for pumps (5 m³/h output) manufactured in industrialized countries approx. 5000 DM.

Operating Costs:

approx. 50 % for energy, 18 % for spare parts and material, 25 % for personnel

Related Costs:

high cost of energy-supply installation

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

2 persons minimum


Maintenance Expenditures:

low |————|————| high

Location Requirements:

large quantities of water must be available

Deposit Requirements:

Gravel pump mining of alluvial deposits of heavy minerals (tin) and precious metal (gold) which exhibit non-consolidated or only slightly consolidated host rock and limited coarseness of granulation suitable for pumping. The strata underlying the deposit should be water-impermeable and preferably slightly inclined. There are no requirements regarding the thickness of the deposit. Steeply inclined overlying strata is unfavorable,and when present must be of minimal thickness.

Host Rock Requirements:

none; however, the abrasive strength of the host rock has a major effect on the lifespan of the pump in hydraulic mining

Replaces other Equipment:

dry mining with wheel loader, trucks, bulldozer, excavators

Regional Distribution:

in tin mining in Thailand and Malaysia, in gold mining worldwide

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |——————| very high


The major cause of environmental pollution is the occaisional high sediment (sludge) load in the high quantities of waste produced; an additional source is the pump's drive-unit.

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

very good metal foundries are necessary for repeated casting of new sand-pump impellers. Gravel pumps are locally produced in Malaysia and Thailand.

Lifespan:

very long |————|————| very short

The working lifespan of gravel pump impellers ranges between 80 and 1200 hours of operation; for locally-manufactured Impellers this figure can lie substantially lower. It has been reported that in Thailand impellers can already wear out after only two days in operation, and are then melted down and recast in a local foundry. The lifespan of the pump housing is about three times longer than that of the impellers.

Bibliography, Source: Hageluken, Gartner

OPERATING PRINCIPLE:

In sand-pump mining of heavy-mineral and precious-metal alluvial deposits, mining is performed hydraulically, and the mined slurry is transported hydraulically to the beneficiation facility where it undergoes wet mechanical and gravity separation. Hydraulic mining can be differentiated according to two different methods.

Thin sediment deposits of medium-sized granulation with a thickness of less than 3 meters are mined from above by water jets. All other thicker deposits are mined from underneath with a so-called monitor. A monitor is a water-powered water Jet stream which is fed by a fresh-water pump (pressure up to 10 bars, discharge velocity 15 · 50 m/s). The jet stream is directed toward the part of the deposit to be mined, whereby the rock bonds are loosened from the impact, releasing the valuable minerals which then Join the slurry being drawn into the gravel pump. The hydraulic gravel pump is placed at the deepest point of excavation and hydraullically conveys the slurry, with a maximum solids content of 5 - 10 % (by volume), through the delivery pipe to the beneficiation facility. Gravel pumps are usually manufactured with wear-resistant housings and impellers. The beneficiation of the slurry occurs in a parallel-operated system of sluices, possibly with subsequent processing in Jig washers, spiral separators (see 14.18), conical separators or similar apparatuses.

SPECIAL AREAS OF APPLICATION:

Reverse-polarity gravel pumps are also used as turbines when turbid slurries or waters with high solids contents make up the propelling fluid flow.

REMARKS:

Gravel pump impellers are subject to extremely high wear due to the abrasive effects of coarse-grained suspended solids, the extent of which depends on the soil conditions. In general, impeller wear increases with increasing grain size. In order to limit this abrasive wear, it is advisable to screen the slurry prior to its being drawn into the pump, choosing a cut-off fraction Just above the largest grain-size with valuable-mineral content.

To avoid Individual particles from settling out during slurry transport, the specified minimum flow velocity must be maintained.

For positioning the gravel pump, the most successful solution has been to suspend the complete apparatus (directly-coupled pump and drive-unit) from a tripod. This avoids the necessity for an expensive foundation construction. Additionally, suspending the system from a tripod makes the frequent repositioning of the gravel pump easier as mining work progresses.

The smallest incline of the underlying strata between the monitor and the gravel pump should be at least 1:40 In order to avoid losses in valuable minerals through sedimentation. An auxiliary monitor, or booster, can possibly be used to maintain the slurry as a stable suspension and to transport materials which have already settled out.

To increase the density of slurry to be conveyed, auxiliary equipment such as bulldozers, hydraulic shovels, bucket wheel loaders, etc. are employed.

The drive-unit of the gravel pump should be about 30 - 50 % oversized to account, in advance, for excessive loading or increased output demands resulting from fluctuations in slurry density, extension of the delivery pipe, etc.

SUITABILITY FOR SMALL-SCALE MINING:

Gravel pump mining is characterized by its low investment cost but high cost of energy. It can be the most profitable method of mining heavy mineral sands if deposit conditions are suitable.


Fig.: Forms of hydraulic mining with with gravel pumps. Source: Gartner.longitudinal section I·I

1. gravel pump. 2. hydromonitor 3. water jet-stream flow direction 4. discharge direction of the slurry (sediment/water mixture)


Fig.: Sand-pump hydraulic mining operation with sluice separation. Source: Gast.


Fig.: Flow chart of alternative mining methods in Southeast Asian open-pit tin mines (not considering floating dredge operation or solid-rock quarries). Source: Hageluken.

Table: Summary of comparison of mining and transporting methods applied in Southeast Asian tin mining.

Source:Hageluken


A

B

C

D


Hidraulic transport




with monitor mining

with monitor mining and auxiliary equipment

Truck transport with dry mining

Combined truck and hydraulic transport

Water requirements

depending on type of earth generally very high since ore is loosened only by water impact

lower than A, since loosening of ore also by auxiliary equipment

low, water only needed for classifying and beneficiation

medium, for interim dump only small loosening forces required

Utilization of energy

bad, mainly transport of water

a little better than A, since higher contents of solids possible

depending mainly on loading capacity/total weight relation of trucks as well as on work organization and conditions of roads

Abrasive wear

depending on type of earth, generally high wear on pump and pipes

EME: depending on on type of soil, load and EME conditions of roads





HT: as A

Coordination of equipment capacity

difficult; necessary power varies after re-location of pump and changed pipe length; mostly oversizing of motors

EBG: simple, since appropriate equipment can be chosen




greater transport

HT: simple, since




distances require

length of pipes




high investments

remain constant

Downtime of the entire operation

by failure of water supply, by moving of the pump position and by failure of a part of the system (pump, pipes, beneficiation or dumping of tailings); direct connection from extraction to waste dump

Total downtime only there is no intermediate deposit and simultaneous failure of all extraction equipment or of all trucks resp. by failure of beneficiation of dumping or tailings if intermediate deposit is impossible

-

Intermediate buffer deposit

not possible

only limited (with auxiliary equipment at the face)

possible

already existing because of method used

Variations in content of solids

high because monitor operations in untouched material

depending on layout of dump, high when dumped directly on grate

lower with controlled monitor operation

Variations in content of valuable material

high because heterogene deposits and sedimentation of heavy minerals in delivery channel and pump sump

reduction of influence by deposit possible by means of blending stockpile





HT: as A

Desintegration of the ore

through monitor (auxiliary equipment), pump and pipe transport; long reaction time of water

by excavator and addition of water at dump point/screen short reaction time

as A, but shorter reaction time of water

Dependence on climatic conditions

in some areas the mining operation must possibly be ceased because of water shortage during dry season

generally, truck open ation is impossible during the rainy season

Operation in difficult terrain:


- swamp

possible

limited

not possible

- lime slone pockets

possible

limited

limited

Widespread very small deposits

only possible for very small mines since for larger operations continuous moving of haulage system and beneficiation would be required

possible, high flexibility through truck transport to centrally positioned beneficiation

Abbreviations: EME = earth moving equipment / HT = hydraulic transportation system

CLOSE THIS BOOKTools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)
Technical Chapter 11: Other special techniques
VIEW THE DOCUMENT11.1 Welding additives
VIEW THE DOCUMENT11.2 Rubber tanks, flexible tanks
VIEW THE DOCUMENT11.3 BY-Pass oil filters, by-pass micro-filters
VIEW THE DOCUMENT11.4 Eccentric motor, vibrator, shaker

Tools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)

Technical Chapter 11: Other special techniques

11.1 Welding additives

Mine Workshop
Surface Mining Special Techniques

engl.:

protection against wear, wear-resistant materials

germ.:

Schwei�zusatzwerkstoffe, Verschei�schutz, Panzerungswerkstoffe

span.:

materiales pare soldadura, proteccion contra desgaste, material de blindaje

Manufacturer:

Vautid

TECHNICAL DATA:

Dimensions:

for electric manual welding, cast or pressed round electrode rods, 2.5 - 8 mm, 350 - 450 mm in length

Power required:

90 - 320 A ave. current strength, whereby amperage increases with the diameter of the electrodes

Form of Driving Energy:

electric

ECONOMIC DATA:

Investment Costs:

electrode rods: approx. 20 - 60 DM/kg

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Personnel Requirements:

good welding skills required

Location Requirements:

power supply must be available

Regional Distribution:

worldwide in industrialized countries

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Lifespan of wear-resistant tools:

very long |————|————| very short


this technique is applied to extend lifespan

Bibliography, Source: Vautid-Company information

OPERATING PRINCIPLE:

Available forms of welding materials are standard electrodes, filling wires, continuous cast rods and injecting powder. Various demands upon materials, such as abrasion by hard minerals or cavitation, impact or compressive stresses, temperature extremes caused by high ambient heat or friction, or corrosion by aggressive media can be counteracted by means of coating with the electrode material. Depending upon the requirements, alloys of Fe, Cr, Mn, Ni, W, V, Mo, Nb with Si, B, and C are applied.

AREAS OF APPLICATION:

Electrodes, for example against abrasion, contain in addition to other alloy elements, high proportions of chromium and carbon which form extremely hard chromium carbide during welding. They are used to increase resistance to abrasion of machine parts subject to wear in mining, beneficiation and energy production.

For mining equipment:

shovel bucket teeth, rail parts, pump blades, sand pump impellers, drilling and cutting tools

For beneficiation equipment:

crusher jaws, crusher rollers, crusher cones, grinder linings, linings in Chilean (edge) mills, chutes, cyclone linings, pump blades, agitators (stirrers) in flotation cells

For motors and engines:

turbine blades

REMARKS:

The coating of machinery parts with wear-resistant welding materials is, of course, work intensive, but extremely effective and especially important in developing countries, where it can substantially improve the quality of locally-produced machinery components for use in the mining industry. Low labor costs in developing countries enable this work-intensive solution to remain economical. A further significant advantage of this hand coating method lies In the fact that even complicated structures such as pump blades, etc., can be treated.

Depending on the electrode material, the goal is to achieve Vickers hardness values HV 10 from 230 - 2000, corresponding to Rockwell HRC values from 19 to about 70.

Welding materials can be used to coat the following materials:

- non-alloyed steel and cast-steel (magnetic, soft: test with magnet and file)

- alloy steel and steel with up to over 0.5 % C (magnetic, hard) after preheating at approx. 300 - 500° C

- manganese steel (non magnetic, hard), welded cold in water bath

- cast iron (magnetic, soft) possibly when thoroughly preheated (approx. 500°C)

- hard cast iron (magnetic, hard) should not be coated due to danger of cracking.

The electric current should not be too strong and welding should not be too slow in order to prevent too much mixing between the welding material and the melted base material which results in a reduction in hardness.

The maximum thickness of the coating depends upon the welding materials and ranges from 5 to 20 mm; greater thickness is achieved through multiple layers of thinner coatings.

Larger surface areas are sometimes reinforced only with individually welded beads or buttons.

During the hardening process, cracks develop in the coating materials which lower the stress and, as a rule, do not extend to the basic material underneath.

A reworking of wear-resistant parts is usually only possible with SiC or corundum grinding wheels.

For large planar surfaces, pre-fabricated hardened compound plates, special threaded fittings, etc., are available on the market.

Armored and wear-resistant elements made of rubber can be recommended for various purposes, particularly when slow moving parts are exposed to abrasive materials (slurry) such as in spiral separation.

SUITABILITY FOR SMALL-SCALE MINING:

Wear-resistant materials are highly suitable and effective in greatly increasing the lifespan of locally-manufactured equipment and machine parts, and in reducing the frequency of maintenance and repairs.

11.2 Rubber tanks, flexible tanks

Surface Facilities General
Surface Mining Special Techniques

germ.:

Gummitanks, flexible Tanks

span.:

tanques de goma, cistern as flexopleglables, tanques flexibles

Manufacturer:

Arcotex, Continental

TECHNICAL DATA:

Dimensions:




from 700 1

over 10.000 1

up to 40.000 1

up to 100.000 1

2.00 × 1.25 m

4.80 × 3.20 m

8.5 × 5.30 m

10.1 × 10.5 × 1.3m

Weight:




12 kg

54 kg

130 kg

338 kg

Extent of Mechanization:

not mechanized



Form of Driving Energy:

not powered



ECONOMIC DATA:

Investment Costs:

5,000 I tank approx. 2000 US$ FOB Santiago de Chile

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Location Requirements:

due to their flexibility and collapsibility, empty tanks can also be transported through small doors in buildings or into the mine.

Replaces other Equipment:

brick tanks, tank-cars

Environmental Impact:

low |————|————| very high

Suitability for Local Production:

very |————|————| goodbad

Lifespan:

very long |————|————| very short

Bibliography, Source: Arcotex Company information, Continental Company information

OPERATING PRINCIPLE:

The flexible tanks have an interior lining which inhibits splashing of the fluid content, enabling transport by truck to meet supply requirements for mine water, gasoline, diesel, chemical fluids, etc. The collapsed empty tanks require very little space (less than 5% that of full tanks), allowing the trucks to be used for product and material transport on the return trip.

AREAS OF APPLICATION:

Transporting of fluids for mining, agriculture and industry.

SPECIAL AREAS OF APPLICATION:

Permanent stationary tanks.

REMARKS:

The tanks are filled without pressure, eliminating any need for filling pumps or similar equipment.

The tanks are made of a very strong nylon material which is coated on both sides with black synthetic rubber. The individual sections are joined by heat-cured (vulcanized) seams. To improve safety, additional nylon tarps are placed underneath the tank.

Flexible tanks are available on the market for the following fluids:

drinking water
gasoline, diesel and other common fuels
vegetable and mineral oils
hydraulic fluids and lubricants
waste water, salt water
alcohols
ethylene and various derivatives
leaches and acids up to medium concentration
formaldehyde, formamide, glucose, glycol, glycerin
carbon dioxide, corrosion-preventives, glue, soap buck, various inorganic salts and their leachates, etc.

The tanks are resistant to ageing and to reactions with the fluid content within a temperature range of -30° to + 70° C.

SUITABILITY FOR SMALL-SCALE MINING:

Flexible tanks are especially attractive as mobile tanks for the combined truck transport of fuels (to the mine) and of raw materials (from the mine). They are also suitable for short term application as stationary tanks.

11.3 BY-Pass oil filters, by-pass micro-filters

Open-Pit Mining General Surface and Under ground Vehicles
Surface Mining Special Techniques

germ.:

Bypass-Olfiiter, Nebenstrom-Feinstfilter

span.:

filtro de aceite-bypass, microfiltro secundario

Manufacturer:

Kleenoil

TECHNICAL DATA:

Dimensions:

0.15 m H, 0.15 - 0.25 m 0

Weight:

approx. 2.5 kg

Form of Driving Energy:

driven by oil pump pressure

Alternative forms:

for stationary systems, additional external manual pump

Throughput/Capacity:

approx. 100 I/h

ECONOMIC DATA:

Investment Costs:

approx. 640 DM without delivery and installation

Operating Costs:

approx. 40 DM per filter element

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Personnel Requirements:

periodic changing of filter

Replaces other Equipment:

recycling of lubricating oil can drastically reduce mining equipment oil consumption, and especially minimizes of used-oil disposal problems

Regional Distribution:

in industrialized countries

Operating Experience:

very |————|————| good bad

Environmental Impact:

low |————|————| very high


technique is environmentally advantageous

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

good metal workshop, filter candles can be made from suitable types of toilet-paper rolls

Lifespan:

very long |————|————| very short

Bibliography, Source: Kleenoil information

OPERATING PRINCIPLE:

A microfilter functions by pressing oil through a filter cartridge which removes:

- particles > 1 ym (common oil filters separate above 5 ym), and
- water (for example, condensed water from combustion) down to < 0.05 %.

This results in greatly reducing the abrasiveness of the oil, and substantially inhibits the development of acids from contact between the condensed water and combustion gases. The filter cartridges are made of tightly wound, long fibrous conifer-wood cellulose, held togother by a cotton sleeve.

AREAS OF APPLICATION:

Applicable either as by-pass filters in secondary oil circuits or as stationary microfilter systems.

In secondary oil circuits in engines, they can be installed, for example, on the pressure (delivery) side at the oil-pressure sensor using a tee-piece, or on the return side at the oil pan. The advantage of this installation is that the oil-change Interval no longer needs to be observed, with only an occasional change of filter cartridge being required.

Employed as stationary microfilters, the oil is pumped from the engine's oil pan during periods of non-operation (engine off) through a microfilter unit.

REMARKS:

Following longer periods of operation between oil changes, the oil normally contains up to 4-5 % impurities. With the use of filter cartridges, these impurities are already partially removed during engine operation, so that the time interval between oil changes (i.e. oil lifespan) can be increased ten to fifteen-fold.

90 % of machine wear is caused by acids which develop when acidic by-products combine with water in the oil.

The crucial problems of waste-oil disposal can be largely minimized through application of such filters, which reduce the volume of used oil to around 10 %.

Stationary filter types can also be used for cleaning of hydraulic oil.

Used filter cartridges can be burned, during which the production of smoke is minimal due to the high proportion of vegetable fibers contained in the filters.

SUITABILITY FOR SMALL-SCALE MINING:

Fine oil filters, either as stationary or by-pass filters, can help solve the disposal problems associated with used oil by substantially extending the lifespan of lubricants.


Fig.: Operating principle of a by-pass oil filter in secondary oil circuit. Source: Kleenoil Company information.

11.4 Eccentric motor, vibrator, shaker

Open-Pit Mining Mine Workshop
Surface Mining Special Techniques

germ.:

Unwuchtmotoren, Ruttler

span.:

motores con contrapeso, vibrador

Manufacturer:

Bosch, Italvibras, Netter, Schenck, AEG, Jost

TECHNICAL DATA:

Dimensions:

depends on type and capacity, from 5 × 5 × 5 cm to 8 × 8 × 65 cm

Weight:

approx. 100 g to more than 100 kg

Extent of Mechanization:

fully mechanized

Power required:

electric alternating-current vibrator: 0.03 - 11 kW; electric direct-current vibrator 0.2 kW (12V)

Form of Driving Energy:

electric with direct and alternating current

Alternative forms:

pneumatic

Technical Efficiency:

vibration frequencies:

depending on form of drive electric


low frequency,

900 - 3000 min-1



high frequency

6000 - 12.000 min-1



mechanical

600 - 35.000 min-1



centrifugal force:

pneumatic vibrator

10 N - 70 kW



electric vibrator

40 N - 120 kW

ECONOMIC DATA:

Investment Costs:

350 to 400 DM for 12 V - external vibrator

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Equipment which can be driven:

conveying chutes, delivery (feed) chutes, discharging chutes, proportioning chutes, vibrating screens, vibrating sorting units, drainage systems

Regional Distribution:

vibrating devices are being increasingly employed in conveying, sorting, feed-proportioning and drainage equipment.

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high


low noise pollution and possible resonance vibrations

Suitability for Local Production:

very good |————|————| bad

Lifespan:

very long |————|————| very short

Bibliography. Source: Company Information

OPERATING PRINCIPLE:

For use as vibrators or shakers, motors are equipped with unbalanced rotating weights which can be adjusted In order to vary the centrifugal force. An alternative system is the pneumatic piston vibrator, which is characterized by its high adjustability of vibrational frequency and amplitude. Shakers and vibrators can be used as external vibrators mounted to the machine exterior, or as internal vibrators shaking the material directly inside the machine.

AREAS OF APPLICATION:

For loosening or jarring, the vibratory motion reduces the friction forces or breaks down the adhesive attraction, causing the material to loosen and attain flow-like properties. For conveyance, the flow of material can be maintained with the help of vibrations inducing minute forward-advancing movements.

For compressing or compacting, an artificial "flow" of the material, similar to that produced for loosening or jarring, is induced by vibrating whereby the material particles are deposited as densely as possible and the volume of air or water pores is minimized.

REMARKS:

Through the use of an eccentric motor, the machine is shaken by rotational vibration forces. The use of two counter-rotating eccentric motors of identical frequencies produces a resonance due to linear vibration (see diagram below).


Fig.: Operating principle of a single centrifugal vibrator (Fig.1); two counter-roatating eccentric motors (Fig.2); and a linear vibration system with foundation determining the direction of vibration (Fig.3).

Vibrators should always be fixed at the most rigid (reinforced) part of a machine to allow optimal transmission of imposed vibration. In the event that no reinforcements exist, they must be added to the construction in the area where the shaker is to be attached.

When the entire machine is subject to a low-frequency vibrating, it should be mounted, depending on the weight, on rubber. metal fixtures, screws or leaf springs.

The following approximation formula can be used to obtain a rough advance estimate of the dimensions for vibrators based on their centrifugal force:

Centrifugal force = (3 to 5) × (weight of the machine to be vibrated + 0.2 × weight of material to be vibrated)

Additionally, the following rough calculation can also be used (by Italvibras):

centrifugal force = amplitude of vibration × total weight of system to be shaken × ( rpm)² / 900.000

with centrifugal force:

kg

weight: kg

work moment:

kg mm

amplitude: mm

rpm:

min-1


Low-voltage direct-current shakers permit operation with energy supplied from solar cells.

SUITABILITY FOR SMALL-SCALE MINING:

Imported vibrators and shakers, incorporated into locally-manufactured mining and beneficiation machines with high "local content", can increase both the efficiency and technical quality of such equipment. In beneficiation machines, for example, vibrators increase the selectivity of the sorting processes.

Selection of the required frequency range is facilitated by the following table according to Bosch company information


Areas of Application and Vibration Frequency/min.

PROCESSES AND MATERIALS:

normal frequency

high frequency (HF) + compressed air


1000

1500

30000

6000

12.000

COMPRESSING/ COMPACTING of light, normal, and heavy concrete



forms + casings for pre-poured concrete parts, vibrating tables, vibrating frames, battery casings, in-situ-concrete casings, slip form paver, stone forming machines

of bulk materials of all kinds, molding sand, graphite, powdered quarzite, food stuffs


foundry machinery, packing machinery furnace lining, production of electrodes,


LOOSING of bulk materials, e.g. sand, lime, cement, coal, grain, etc.


emptying of silos, bunkers, containers, casting boxes, forms, settling grids



CLEANING


filter equipment, amongst others



CONVEYING of bulk materials, such as sand, gravel, crushed stone, granulates, concrete; of piece goods, such as castings, packages, chips/cuttings

conveyor chutes, discharge chutes, conveying pipes, ducts, vibrating chutes, spiral conveyors



SCREENING dewatering

vibrating (jigging) screen, classifying (sizer) screens, dewatering screening through ceramic sieve



CLOSE THIS BOOKTools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)
D. Beneficiation
VIEW THE DOCUMENTD.1. Definition
VIEW THE DOCUMENTD.2. Initial conditions and problem areas
VIEW THE DOCUMENTD.3. Proposals for procedural and organizational solutions
VIEW THE DOCUMENTD.4. Environmental and health aspects
VIEW THE DOCUMENTD.5. Processing of diamonds
VIEW THE DOCUMENTD.6. Gold beneficiation processing
VIEW THE DOCUMENTD.7 The processing of phosphate-containing raw-minerals into p-fertilizers

Tools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)

D. Beneficiation

D.1. Definition

The term beneficiation includes all procedures related to the enrichment of raw ores to produce marketable concentrates. These include not only mechanical procedures (e.g. wet mechanical processing) which leaves the material composition of the mineral unchanged, but also chemical procedures (e.g. leaching), which transforms the valuable mineral into other chemical compounds. In addition to the separation of valuable minerals from the non-desired material for purposes of concentration, or the so-called sorting process, the pre- and post-preparatory activities such as crushing, classification, drying, etc. are also included under beneficiation.

Significant values which define the success of beneficiation operations are the concentration factor, total weight recovery and valuable mineral recovery as well as the contents of the concentrate.

D.2. Initial conditions and problem areas

The processing of raw ores into marketable products is a problem of major concern for small-scale mining operations. At present, small-scale mining in developing countries is characterized by a distinct dualism. On the one hand, small operations exist which process their products using modern techniques. Problems with energy supply, the acquisition of spare parts, the availability of operating funds, or simply an inadequate knowledge of the equipment frequently drive these operations to the brink of economical efficiency. On the other hand, there are a number of small-scale mining operations which use more primitive labor-intensive methods and simple machine technology to process the raw ore. These operations are also confronted with substantial technical, organizational and economic difficulties. The major problems associated with these traditional processing methods are:

- minimal throughput, or low specific recovery

Traditional beneficiation facilities produce a throughput value for raw ore which is, in some cases, clearly below 1 t/MS. As a result, small-scale mining processing operations in developing countries are labor-intensive. The problem is intensified by the fact that, as a rule, the beneficiation is performed as a noncontinuous operation with frequent breaks and repetition of feeding, drawing, and deposition activites, resulting in high proportions of idle time. In some cases, the idle periods can total up to 50 % of the total work time in small-scale mining beneficiation plants.

- low recovery

Desired-mineral recovery of only 50 % or even less occurs frequently . Half of the valuable minerals, which are expensive to extract underground, end up in the tailings piles. As a result, the recovered concentrate represents high production costs. The reasons for this minimal recovery are predominantly attributable to poor organization and planning of the work steps: too coarse or too fine grinding, insufficient classifying, inappropriate equipment selection, interrupted noncontinuous work operation, careless processing of fine-grained material, etc.

The causes for the low concentrate contents which sometimes occur are:

too wide a range of classification of the feed material for the wet mechanical sorting,

too coarse comminution (liberation not yet attained) or

very finely intergrown ores, for which the separation cut-off size in the fine-grain beneficiation is insufficient.

A modification of the entire beneficiation method is not possible for small-scale mining operations; however, there are a number of technical processes available which, when combined, can significantly increase the recovery in modern facilities to values typically in the range of 70 % and even up to 80 - 90 %, depending upon the degree of intergrowth in the minerals. These processes are:

Physical processes

*

wet and dry mechanical

*

optical

**

magnetic electrostatic processing

Surface-physical processes

*

flotation

Chemical processes

*

amalgamation and leaching, and finally

Biochemical processes


microbial leaching

Of these, only those marked with a * are of relevance for small-scale mining. Those marked with ** are generally only applied for secondary cleaning of the concentrate (re-concentration) and are farmed out to subcontractors (commission beneficiation). All remaining processes are not suitable alternatives for use in small-scale mining beneficiation due to high investment costs, high degree of complexity, local-market restrictions, or the absence of tradition surrounding the particular process in small-scale mining.

A mechanization and modernization of existing processing plants in small-scale mining operations is hindered by a chronic lack of capital or available funds. Credits for financing mechanization are also not available due to insufficient knowledge of the mineral reserves and the lack of feasibility studies necessary to allow the deposit to serve as collateral.

It should also be emphasized that mechanization and modernization cannot always be regarded as positive entities. This is clearly indicated through numerous examples where partially malfunctioning or already abandoned modern beneficiation facilities have been rejected in favor of the simple, traditional small-scale mining techniques. The dependence on energy, spare parts and operating materials, combined with the loss of flexibility as a result of high investment costs, often led to more severe problems than those associated with traditional techniques.

Therefore, the possibilities of technical improvements are limited to the most economic inexpensive investments through the purchase and step-by-step introduction of locally-manufactured equipment. Furthermore, organizational improvements in the processing procedure can provide substantial economic advantages.

As an example, the cooperatively-run lead-silver mine in Pulacayo, Bolivia illustrates the necessity for changes in the work organization of the processing procedures. The miners, organized into cuadrillas (four-man mining team) operate about 30 parallel, traditional beneficiation plants, some of which are only able to process coarse-grained feed exceeding 1 mm in size. Fine-grained material with very high silver contents are discharged as tailings without being separated. The follow a rotating schedule between production and processing in which about one third of a monthly work phase is spent on processing. The ore quantity being mined by the cuadrillas for processing is, however, too small to support a beneficiation which includes fine-grain separation. Only the combined raw-ore output of several cuadrillas would provide a volume sufficient to justify fine-grain separation steps.

Beneficiation facilities exhibiting fewer, less critical problems, can also benefit from the incorporation of organizational or procedural improvements. Even minor optimization can achieve lasting improvements in operating efficiency. The critical role played by beneficiation in small-scale mining has long been overlooked.

Other concepts presented as solutions to small-scale mining beneficiation problems have often failed, as illustrated below:

Mobile processing plants which periodically concentrate the raw ore from an entire small-scale mining area, have failed due to problems with infrastructure and technology. According to a study done by the KfW on the possibility of introducing a mobile processing plant for lead-silver ores in the deposit-rich highlands of Bolivia, no appropriate location or mining region could be found. The lack of homogeneity of raw ores and deposits, poor road connections, and the subsistence existence of small-scale mining operations which demand a rapid return on capital, prevent the successful introduction of mobile processing plants.

Equally problematic is introduction of central raw-ore processing plants. High transportation costs and low ore values limit the profitability of central processing. Furthermore, the experience in small-scale mining in Bolivia has shown that central processing plants can only be successful when operated as non-profit enterprises, possibly sponsored by mining-related governmental agencies, and must be run at high capacity. Such an endeavor requires realistic analysis and weighing of facts prior to implementation. Concepts which deliver ore in the form of preconcentrates, whether as hand-sorted products or as pre-concentrates from simple, traditional separation facilities, expand the area of economic influence (marketing base) and offer more efficient solutions than those involving the sale of raw ores or poorly-processed final concentrates.

Almost without exception, mines located in isolated remote areas have to process their ore in their own beneficiation plants due to the high cost of transportation. The following chapter offers suggestions regarding planning, construction and operation of processing plants appropriate for the needs of small-scale mining.

D.3. Proposals for procedural and organizational solutions



D.3.1 VARIOUS BENEFICIATION PROCEDURES

A number of different processing methods are available for separating raw ores into marketable mineral-ore concentrates, by-products and waste. The composition of the raw ore, the chemical and physical characteristics of the minerals contained in the raw ore, the grain-size distribution, etc. determine which of these methods are most appropriate for separating the desired mineral from the non-desired host material.

The primary processing methods available are:

THE GRAVIMETRIC BENEFICIATION PROCESS:

For the sorting of raw ore feed in which heavy minerals are the valuable mineral source, either dry or wet mechanical methods are employed, depending on the location, which utilize the difference in density between minerals to achieve the separation. In gravimetric processes, variations in density-specific phenomena (e.g. falling speed, radial acceleration), which appear in a sorting medium of air (dry sorting) or water (wet mechanical sorting), to produce a separation of the feed into two or more components (streams), one chiefly containing ore minerals and the other host-rock particles.
Equipment used in gravimetric sorting includes sluices jigs, sink-float (heavy-medium) separators, buddies, spiral separators, cyclones, pneumatic classifiers (sifters), etc.

The gravimetric separation is the processing method typically used in small-scale mining.

THE FLOTATION PROCESS:

In flotation, the different electro-chemical surface characteristics of minerals are utilized in the separation process, in that some minerals in a fine-grained slurry are made hydrophobic through the addition of reagents (collectors, activators). Air injected into a tank (flotation cell) containing the slurry carries the hydrophobic particles to the surface where they collect as foam which is then subsequently scooped off. This form of separation, where the mineral concentrate is removed in the foam is known as direct flotation; when the mineral remains in the heavy liquid component, the process is known as indirect flotation. By varying the pH-values of the slurry and the reagent additives, different minerals can be selectively recovered.

In mechanized ore mining, flotation is the most widely used processing method.

THE AMALGAMATION PROCESS:

This process is applied on precious-metal ores. Gold, silver and some of their compounds have the characteristic that they can alloy with mercury. These alloys are referred to as amalgams. To separate the precious metal, the raw ore is processed together with mercury, the amalgam removed, and the compound then dissociated into the precious metal and mercury by distillation. The amalgamation is performed in washing pans (bateas), sluices, vessels, barrels, amalgamating drums, Chilean (edge) mills, stamp mills, amalgamating bottles or tables.

THE MAGNETIC SEPARATION PROCESS:

Magnetic separation makes use of the varying magnetic susceptability of the minerals contained in the ore being processed. This physical characteristic (magnetism) enables individual, magnetic minerals to be separated from non-magnetic, or less magnetic ones through the use of a magnet.

THE LEACHING PROCESS:

Separation by leaching utilizes chemical solutions, transport and precipitating phenomena Here, under specific Eh-pH conditions, minerals are dissolved by certain acids, leaches or solutions. The presence of bacteria can have a catalytic effect on the reactions. In a separate facility, the metals are dissociated from the solution and concentrated. Leaching is performed in tanks, on ore stockpiles, or in-situ.

Cyanide leaching is gaining in importance in gold mining.

THE ELECTROSTATIC SEPARATION PROCESS:

Electrostatic separation is based on the varying ionization characteristics between minerals subjected to an electric field. This procedure is, however, seldom used.

In addition, there are methods of optical sorting which, however, are only of marginal importance.

Fundamentally, the design of a beneficiation facility should limit, as much as possible, the number of different sorting procedures employed; the greater the number of processes, the more expensive the machinery, and the more complicated, sensitive and unmanageable the beneficiation operation becomes in general.

D.3.2 PREVENTING IDLE PERIODS AND ACHIEVING A CONTINUOUS MODE OF OPERATION

Ore beneficiation in the traditional small-scale mining industry in Bolivia is usually performed as a discontinuous process. Substantial time is lost through intermediary storage of products, restocking the supply of feed or in preparing the equipment. Observations by the authors in the processing facilities indicate that this idle, wasted time accounts for up to 50% of the total time worked. Consequently, attempts to improve processing-plant throughput should be directed toward achieving a continuous mode of operation in which the entire raw-ore feed quantity undergoes comminution, sorting and classifying steps.

D.3.3 CAREFULLY-PERFORMED COMMINUTION

The output in processing plants drops with decreasing grain-size of the feed. Even in modern mechanized plants, the finest grains present difficulties for the operation. Hence, it is absolutely necessary to ensure that comminution is performed so as to produce the smallest possible quantity of fines. This is especially important for those valuable minerals which exhibit a brittle to very brittle tenacity, such as cassiterite, sphalerite and the tungsten minerals scheelite and wolframite. The tenacity describes the fracturing behavior (as opposed to cleavage or scratch (abrasive) hardness) of the mineral, and decisively governs the behavior of a mineral during comminution. Brittle minerals tend to be comminuted quicker, frequently resulting in over-milling (and associated higher proportion of fine material). To prevent the valuable mineral from being reduced to such fine fractions that they can be separated only with great effort, a carefully-controlled crushing is required. When grinding is necessary, it should be limited to a short period, after which a classification can be performed with subsequent regrinding of the over-sized grains.

It is often possible to omit grinding to a large extent.


Figure

D.3.4 PREVENTION OF OVER-GRINDING

Grinding until liberation, or the dissociation of valuable minerals from host rock or waste material, is of fundamental importance to beneficiation technology. In so doing, the occurrence of intermediate products (middlings), i.e. intergrowths of host material with the mineral ores within individual grains, is prevented. On the other hand, however, such a technically-appropriate grinding (from the beneficiation point of view) creates other problems.

High concentrations of fines resulting from excessive grinding not only adversely affect the separation by reducing recovery but also raise energy consumption during grinding, which comprises up to 50 % of the processing costs in modern plants in some cases. In traditional manually-operated processing plants, this energy is produced by hand, for example through the use of simple "see-saw" (or rocker) crushers.

To eliminate the above-mentioned problems, grinding should be entirely omitted when possible and replaced by the processing of coarser-grained material to produce pre-concentrates. A regrinding of the middlings from the coarse-material sorting considerably reduces the feed quantity for the grinding process. This results in lower energy costs (also of importance in terms of energy-supply investment costs), relatively high recovery values, but non-optimal concentrate contents, however.

When the optimal grain size is exceeded, increased losses of the valuable mineral occur during the pre-concentrate separation process as a result of intergrowths which inhibit the complete liberation of the mineral contained in the large grain sizes.

Raw ore characteristics such as degree of intergrowth, grain-size distribution of the valuable minerals, etc. determine whether a grinding of the feed material is absolutely necessary. Whenever possible, the separation steps should receive only a crushed or broken feed material, such as can be produced by a roll crusher, which yields a final grain size of up to 1 mm. The roll-crusher produces a product which is homogeneous in granulation and therefore exhibits a relatively low proportion of fine fractions.

D.3.5 PROCESSING OF NARROW GRAINSIZE RANGES

In all of the sorting processes, and particularly the gravimentric processes, a classifying effect occurs in addition to a separating effect. Many of the gravity-separation processes are based on sedimentation within a water media, whereby the settling velocity plays a major role. Particle behavior of large, light grains (of low specific density) and small, heavy grains (of high specific density) is similar, which is indicated by their almost identical speed of falling. In order to minimize the classifying effects during classification separation, it is necessary to achieve a sufficiently thorough pare-classifying of the feed material to permit further separation to occur only on narrow grain-size ranges. Many of the traditional small-scale mining plants in Bolivia classify their feed, with grain-sizes between less than 30 mm and the finest fraction, into only five or even fewer grain-size fractions. This results in a relatively low total recovery, and low valuable-mineral content in the concentrate, since the concentrate contains impurities of waste-material particles which exhibited the same hydraulic behavior as the valuable-mineral particles during gravity separation.

The density and solids content of the slurry feed are essential parameters for achieving good separation results from classifying, sorting, and clarifying steps. The maximum allowable solids-contents of the feed for the various separation equipment are presented in the following table (from Trawinski, Priester):

Table: Standard Values for Solid Contents of Slurry Feed for Classifying, Sorting and Clarifying Processes


Solids Content of Feed

Conical hydrocyclone

max. 20 % by vol


in extreme cases up to


40 % by vol

CBC cyclone

max. 15 % by vol


in extreme cases up to


25 % by vol

Countercurrent hydro-classifier

25 - 40 % by vol

Rake classifier

30 - 50 % by vol

Spiral classifier

30 - 50 % by vol

Tables

max. 15 - 20 % by vol

Spiral cleaner

max. 15 - 20 % by vol

Conical separator

max. 20 % by vol

Jigs

max. 10 % by vol

Dense medium cyclone

max. 10 % by vol

Countercurrent separator

max. 25 % by vol

Buddles

max. 10 - 15 % by vol

Circular buddies

max. 10 % by vol

Sedimentation barrel

approx. 30 - 50 % by vol

Filter press

15 - 40 % by vol

Disk-type vacuum filter

10 - 20 % by vol

Rotary drum vacuum filter

10 - 30 % by vol

Rotary-drum belt-type


vacuum filter

20 - 40 % by vol

Thickener

max. 5 - 10 % by vol


Fig.: Schematic diagram of a classifying separation with wide-range (1) and two narrow-range (B1 and B2) classified feed fraction; black circles; valuable mineral (heavy component), white circles: vaste mineral (light component).

Table: Gran-size ranges (in ym) of feed material for various beneficiation equipment and techniques: upper and lower limit, respectively; extreme values in parentheses.

Conical hydrocyclone

(5) 10 - 200

Rake classifier

200 - 5000

Hydraulic classifier

(20) 50 - 1000 (2000)

Wet screen classifier

(50) 75 - 5000

Dry screen classifier

(40) 100 - 10000

Pneumatic cyclone

(10) 50 - 150

Sizing drum

250 - 50000

Hand sorting

5000 - (500 mm)

CBC cyclone

20 - 500

Shaking table

(20) 50 - 1000 (3000)

Spiral separator

(30) 50 - 1000 (3000)

Cone separator/ fanned sluice

(30) 50 - 1000 (3000)

Sink-float separator

(400) 500 - 5000

Dense-medium cyclone

200 - 5000

Jig

(80) 100 - 5000 (10000)

Sluices

(60) 100 - 1500 (3000)

Bartle's-Mozley table

(2) 5 - 100 (200)

Low-intensity wet magnetic separator

(40) 50 - 2000 (5000)

High-intensity wet magnetic separator

(10) 20 - 500 (2000)

Flotation

(5) 15 - 500

Foam Flotation

(100) 150 - 1500 (2000)

Selective agglomeration

2 - 50

Thickener

0 - 50

Bartle's belt table

(5) 10 - 100

Amalgamation

(20) 50 - 2000

Gold leaching

0 - 750

Fluidized bed concentrators or centrifuge

20 - 2000

Flotation in sluices

200 - 3000

Flotation in buddies

20 - 250

Washing gulley

100 - 2000

Sludge pond, buddle

(20) 50 - 1500

Mechanized buddle

10 - 500

Dolly tub (Schanz process)

20 - 2000

Air Jigs

30 (200) 500 - 2000

Air tables

50 - 600 (50 mm)

Dry magnetic separation


- low intensity

100 - 5000

- high intensity

80 - 1000

Electrostatic sorting

(75) 100 - 1000 (1500)

Electrodynamic sorting

(40) 70 - 2000 (5000)

Magnetic induction

500 - 10000

Dry Sluice

75 - 1500

Dry vibrating Sluice

200 - 1500


D.3.6 INCREASING SPECIFIC THROUGHPUTS

The use of certain equipment or processes in a traditional beneficiation procedure limits the throughput of the entire operation. An example of this is the employment of sludge ponds to recover the fine-grained solids in a slurry, which perform with such a low throughput so that some processing plants have entirely eliminated any separation of fines. Considering that the finest grains contain significant amounts of the valuable mineral, this decision is detrimental in terms of total plant recovery values. As an alternative, solutions such as those applied, for example, in San Cristobal, Porco, Bolivia should be emphasised. In this region, the parallel operation of multiple sludge ponds has been implemented in order to increase the specific throughput in the fine-grain separation steps. The simultaneous, parallel running of other processing steps in a continuous or semi" continuous operation is likewise possible, such as pinched sluices, spiral separators, funnel furnaces, etc.

D.3.7 HYDROCLASSIFYING VS. SCREENING

Especially in wet mechanical beneficiation processing, the type of classifying employed determines the precision of separation in the sorting process. Hydroclassifying is clearly more appropriate than screening for feed-preparation of sorting equipment such as furnaces, buddies and sluices. The reason for this is that a hydroclassified material is separated according to equal settling rates, which means that larger, lighter particles and smaller, heavier particles end up in the same fraction. When one of the above-named pieces of equipment is charged with this feed, a better spatial separation between heavy and light materials is achieved than with screened feed due to the drifting resulting from the flow forces applied on the grain surfaces. A further advantage for small-scale mining is the continuous operating mode which hydroclassifying provides in non-mechanized plants.

At present, screening is the primary feed separation method used in traditional small-scale mining in developing countries. It has, however, the following disadvantages:

- low throughputs
- low separation precision
- higher operating costs, and
- discontinuous mode of operation,

which are eliminated with hydroclassifying.

D.3.8 PRODUCTION OF PRE-CONCENTRATES

In order to avoid handling large quantities of material in the beneficiation facility, one of the initial steps should be the production of pre-concentrates, particularly where feeds of low valuable-mineral content are involved, such as tin ore with around 2 % Sn, but also for higher-content feeds as well. These pre-concentrates can be produced by one of two methods, or a combination of both. The simplest method involves manual hand sorting, whose importance and application to "selective semi-mechanized mining" in solving beneficiation problems specific to small-scale mining has already been described in Horvay (1983). Through manual sorting or hand picking, a marketable hand-sorted concentrate, as well as a pre-concentrate for further beneficiation, is obtained. The alternative method for achieving pre-concentrates employs sorting equipment with high specific throughput.

Whereas hand sorting of pre-concentrates is realistically limited to material of grain-sizes larger than 10 mm, a wide assortment of pre-concentrating sorting equipment is available for feed material of grain-sizes ranging from 30 to 100 mm. These are:

piston jig

Sluices, sludge ponds, spiral separators,

pinched sluices

The employment of any of the above-named sorting equipment requires a presizing of the feed material in order to achieve a sufficiently high recovery from the pre-concentrating process.

- The primary advantage of pre-concentrating the raw ore is that the quantity of feed entering successive sorting steps is reduced. Pre-concentration of feed material, for example tin ore, from 2 to 4 % Sn (in this case), eliminates 50% of the waste material (assuming 100% recovery), and the throughput quantity in the succeeding steps is reduced to one half.

- For all of the marketable hand-sorted pre-concentrates, further beneficiation efforts (comminution, classifying, sorting) are not necessary. Losses in recovery can also be avoided for this portion of the ore.



D.3.9 HOMOGENIZATION OF FEED MATERIAL

In small-scale mining in Bolivia, the authors could repeatedly observe that totally inhomogeneous feed material served as charge for the various separation equipment. A sludge pond for fine-grain separation serves as an example in which first the middlings from a previous separation step and then raw ore comprised the feed, whereby the second feed input (raw ore) was deposited directly onto the sedimentation cone of the first (middlings). This procedure can lead to spatial variations in concentrations within the subsequent sedimentation cone due to extreme periodic variations in the granulation and heavy-metal content of the feed. This problem can be solved by mixing the separate feed constituents in order to attain a homogenous feed prior to further processing. Homogeneity of the feed is essential for semi-continuous or continuous processes whose operating parameters such as feed quantity and rate, inclination of separating tables, reagent additives, etc. are determined by the slurry-feed characteristics.

Sufficient homogenisation can frequently be achieved through very simple methods, such as the dumping of different feeds, one on top of the other, onto the cone-shaped discharge pile. While the cone as a whole is inhomogeneous, removing the material from the side near the bottom of the cone induces a certain degree of homogeneity through the resulting sliding and resettling of material.

D.3.10 SECONDARY PROCESSING OF THE MIDDLINGS

In all traditional beneficiation procedures, middlings are produced as a by-product of the processes. These products occur as two different forms, namely:

- middlings produced as a result of low separation accuracy in the sorting facility. Although the components are liberated, i.e., the valuable mineral occurs as free grains and is no longer intergrown with host rock, waste material, or secondary minerals; however, the grains are not separated according to whether they do or do not contain the valuable mineral. This type of middlings frequently occurs in mechanized gravity-separation processing, especially when the specific characteristics, such as density, do not vary greatly between the valuable mineral and the host rock particles.

- middlings which emerge from prior comminution steps but still exist in an unliberated form where individual grains still contain intergrowths of the valuable mineral with host rock material. This type of middling product occurs even in the most precise separation processes, and valuable mineral so contained cannot be separated by further processing without additional comminution.

The two forms of middlings can also occur as a combination. In any event, the nature of the middlings must be determined prior to any successive processing to prevent any unnecessary expensive regrinding of already-liberated material and resulting reduced recovery due to the increased proportion of fines. The washing pan (common for panning for gold) offers a simple, fast and reasonably priced apparatus for quickly determining the characteristics of the middlings and the further processing steps required:


- liberated middlings require secondary separation
- non-liberated middlings require recrushing or regrinding prior to secondary separation.

In small-scale mining in developing countries, middlings frequently receive only very incomplete further processing, or are simply discarded as waste. This practice, however, cannot be economically justified; no additional mining costs, and only minimal grinding and separating costs, are incurred by secondary processing of the middlings, costs which generally can be recovered through marketing of the resulting products. Only in cases of very fine-grained material should the sale of middlings to an operation with mechanised beneficiation be considered.

D.3.11 CLASSIFYING OF FEED PRIOR TO SEPARATION PROCESSING

Technical journals of the last century record the debate among engineers over the English versus German classifying methods used in beneficiation processes.

The "Harzer" or German method involves first sizing the feed material and then separating the narrow grain-size fractions, while the English method makes use of the sizing effect of the wet mechanized separation operation and then classifies only the products. For example, in the case of sludge-pond separation, the feed material, which includes a wide range of grain-sizes, is sorted and the concentrate extracted and then classified. The coarse-sized material thus obtained comprises the end concentrate, and the undersized material constitutes the pre-concentrate which is then further separated.

Mining of base metals (non-ferrous metals) in Latin America, particularly tin mining, was primarily influenced by Anglo-Saxon engineering during the 19th century. As a result, the English method of wet-mechanized beneficiation has been dominated even in small-scale mining. The advantage of this method is that only the concentrates and the middlings are classified, with waste material remaining unclassified. In so doing, the cost of sizing is minimised. I However, the several disadvantages associated with this method justify a reconsideration of the use of the English method in small-scale mining. On one hand, the sorting of feed material which exhibits a wide-range granulation occurs at such high slurry flow velocities that the coarse grain fractions are also separated out. These high slurry velocities also frequently cause the fine and very fine-grained particles to be carried off due to their large specific surface area and be removed as part of the tailings. A sizing of the material before sorting would have the advantage that the fine and finest grain fractions could be separated and sorted at low slurry flow velocity. On the other hand, the disadvantages of subsequent classifying via settling are substantial. Materials exhibiting a wide range of grain sizes are more difficult to sort by settling processes than materials of narrow-range granulation. This is explained by the fact that the bonds in narrow-range grain-size fractions are loosened more easily during the pulsating settling process, therefore requiring less energy. This is of significance particularly in the manually-run jig separation process in small-scale mining in developing countries.

D.3.12 BENEFICIATION OF FINE-GRAINED MATERIAL

A significant shortcoming of beneficiation facilities, both in large-scale operations as well as in small-scale mining processes in developing countries, is the insufficient attention devoted to fine grain sorting. Beneficiation plants with low valuable-mineral recovery (for example, less than 50 % recovery from modern mechanized beneficiation of tin ores at the Bolivian state-owned COMIBOL mines), lose, as a rule, a large quantity of the valuable-mineral source in the fines. Additionally, plants are encountered where fine-grain sorting is non-existent. The rich silver ores of Pulacayo (Bolivia) are beneficiated using traditional small-scale mining methods whereby, in some cases, all material smaller than 1 mm lands on the waste pile. In view of this problem, the significance of fine-grain beneficiation cannot be emphasized enough. Especially for two raw-ore types, the concentration of valuable mineral in the fine and finest fractions is of great importance:

- raw ores which exhibit a fine intergrowth and therefore require fine grinding to liberate the valuable mineral. Deposits of non-iron metallic ores, for example those of sub-Volcanic or submarine emanative genesis, or sulfide veins with oxidized valuable-mineral sources, or stratified tin deposits, such as frequently occur in the Latin American Andes, exhibit this fine intergrowth and must be handled during beneficiation with special attention regarding the fine grain distribution. Similarly, alluvial gold deposits where the gold occurs as fine grains also belong to this category of raw ores. In traditional mining operations without any separate fine-grain separation processes, the recovery can lie well below 10% in some instances.

- raw ores where the valuable-mineral sources are brittle minerals which are quite easily subject to overgrinding during comminution. Sphalerite, cassiterite (tin ore) and scheelite are only a few examples of this type of brittle mineral ore (see Table). A pre-concentrate can already be achieved by performing selective classifying, since the fine" grain fraction already represents a pre-concentrate following the initial comminution step. In any event, beneficiation of these raw materials requires that particular consideration be given to the fine-grain fractions.

One solution is demonstrated by the unfortunately already historic example of a wet mechanized silver-ore beneficiation performed in Pulacayo, Boliva up until 1952, where even separating table wastes were resorted using mechanized sludge ponds to achieve very fine concentrates. In mining of gold alluvial deposits, gold centrifuges and cyclones, for example, could be employed; for extracting non-iron metallic-ore concentrates, the above-mentioned mechanized sludge pond, Bartles-Mozley-separating table, or blanket sluice (corduroy table), etc. could be used.

Difficulties are encountered in the wet mechanical separation of fine and very fine-grained material due to the fact the final falling velocities of minerals of varying density approach similar values with decreasing grain size. Thus, beneficiation of the finest grains involves greater expense and achieves lower recovery at a lower degree of concentration compared to those separation facilities for coarsergrained material. Nevertheless, in the majority of cases, a fine or finest-grain sorting stage is of advantage.

D.3.13 MANUAL SORTING BY HAND

Hand sorting of raw ores, feed materials and concentrates during beneficiation is of special significance in small-scale mining operations, as mentioned by Horvay (1983) amongst others. Examples from fluorite mining in the Upper Pfalz region of Germany (until 1988) show that even under conditions of extremely high labor costs, as found in German mechanized mining, hand picking plays an important role. Pre-concentrates or concentrates can be won by manual sorting, performed either as negative selection (sorting out of waste-rock material) or as positive selection (selection of chunks of pure ore). In both cases, the material load on the beneficiation plant is obviously reduced. Moreover, for positively-selected material, losses due to low valuable-mineral recovery are minimised. One difficulty is the relatively low efficiency, or performance rate, which characterizes the hand-sorting operation in Andean small-scale mining, as a result of very poor working and sorting conditions. Improving the hand-sorting operation by providing cleaner material (through wet classifying of coarse material, for example), better lighting, etc. at the separation tables or sorting belts could increase efficiency.

D.4. Environmental and health aspects

Beneficiation operations exert substantial impact on the natural environment.

Noise pollution from comminution (crushing or grinding) processes and the operation of power equipment.

Air pollution from multiple sources:

- Dust pollution, especially as a result of dry sorting of feed material, for example from air classifiers and dry classifying.

- Air pollution resulting from mercury vapors produced during open-circuit distillation of amalgam occurs frequently in gold mining and leads to a variety of health risks due to mercury contamination: loss of hair, decay of fingernails and bones, and can also result in death (see also Section D.6.5.1).

One solution to this problem is the implementation of closed-circuit amalgamation through the use of distillation retorts.

Water pollution. Contamination of the drainage system from beneficiation processes is an especially serious and dangerous problem, particularly considering the multiple utilization of surface water. In semi-arid regions with defined dry periods, rivers represent the ultimate source of water. The use of water can basically be categorized according to three primary purposes:

1. as drinking water for the population, which usually uses untreated water directly from rivers.

2. for irrigation purposes in agriculture, and

3. as process water for small industries, whereby mining with its widespread geographical distribution and large water requirements for raw-ore beneficiation is the primary industrial consumer of water.

Legal restrictions regarding water rights, environmental regulations, etc. in the Andes region are generally either non-existent, or their compliance not controlled, so that competitive surface water consumption needs pose serious problems.

The situation is worsened by the fact that the natural biochemical decomposition of toxic pollutants in the water occurs at a substantially slower rate in the Andes region due to the high elevation with its low oxygen partial pressure and very low water temperatures.

Specifically, the following pollutants may be released by beneficiation processing:

- Sludge/Silt: occurs in all wet-mechanized and flotation beneficiation processes.

- Toxic flotation reagents: those reagents most commonly used in small-scale mining in Latin America are sulfuric acid, diesel oil and long-chained carbon-hydroxides (frothers and collectors) such as xanthate. In small-scale mining, the manner in which these substances reach the drainage system is not known. Especially problematic is the regulation of dosages of reagent additives used for the noncontinuous, low-recovery flotation processes. Compared to large industrial-scale flotation operations, the concentrations of reagents used in small-scale mining are extremely high.

- Highly toxic cyanides: used as activator substances in selective sulfide flotation and in leaching. The decomposition of cyanide normally takes two years; however, in the Andes region the process is accelerated as a result of more intensive ultra-violet (UV) radiation at higher elevations. Demarcated sludge ponds (sedimentation basins) for receiving waste products are urgently necessary in small-scale mining as well.

- Amalgam and mercury: These two substances are released in water during amalgamation of gold in stamp mills, sluices, tables, and Chilean (edge) mills. More detailed information on this subject is presented in Section D.6.5.

The mining industry's most serious environmental problems stem from the beneficiation operations. In this area, changes and remedial measures designed specifically for small-scale mining are particularly important, a fact which justifies the large amount of attention given to beneficiation in this handbook.

D.5. Processing of diamonds

Diamonds constitute an important branch of precious-stone extraction. Small-scale mining accounts for about 10 - 15 % of the entire global diamond production. The methods employed for mining and processing diamonds differ according to the geology of the deposit:

1. Primary deposits, diamond-containing volvcanic breccia (tuff) of basic and ultra-basic rocks such as Volcanic chimney vents, the socalled Kimberlite or blue ground; additionally, Precambrian olivine rock.

2. Secondary deposits which consist of weathered, decomposed products of diamond-containing rocks. These may develop either as hardened sediments, for example in the form of conglomerates, as loose sediments in river beds, or above blue-ground deposits as yellow ground.

In the beneficiation of diamonds originating from primary deposits or hardened sediments, care must be taken to prevent the precious raw stones from being crushed or ground along with the waste rock. The high cleavability (splitting tendency) of diamonds requires a very careful grinding of the parent rock. In the South African small- and medium-scale diamond mining operations, a special form of grinding has been developed. Following extraction, the feed material is thinly distributed over the ground surface where it is exposed to natural weathering. On the so-called 'floors' the weathering process is enhanced by adding water. The sorting of the comminuted material can proceed in different ways:

OPTIC-MECHANICAL :

Performed by hand sorting, whereby the feed material is spread out in a thin layer on a sorting table and the diamonds, being highly visible due to their light refracting characteristic, are manually sorted. The lower profitable grain-size limit lies at a weight of about 5 mg (1/40 karat).

Modern optic-mechanical separation procedures involve photometric or radiometric sorting which utilizes artificially-induced luminiscence of the diamond. A thin stream of material flows through an optical detector which responds to the special optical characteristics of the diamonds and steers a pneumatic nozzle which blows the diamond grain out of the material stream.

GRAVIMETRIC :

Gravimetric utilizing the density of the diamond (3.52 g/cm³ )

In the processing of diamonds, small-scale mining in developing countries frequently uses jigs, mostly in the form of manual separators. In this procedure, the lower profitable grain size is about 150 ym due to the minimal density variations between the quartz, the main sediment component, and the diamonds, the valuable mineral (q = 1.48 for separation in water). To increase the precision of separation, jigs with beds are used; for diamond processing, glass balls serve as the bed material (glass bed).

Grease tables utilize the strong hydrophobia exhibited by diamonds; the feed material is suspended in a slurry which flows over the greased surface of a stationary sorting table. The diamonds are drawn to the grease, from which they are later individually recovered.

Additional methods of gravimetric separation include the sink-float separation processes with FeSi-slurries in normal sink-float separators or in heavy-media cyclones. The FeSi, a weighting material for increasing the slurry density which appears 65 to 90 % in the <0.05 mm fraction, is recovered after sorting by means of magnetic separation.

ELECTROMECHANICAL:

Electrostatic-separators can successfully separate diamond-containing feed up to maximum grain size of 6 mm, whereby the semi-conducting characteristic of diamonds are utilized as the basis of separation.

D.6. Gold beneficiation processing



D.6.1 GENERAL INFORMATION

The processing of precious-metal-containing raw minerals places special demands on the separation method employed due to the physical and geochemical characteristics of the gold and the economic geology of the deposits. Gold generally occurs in deposits where the content of raw ore, in primary deposits, lies at 100 - 200 g/t (maximum) and 1 - 2 g/t (minimum). The lower limit serves as the grade cut-off for marginally economically mineable deposits. Sedimentary deposits generally contain between 0.2 and approx. 20 · 50 g/t raw precious-metal ore. The beneficiation of these ores must, correspondingly, concentrate to a factor of up to 100,000. At the same time, comparatively larger amounts of raw ores must be mined and processed in order to cover the production and processing costs. Due to the low wages in most developing countries, coupled with the predominance of manual labor, a gold recovery of about 0.3 9 gold per man-shift is still considered an acceptable production level.

A further problem confronting gold processing, specific to precious-metal alluvial (placer) deposits, is that many operations can only mine seasonally. During the rainy season, the rivers often carry such large quantities of water that mining activities in the riverbed or along the banks are hindered. Correspondingly, the beneficiation facilities must either be located above the high-water level or be semi-mobile to allow its transfer to higher ground at the start of the rainy season.

Additionally, the grain shape of gold, both from sedimentary deposits as well as after grinding, is in many ways unfavourable for hydromechanic gravity processing. Flat, flour-type gold grains of the smaller particle range can only be gravimetrically separated with major difficulty, despite the high specific density of gold.

D.6.2 ALTERNATIVE PROCEDURES

Among the various techniques for general mineral processing, many can be applied specifically for the processing of gold ores. The methods can be differentiated according to those methods which produce pre-concentrates that are not marketable as final concentrates, and those methods which lead to marketable final concentrates containing between 90 and > 99 % Au. These processing alternatives are presented in the following tables, in which those techniques appropriate to small-scale mining appear in bold face.

Table: Methods for the processing of gold ores into pre-concentrates.

Type of separation

Process

Steps

Equipment

Reeagents

mechanical

GRAVIMETRIC BENEFICIATION

sorting

gold pan, jigs, sluices (wet + aero), tables (wet + aero), animal skins centrifugal classifiers, spiral classifiers, CBC cyclone separators, heavy material traps



DENSE MEDIUM SEPARATION

sink-float separation

sink-float separator, glass flask

dihydrogendodecawolfra. mate =3.1g/cm³

electrical

ELECTRO-STATIC BENEFICIATION


esta-separator


surface mechanical

FLOTATION





- indirect

conditioning, sorting, washing

conditioning tank flotation cell

frothing agents, collectors, depressants, activators


- direct

conditioning, sorting, washing


pH-reagents

magnetic

MAGNETIC SEPARATION

sorting

magnetic separator


* analytical method only

Table: Methods for Beneficiation of Gold Pre-concentrates into high-quality marketable Gold Concentrates

Clase of separation

Process

Steps

Equipment

Reagents

mechanical

HAND PICKING (SORTING)





COAL-GOLD AGGLOMERATION

agglomeration, separation, stripping

reaction vessel/tank

oil, activated carbon

thermal

ROASTING, AIR CLASSIFYING

roasting, air classifying

roasting furnace



GOLD VOLATILIZATION

chloridized roasting, voiatilization


sodium chloride, chlorine gas


SEPARATION by SMELTING

smelting, separation of gold

furnace, caucible

borax, soda, potash


FIRE ASSAY*

smelting with gold collector, separation, cupellation

muffle or retort furnace, crucible, cupel

taste (assay) lead, borax, soda, potash

chemical

AMALGAMATION with open or closed Hg cycle

alloying, separation, distillation

in stamp mill, chilean mill, amalgamating barrel, gold trap, sluice, amalgamating table, gold pan, centrifuge, amalgam press distillation retort

mercury, possibly caustic soda, sodium amalgam ammonium chloride, cyanide or nitric acid for joining finest Hg beads surface act. agts., tensides.


CYANIDE LEACHING as heap leaching, vat leaching, agitation leaching with Merill-Crowe, CIP, CIC-, CIL process or zinc precipitation

chemical solution as complex, adsorption, stripping

leaching tanks, adsorbers

Na cyanide CaO for adjusting pH, Zn
(possibly + PbNO3) or activated carbon


THIOUREA LEACHING

chemical solution as complex, adsorption, stripping

leaching tanks, adsorbers

thiourea, pH-reagents, Al or Fe powder SO2


CHLORINATION BIO-D- LEACHANT PROCESS

formation of halogen- complexes (e.g. tetra- chlorine- bromine com plex)

reaction tanks, leaching tanks

chlorine gas, organic bromodimethylhydrates


BRINE LEACHING



salt solutions, manganese dioxide, sulfuric acid


LEACHING with solutions, containing thiosulfate, rhodonate, polysulfides or nitrite




biological

BACTERIAL LEACHING



bacteria, air as oxidizing agent

* as an analytical method only. Techniques printed in bold type are wholly or partly applicable to small-scale mining.

D.6.3 PROCESSING PROCEDURES

Depending upon the nature of the raw ore, and the investment possibilities for the beneficiation plant to acquire equipment, processes emerge which include production of final concentrates. A few selected procedures for gold-ore beneficiation of various raw ores and grain size magnitudes are presented as flow sheets on the following pages.


Flow sheet of a small-scale manually-run gold-ore beneficiation plant in the Philippines.


Flow sheet of a small-scale tank leaching of tailing containing free (liberated) gold and adsorption using locally produced activated carbons, Brazil.


Flow sheet of a small gravimetric beneficiation plant for primary gold-ores in the Andean region of Narino, Colombia.


Flow sheet of a large mechanized beneficiation plant for primary gold-ores with a combined gravitational and leaching process. The hydromechanically-extracted pre-concentrates are amalgamated, the fine material processed by a tank leaching and the Merrill-Crowe process and then refined by a smelting separation.


Flow sheet of a beneficiation plant for primary gold ores with amalgamation and leaching, Mina Los Guavos, Narino, Colombia.


Flow sheet of a mechanized beneficiation plant for primary gold-ores from Bolivia (Mina Luchusa/Dept. La Paz), wich is however also typical for small and medium-scale operations in Chilean gold mining.


Flow sheet of a small gold beneficiation facility in vein-ore gold mining in Ecuador.


Flow sheet of a small manual alluvial-gold beneficiation operation in Brazil.


Flow sheet of a mechanized alluvial-gold beneficiation facility near Barbacoas, Narino, Colombia.

In small-scale gold mining in developing countries, gravity separation for pre-concentrating as well as amalgamation for production of marketable final concentrates are of major importance. The technical optimization of these processes in order to increase recovery and pre-concentrate contents are critical aspects in improving beneficiation operations. Suggestions for attaining these goals are offered in the respective technical sections of the handbook.

D.6.4 PRODUCTION OF BY-PRODUCTS

A further strategy for improving the economic success of gold processing plants includes the marketing of by-products. In primary gold deposits, the deposit genesis of the associated (paragenetic) mineral composition determine the economic feasibility of mining or processing by-products, which, amongst others, include:

- Antimonite

- Scheelite

- Copper pyrite

- Bismuth minerals

- Uranium minerals

- Silver and silver minerals

- Galena (PbS)

- Sphalerite

ALLUVIAL GOLD DEPOSITS

Fluvial heavy-mineral deposits, which include important gold deposits, represent the physical deposition of heavy, weather-resistant minerals, meaning that the sought-after gold can be associated with numerous other minerals. Some of these by-product minerals are easy to extract and market separately (the names of which appear marked with a * in the following table).

Table: Potential Composition of Alluvial Gold Deposits and their Primary Characteristics

Mineral

Chemical Formula

Color

Density (g/cm³)

Hardness according to Mohs

Remarks

Free gold*

Au(+Ag)

golden-yellow

15.6 - 19.3

2.5


Magnetite

Fe3O4

black

5.2

5.5 - 6.5

shiny, strongly magnetic

Ilemenite

(Mg,Fe)TiO3

black

4.5 - 5.0

5.6

weakly magnetic

Garnet

+3M³+2(SiO4)3²

red, brown

3.8

6.5 - 7.5

vitreous luster

Zirkon *

ZrSiO4

brown, light yellow, colourless

4.7

7.5

diamond luster

Hematite

Fe2O3

dark steel grey, black

4.9 - 5.3

5.5 - 6.5

rounded grains

Chromite

FeCr2O4

iron black to brown black

4.1- 4.9

5.5

possibly weakly magnetic

Olivine

(Mg,Fe)2SiO4

olive green

3.3 - 3.4

6.5 - 7.0

vitreous luster, transparent to translucent, good cleavability

Epidote

HCa2(Al,Fe)3SiSO1V3

pistachio green

3.2 - 3.5

6.7


Pyrite

FeS2

bronze yellow

4.9 - 5.1

6.0 - 6.5

angular grains, metallic luster

Monazite *

(Ce,La,Di)PO4+ThO2

yellow

4.9 - 5.3

5.0 - 5.5

resinous or greasy luster, rounded grains

Limonite

2Fe2O33HO

dark brown

3.6 - 4.0

5.0 - 5.5


Rutile

TiO2

red brown, red

4.2

6.0 - 6.5

metallic diamond luster

Platinum *

Pt (possibly also Ir)

steel white

16.5 - 18.0

4.0 - 4.5

malleable, flakes and grains

Iridium *

Ir (also Pt, etc.)

silver white greyish

22.6 - 22.8

6.7

angular grains

Iridosmium*

Ir Os

tin white to light steel-gray

19.3 - 21.1

6.7

flat grains, tenacious, good cleaveability

Cinnabar

HgS

red

8.0 - 8.2

2.0 - 2.5


Wolframite*

(Fe,Mn)WO4

black, dark grey

7.2 - 7.5

5.0 - 5.5

semi-metallic luster, good cleavability (axotomous)

Scheelite *

CaWO4

white, light yellow, brown or grey

5.9 - 6.1

4.5 - 5.0

diamond to greasy luster, translucent

Cassiterite *

SnO2

brown or black

6.8 - 7.1

6.0 - 7.0

friable, rounded grains

Corundum *

Al2O3

brown, yellow

3.9 - 4.1

9.0

diamond to vitreous luster

Saphire

Al2O3

blue

3.9 - 4.1

9.0

diamond to vitreous luster

Ruby

Al2O3

red

3.9 - 4.1

9.0

diamond to vitreous luster

Diamond *

C

white, colourless, pale

3.5

10.0

diamond to greasy luster

Native Mercury

Hg

tin white

13.6


small opaque, fluid beads

Amalgam

Hg, Ag, Au

silver white

13.0 - 14.0


friable to tenacious

Galena

PbS

lead grey

7.4 - 7.6

2.5 - 2.7

metallic luster,very good cubic cleavage, brittle

Silver *

Ag

silver white

10.1 - 11.1

2.5 - 3.0

tenacious,malleable, black tarnished

Copper

Cu

red brown

8.8 - 8.9

2.5 - 3.0

tenacious, flexible

Bismuth

Bi

tin white

9.8

2.5

friable, metallic luster

Cerussite

PbCO3

colourless, white

6.5

3.0 - 3.5

diamond luster

Columbite * Tantalite

(Fe,Mn)(Nb,Ta)2O6

iron-black, grey, brown-black

5.3 - 7.3

6.0

iridescent, semi- metallic luster, good cleavability

Quartz

SiO2

colourless

2.6

7.0

vitreous or greasy luster, no cleavage

Felspar

Silicates with K, Na, Ca, Al, etc.

colourless, white, light yellow, cream, pink

2.5 - 2.7

6.0 - 6.5

good cleavage vitreous luster,


D.6.5 TECHNICAL AND ECOLOGICAL PROBLEMS IN AMALGAMATION

Amalgamation is one of the most important processes in gold production in small-scale mining in developing countries. Gold in ore slime is alloyed with mercury into an amalgam and then this is separated by heating into mercury steam and gold.

The simplicity of the technique and its gold yield has favoured amalgamation in the eyes of small-scale miners. Health risks and ecological dangers are however not considered. As a result of the faulty application of the procedure, reports of massive mercury poisoning in developing coutries are encountered now and again, Unfortunately, such incidents are not to be viewed as isolated accidents. The same is true for Latin America where, according to estimates, a million people work directly in gold mining. In Brazil alone 650.000 people are active in this branch. Other important gold producing problematic countries of South America are Bolivia, Chile, Ecuador, Colombia, Venezuela and Surinam. But also in countries of other continents, for instance, the Philippines, New Guinea and Ghana, environmental problems as a result of the application of mercury are increasing.

The sensibilization of people to ecological issues in Brazil in connection with the destruction of tropical rain forests has lead to intensified investigations into the mercury problems.

Exact figures about the extent of Hg-emssion in the tropical ecosystem are hardly available especially since figures about mercury purchase do not exist and the real gold production - which eventually allow inferences - lies very evidently above the official output. According to Brazilian reports, mercury consumption lies between 35 and 200 t Hg/y. The most recently promulgated mercury prohibition in Brazil has largely remained ineffective.

D.6.5.1 TOXICOLOGY OF THE HG AND ITS COMPOUNDS

The toxicity of mercury depends greatly upon the nature of the compound and the state of oxidation of the mercury.

Some 75 - 80 % of steam-forming mercury, such as that released in amalgam distillation in an open cycle or circulation, is reabsorbed pulmonarily by humans. It reaches the kidneys through the bloodstream and with a half-life period of about two months, it is excreted again from the body as Hg-protein compound. The toxic effect results from the Hg2+-lons. The manifestation of an acute Hg poisoning through inhaling of mercury steam proceeds in stages as follows:

1. Colic, vomitting and intestinal inflammation

2. Kidney and urinary tract complaints

3. Acute intestinal inflammation, and eventually

4. Formation of cysts on the gums (stomatitis mercurialis) accompanied by a heightened light sensibility (Photophobia).

If the mercury steam is inhaled for a longer period, chronic poisoning develops (Merkurialismus). The symptoms are:

- formation of cysts
- HgS-deposits in the body
- nervousness, and trembling
- speech impairments, concentration difficulties, among others

Many "garimpeiros" ("gold diggers" in Brazilian Portuguese) suffer from acute and chronic mercury poisoning.

Inorganic Hg2+-compounds exhibit analogous toxicity consequences.

Organic mercury compounds, particularly methyl mercury (CH3Hg+) are highly toxic for men. When taken in through contaminated food, this is assimilated in the blood due to its stability and solubility in fat, and leads to damages to nerve ends.

Metallic mercury cannot be absorbed by the human body and is not toxic in this form.

D.6.5.2 MERCURY CYCLE

Mercury that is released in the atmosphere by evaporation is oxidized in the course of time under the influence of ozone, air humidity and ultra-violet radiation. Precipitation transport these ions to earth. Further details of the Hg-cycle in the biosphere and the incorporation of metallic mercury through mining. Microbial anaerobic conversions especially in aquatic ecosystems and on land can lead to a methylizing of the mercury.

The above mentioned inorganic and organic Hg-compounds reach the human body through drinking water, food and through respiration. An especially critical point is the Hg-concentration through the food chain of fishes which can accumulate this element at a multiple rate compared to the concentration in the environment. This effect is even increased by the fact that the Hg-transformation in methyl mercury and its intake in warm, tropical bodies of water (depending upon the temperature and Eh-pH conditions) is especially high.

New researches in Brazilian ecosystems show clear violations of the effective "Maximale Arbeitsplatz Konzentration" (MAK) and "World Health Organization" (WHO) threshold value for Hg and its compounds (see box).

WHO- and MAK-limits for mercury

drinking water

maximum 4 yg/1


fish

maximum 0.5 yg/g weight;



or

maximum 0.2 mg methyl-Hg


per person and week



or

maximum 0.3 mg inorganic Hg

fruits

maximum 0.03 mg/kg weight


air one breathes

for Hg°

maximum 0.1 mg/m³ (MAK)


for organic



Hg-compounds

maximum. 0.01 mg/m³ (MAK)

The following mercury contents were found in:

drinking water, up to

11/µ/ltr

in fishes, up to

2.7 µg/g peso fresco

in spawns, up to

3.8 µg/g

in the air, up to

0.3 mg/m³

The last figure was obtained in the surroundings of an amalgam distillation plant The extreme values measured exceed the corresponding reference measurement in drinking water by a factor of 250, in fishes by about 300 times and in the air by a factor of 14,000. Unfortunately, it was found that the mercury concentrations were not restricted to the particular area. Rather, significant mercury levels were found within a radius of about 200 km around the mining area.

This manifests itself in the mercury levels in human blood, in the urine and in the hair particularly in comparison to the normal values contained in parentheses below:

in the blood

in urine

in the hair


ppb Hg

ppb Hg

yg/g dry weight


up to 175

up to 225

up to 40.0


(10-13)


(0.5-8)

(0.7-3)

The indian natives are affected in a particular way by the mercury contamination of the environment since they nourish themselves almost exclusively from their immediate surroundings. River fishes are, for example the most important source of animal protein for this ethnic group. To worsen their situation, migrating gold diggers are competing in their living space.

D.6.5.3 AMALGAMATION IN SMALL-SCALE MINING FOR GOLD

The first use of amalgamation for gold production presumably dates back to mining in Bosnia in the reign of Emperor Nero (54- 68 A.D.). Until now, small-scale mining uses this technique very intensively.

For amalgamation, liberated, basic, not incrusted Au- for instance through fine iron oxides - in grain sizes of between 2 mm and 20 - 50 m is appropriate. The lower grain size is essentially determined by the interfacial tension of the mercury and that of the water as well as the shape of the grain.

Amalgamation may be applied in sedimentary ores as well as the primary intergrown gold ores. In alluvial deposit mining, the already liberated gold is made to combine with Hg. Riffle troughs whose riffle spaces are filled with mercury mainly serves this purpose. The entire suspended feed is made to flow through the trough. During this process, the slurry extracts about 5 - 30 % of the mercury from the troughs for which generally there is no available catchment mechanism. The addition of bigger amounts of soap or similar tensides should increase the beneficiation output while Hg losses decreases.

Primary ores require the exploration of valuable minerals. The miner amalgamates either directly during the grinding or crushing or in a separate procedural stage after grinding. In simultaneous amalgamation and crushing, small-scale mining utilizes pan grinders, stamping mills, ball mills or manual weight crusher. For post-activated amalgamation, amalgamating barrels, amalgamating furnaces (see respective technical discussions) and manual amalgamation in washing pans are used.

On the average, losses on metallic mercury from the sorting and amalgamation installations account for about 40 - 50 % of total losses.

The resulting amalgam-Hg mixture is separated into the highly viscous amalgam (Au2Hg and Au3Hg) and liquid mercury by squeezing-through a piece of leather or a towel (usually through the shirt of the miner).

The production of gold takes place through heating of the amalgam lumps with about 50 - 60 wt. % Hg, 40 - 50 % Au which are wrapped in paper. The procedure is done in an open ceramic bowl using a blow lamp and in temperatures of 350-600%. The steamed mercury goes directly uinto the atmosphere; it accounts for about 50 - 60 % of the entire Hg emissions.

Researches of the author in Ecuador and Colombia have shown that retorts (see technical discussion 15.7) for Hg distillation in closed cycles are known and usually available but are rarely applied. The main reason behind this is the discoloration of the gold after distillation in the retorts- presumably as a result of Fe-compounds-, and consequently a lesser valuation of the product by small-scale miners. It is to be determined to what extent technical improvements could encourage acceptance of distillation retorts.

In some cases, especially when mercury supply is short, a fresh banana leaf placed on top of a vaporising dish or basin can serve to the partial recovery of mercury. Mercury condenses on the surface of the leaf.

D.6.5.4 WAYS OF MINIMIZING RELEASE OF MERCURY DURING AMALGAMATION

As described above, the emission of mercury takes place in metallic form during amalgamation as well as in the form of steam through the separation of the amalgam in mercury and gold. This section discusses ways of avoiding both of these sources of contamination.

Metallic mercury is produced in the amalgamation devices almost exclusively as crushed mercury in the form of tiny pearls, referred to as "floured mercury". The surface of these tiny globules are usually inactive due to impurities (among others, very fine mineral particles, fat and oil sediments from the water), other chemical transformations (for example, incrustations from antimony amalgam and the globules' inherent surface tension. This means that the globules can neither serve amalgamation nor fusion of gold and are discharged during high slurry speeds.

In vein ore mining, it is possible to avoid such loss of mercury. This is done through the separation of the simultaneous processes of amalgamation and grinding or comminution in pan grinders (as in Chile) or stamping mills (as in Ecuador and Colombia) using two procedural steps. The effect of high slurry speeds during amalgamation is avoided.

In alluvial gold deposit mining the use of mercury in trough washing, during which huge amounts of mercury is released in the environment, should be avoided. Instead, it is recommended in the two branches of mining to first produce the highest possible quality of pre-concentrate. Among the devices appropriate to wet mechanized gravity sorting using specifically high throughput are: fluid bed centrifugals, spiral separator, cone separator and fine grain separator with bedding, tables or improved sluices. Through post-concentration by means of precipitation of mineral by-products, for instance through magnetic separation, the pre-concentrates can be further improved.

Afterwards, the relatively small amounts of concentrate can be amalgamated in appropriate amalgamation installations such as in closed amalgamation barrels (referred to in Ecuador as "chancho") or in quick grinding mill (for example, Berdan pan). These devices also allow the addition of reagents for the improvement of the surface activity of mercury, for example (NaOH, nitrate amalgam, ammonium chloride, cyanide and nitric acid or tenside.

The least that can be done in plants in which a change in the course of the process is not possible would be planning post-activated sink angles to catch the "floured mercury".

To prevent the release of mercury steam, the "queimador" (the one which distills the amalgam) must distill only in close mercury cycle. Amalgam pressing and distillation retorts sink the mercury loss up to below 0.1% per distillation. Distillation retort must be user-friendly and hence, in their construction, care must be taken especially in the choice of materials and the cooling systems.

Alternatively, the amalgam can be chemically separated. In the process, the hot thinned or diluted nitric acid dissolves the mercury and gold slime comes off. From the resulting mercury nitrate solution mercury is again deposited with base metals. Ores containing silver, lead to a successive Ag-concentration in mercury which then necessitates distillation to purify.

Generally, it appears that the centralisation of amalgamation and/or distillation is to be advised. Miners can then further process pre-concentrates or amalgam in these central plants.

D.6.5.5 TECHNICAL ALTERNATIVES TO THE SUBSTITUTION OF AMALGAMATION

As alternative to amalgamation, there are available a number of methods of gold production or extraction. Most of these however have not gained currency in mining until today. Among these is the "gold-coal agglomeration" which was developed about 70 years ago but has not found application in beneficiation. Others such as cyanide leaching has extensively dispensed with amalgamation in large-scale mining. Due to complicated procedures, difficult control and the dependence on huge amounts of reagents etc., these alternatives are not rendered less appropriate for small-scale mining. Further development, technically, of the gravimetric beneficiation such as the sorting in centrifugal area, the increased utilization of vibration devices or equipment or the combination of gravity beneficiation with other physical processes correspond more to the requirement of small-scale mining. Such devices, for example, the Knelson centrifugal, allow the production of pre-concentrates with very high quality and whose final conversion into marketable products takes place in one last procedural step. This is the melting separation of gold pre-concentrates in gold and clinker using borax as fluxing agent, a process which the "mineros" usually do themselves.

D.7 The processing of phosphate-containing raw-minerals into p-fertilizers

Around 85% of phosphate fertilizers produced today come from phosphorites and sedimentary phosphate mineralizations which are comprised of fine mineral crystallises. For application in developing countries, the simplest fertilizer processing methods are most appropriate for meeting the needs of small-scale mining. A direct feed of raw mineral is frequently not practical due to the relatively low solubility of untreated phosphorites. This can be alleviated by performing a short activation grinding, which dissociates the mineral bonds and consequently increases the specific surface area, and also fractures the crystallite structure which significantly increases the weatherability and therefore the solubility of these minerals.

The other important raw material from which phosphate fertilizers are produced is apatite. This mineral is even less soluble than phosphorite, so that a direct application of apatite onto cultivated fields exhibits a fertilizing effect only after a period of 10- 15 years. In small-scale mining in Zambia, the apatite raw-ore with about 10 - 20 % POx content, is currently being processed by having it react with sulfuric acid which produces a readily soluble mineral fertilizer. Small processing plants, with capacities of up to 2t/d, employ cement mixers as reaction tanks for the treatment with sulfuric acid.


Fig.: Impact and circulation of mercury into the ecosystem by small-scale mining.

CLOSE THIS BOOKTools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)
Technical Chapter 12: Crushing
VIEW THE DOCUMENT(introduction...)
VIEW THE DOCUMENT12.1 Jaw crusher, jaw breaker
VIEW THE DOCUMENT12.2 Roll crusher, roll grinder
VIEW THE DOCUMENT12.3 Ball mill
VIEW THE DOCUMENT12.4 Stamp mill, hammer mill
VIEW THE DOCUMENT12.5 Chilean mill edge mill, roller mill
VIEW THE DOCUMENT12.6 ''See-saw'' crusher, ''rocker'' crusher

Tools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)

Technical Chapter 12: Crushing

BENEFICATION TECHNIQUES

12.1 Jaw crusher, jaw breaker

Mining General (Ore, Coal, Sand and Gravel)
Beneficiation, Crushing

germ.:

Backenbrecher, Knackwerk

span.:

chancadora de mandibulas, trituradora de mandibulas

Manufacturer:

Millan, Volcan, Denver Peru, Denver USA, FUNSA, MAFUQUI, Alquexco, Eq. Ind. Astecnia, IAA, INCOMAQ, COMESA, FAHENA, FIMA, Fund. Callao, H.M., MAGENSA, MAEPSA, Met. Callao E.P.S., Met. Mec. Soriano, Talleres Mejia, ASEA, FAMESA, MEPSA

TECHNICAL DATA:

Dimensions:

approx. 0.7 × 0.7 × 1.5 m minimum

Weight:

approx. 350 kg minimum

Extent of Mechanization:

fully mechanized

Power Required:

3 - 10 kW for <=2 t/h

Form of Driving Energy:

electric, diesel or gasoline driven internal combustion engine

Alternative forms:

very successful with turbine drive and transmission

Mode of Operation:

continuous

Throughput/Capacity:

from 350 kg/h

ECONOMIC DATA:

Investment Costs:

between 1000 US$ (350 kg/h) and 4000 US$ (1.5 t/h) for Bolivian production; etween 4000 US$ (1 t/h) and 18.000 US$ (2 t/h) for imported crusher cif La Paz

Operating Costs:

personnel wages, energy costs and minimal repair costs; cost of replacing jaws when worm

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Personnel Requirements:

low

Grain Size Material:

depends on type of crusher: here < 20 cm 0

Output:

crushing ratio of 5: 1 to 10: 1; smallest final grain size approx. 5 - 10 mm; only compressive loading: maximum grain size of feed up to 1,000 mm; crushed product approx. 100 mm (main area of application)

Replace other Equipment:

stamp mill

Regional Distribution:

worldwide

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high


noise and dust pollution

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

local machine manufacturing

Lifespan:

very long |————|————| very short

Bibliography, Source: Taggert, Schubert, v. Bernewitz, Priester, Gerth, DBM, Callon, Althaus

OPERATING PRINCIPLE:

The Jaw crusher crushes the raw-ore feed by pressing it between two jaws, one fixed and one moveable, in a wedge-shaped crushing chamber. The moving Jaw pivots around its upper (feed side) axis. At its lower end, the Jaw is moved via an eccentrically-driven toggle system, which in turn increases or decreases the volume of the crushing chamber. During the decreasing stroke, the ore becomes broken, and subsequently slides deeper into the chamber as the Jaws open again, expanding the crushing chamber; this process repeats itself until the final grain size is reached, whereby the crushed ore falls out of the chamber through a slit at the bottom.

AREAS OF APPLICATION:

Pre-crushing and crushing of raw ore.

REMARKS:

Can successfully be mechanizing with turbines, whereby the starting torque of turbines has an advantageous effect, for example if the crusher is clogged; in this case, the power can be adjusted significantly lower than with electric power units.

Raw ore should first be screened µ® reduced feed quantities, lower energy costs.

The wear on the crushing Jaws depends greatly on the tenacity (toughness) of the feed material; sufidic ores rich in quartz, for example, can wear out a set of crushing jaws after only 30.000 t, galena-sphalerite ores in graywacke after approx. 60.000 t and carbonate iron-ores first after around 300.000 t (Gerth, et. al.).

Fine Jaw crushers have wider jaws and operate at higher rpms, with one jaw frequently being of concave construction so that the crushing chamber tapers down in almost parallel flanks, thereby minimizing the occurrence of fines.

Wear-resistant coating of crushing jaws with welding material (see 11.1) leads to an extended lifespan.

SUITABILITY FOR SMALL-SCALE MINING:

Jaw crushers are the most simply-constructed apparatuses for coarse preliminary crushing, and can also be locally produced in developing countries. The application of jaw crushers can significantly improve the efficiency of beneficiation operations.


Fig.: Operating principle of the single-jaw crusher. Source: Ullmann. a) crushing jaw c) supporting plate d) fixed plate B: eccentric pivot C: supporting-plate bearing.


Fig.: Jaw crusher. Source: Armstrong.


Fig.: Jaw crusher. Source: Gerth.


Fig.: Detailed diagram of a jaw crusher. Source: Bernewitz.

12.2 Roll crusher, roll grinder

Mining General (Ore, Sand and Gravel)
Beneficiation, Crushing

germ.:

Walzenbrecher, Walzwerk, Walzenmuhlen

span.:

trituradora de rodillos, chancadora de rodillos, molino de discos, laminador, molino de rodillos

Manufacturer:

Millan, Volcan, Denver

TECHNICAL DATA:

Dimensions:

approx. 0.7 × 0.7 × 1.5 m, roller die 25 cm or more

Weight:

approx. 350 kg

Extent of Mechanization:

fully mechanized

Power Required:

starting at approx: 5 kW

Form of Driving Energy:

electric motor, internal combustion engine

Alternative Forms:

possibly hydromechanic

Mode of Operation:

continuous

Throughput/Capacity:

approx. 700 kg/in

Technical Efficiency:

degree of comminution between 3:1 and 4:1

ECONOMIC DATA:

Investment Costs:

Denver mill, 2 t/h: 18.900 US $, Volcan mill, 500 kg/h: 5000 US $, Millan mill approx. 6500 DM including motor fob La Paz

Operating Costs:

labor costs, energy costs, minimal wear

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Personnel Requirements:

low

Grain Size:

> 20 - 25 mm (max. 100 mm)

Output:

100 % < 1.5 mm with especially homogeneous grain-size distribution

Replaces other Equipment:

other mills

Regional Distribution:

rare

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high


especially dust and noise pollution

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

metal manufacturer for steel

Lifespan:

very long |————————| very short

Bibliography, Source: Priester, Schennen, Treptow, Gerth, Callon, Schubert

OPERATING PRINCIPLE:

The feed material is crushed between two counter-clockwise rotating rollers to a degree of fineness allowing it to fall through a slit at the bottom. In the event that the pressure becomes too great, the rollers deflect outwardly, increasing the gap between them and consequently also the final grain size.

AREAS OF APPLICATION:

Crushing of brittle ore in preparation of hydromechanic gravimetric sorting of medium-sized grain fractions.

REMARKS:

Roll crushers are known for producing a ground product with a very low proportion of fines.

30 - 200 g of hard-steel wear per ton throughput depending on hardness and tenacity of the feed material.

The roll crushing of hard minerals (igneous rocks, hard ores, gravel sediments) uses smooth Jaws, whereas the rollers for crushing medium hard or soft material (e.g. Iimestone, anhydrite, sedimentary Iron ores, etc. or salts, clays, soft brown coal, etc.) are fluted or serrated.

The roller diameters should equal approx. 20 times that of that largest grain-size contained in the feed.

SUITABILITY FOR SMALL-SCALE MINING:

Roller mills are suitable machines for fine crushing, which leads to extreme exposure of the feed in case of somewhat coarse intergrown ore avoiding further fine milling.


Fig.: Roll crusher. Source: Gerth. Above: side view; Below: plan view.


Fig.: Plan diagram of a roll crusher with swinging rollers. Source: Schennen.


Fig.: Roll crusher. Source: Treptow. Above: side view, Below: plan view.

12.3 Ball mill

Mining General (Ore, Sand and Gravel)
Beneficiation, Crushing

engl.:

ball crusher, manual ball mill

germ.:

Kugelmuhle, Handkugelmuhle

span.:

molino de boles, molino de boles a mano

Manufacturer:

Millan, KHD, Volcan, Denver, Alquexco, Eq. Ind. Astecnia, IAA, Talleres Mejia, Buena Fortuna, COMESA, Met. Mec. Soriano, FAMESA, FAHENA, FIMA, FUnd. Callao, H.M., MAGENSA, MAEPSA, Met. Callao E.P.S.

TECHNICAL DATA:

Dimensions:

approx. 1.5 × 1 × 1 m

Weight:

approx. 150 kg

Extent of Mechanization:

manual to fully mechanized, depending on drive system

Power Required:

from 100 W up to several kW, e.g. approx. 7.5 kWh/t energy input to crush Volcanic sulfide ores, up to 50 kWh/t energy consumption for milling of hard quartzite and similar ores

Form of Driving Energy:

electric

Alternative forms:

manual, pedal drive, hydromechanic with water wheel

Mode of Operation:

semi-continuous/continuous

Throughput/Capacity:

1 t/h: 11 - 12 kW

Operating Materials:


Type:

Water grinding bodies (Zylpebs or balls)

Quantity:

bulk-volume approx. 25 - 45 % of mill capacity

ECONOMIC DATA:

Investment Costs:

manual ball mill: approx. 1000 DM when locally produced; Millan mill 500 US$,

Volcan mill:

10.000 US$, Denver mill: 22.000 US$ for mills with approx. 1 t/h throughput

Operating Costs:

replacement of worn milling balls, energy costs

Related Costs:

possibly thickener, since ground product is a slurry

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Personnel Requirements:

low

Location Requirements:

water availability is the only requirement

Grain Size:

approx. < 30 mm

Replaces other Equipment:

see-saw (rocker) crusher for fine crushing

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

small ball mills can be produced locally in good metal-manufacturing workshops, for example in the Philippines, where ball mills are being produced entirely locally.

Lifespan:

very long |————|————| very short

Bibliography, Source: Museum case de la Moneda, Potosi, Ullman, Schubert, Taggert, Stewart

OPERATING PRINCIPLE:

Manual hand-cranked ball mills with spiral feed chute are used for fine grinding. The ball mill is a rotating cylindrical crushing device which contains steel balls which comminute the material through percussive, shearing and compressive (squeezing) forces. Rotating the drum results in a continuous cascading of the balls and material contained inside. The duration of milling is determined by the final grain-size desired for the ground product. Water flowing through the mill removes the fine material.

AREAS OF APPLICATION:

Fine grinding of middlings, raw ores or pre-concentrates.

SPECIAL AREAS OF APPLICATION:

For special grinding steps where it is important that the products remain free of iron, such as in grinding of graphite, hard stones of flint, granite, etc. are used instead of the balls.

REMARKS:

In autogenous grinding, only the feed material itself, in the absence of balls or other grinding bodies, is subjected to the rotation of the mill drum. The grinding is achieved as a result of the larger material grains functioning as the balls, crushing the smaller or softer feed components. An example where autogenous grinding is applied is in the liberation of loosely-consolidated gold-containing conglomerates.

All types of ball mills produce high proportions of fine-grained product. In the case of particularly brittle minerals such as scheelite, wolframite, cassiterite, sphalerite, etc., this readily leads to overgrinding, resulting in poor recovery of the valuable mineral. Under these conditions, grinding needs to be performed with care, including prescreening and intermediate screening of the fines, and recycling of the screened overs back into the mill.

When the ground product is discharged from the mill as a slurry, the heavy material components remain in the mill longer due to their increased resistance to the flow forces. Consequently, grinding must be conducted correspondingly carefully, or an alternative method of removing the ground product from the mill must be employed, such as screening.

CONSTRUCTION INFORMATION:

Wheel bearings from cars are suitable as bearings for hand-cranked ball mills.

With belt or chain-driven systems, the entire mill housing is rotated.

The optimal rotational speed (rpm) is 75 % that of the critical rotational speed, or that where the centrifugal force causes the mill balls to remain on the drum perimeter:


n in min-1
D = mill diameter in m

For this rotational speed, at 30 % degree of filling, the power can be determined by the following formula

P (kW) ~ 10 GK (t) × V D (m), where GK is weight of balls in 1000 kg

For 20 % degree of filling the power is about 10 % higher, and for 40 % degree of filling about 15 % lower.

The rotational speeds for coarse grinding lie somewhat higher than for fine grinding, to a maximum of

D diameter of ball mill <= D/20

Old rail sections, cemented Into place, provide an inexpensive ball-mill lining.

The ends of the mill housing can be placed on roller or ball bearings, or on other forms of rollers or tires, the latter form can also be used to drive the mill, allowing good access to the front and back ends of the mill for easier handling at the feed and discharge points.

SUITABILITY FOR SMALL-SCALE MINING:

Hand-cranked ball mills have a rather limited application due to their low throughput. Useful primarily for regrinding of middlings. Small mechanized ball mills are appropriate in small-scale mining operations where finely-intergrown ore requires a fine liberation grinding, in which case a good supply of replacement parts must be available.


Fig.: Mill lining of old rails cemented to the drum. Source: Stewart.


Fig.: Schematic diagram of a ball mill. Source: Armstrong.

12.4 Stamp mill, hammer mill

Metal Mining (gold ores, tenacious ores)
Beneficiation, Comminution

germ.:

Pochwerk, Hammerwerk

span.:

bocarte, bateria de pisones, molino antioqueno, molino caiforniano, mortero (K.)

TECHNICAL DATA:

Dimensions:

approx. 4 × 2 × 1 m; 400 - 700 mm-deep die (box) in wet stamp mill, depending on final grain size (approx. 1 mm)

Weight:

several tons; stamp piston about 150 kg

Extent of Mechanization:

fully mechanized

Power Required:

depending on size, up to 10 kW

Form of Driving Energy:

mechanical, driven by hydropower or internal combustion engine; approx. 300 mm lift; approx. 60 stamps/mini approx. 0.6 PS/ stamp

Mode of Operation:

intermittent/semi-continuous/continuous

Throughput/Capacity:

approx. 0.8 - 2.5 t / 24 hrs / stamp

Operating Materials:


Type:

water for wet stamping

Quantity:

0.4 - 0.8 ft³/min. stamp

ECONOMIC DATA:

Investment Costs:

steel stamp mills approx. 10.000 DM including motor (in Colombia); wooden stamp mills approx. 1000 DM for a three-piston stamp mill of wooden-construction, and an additional 100 DM per stamp shoe. Wooden stamp mills are much cheaper, since the raw materials are generally less expensive and the mill easier to construct.

Operating Costs:

depends on mechanization

Related Costs:

drive system; e.g. approx. 1300 DM for wooden water wheel in Columbia

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Location Requirements:

water availability

Grain Size:

< 100 mm

Output:

high degree of crushing; final grain sizes < 2 mm

Replaces other Equipment:

crushers, other mills, Chilean (edge) mill

Regional Distribution:

historically widely distributed, today rather rare; used in Asia for Au and rice!, in Brazil, Ecuador and Colombia for processing gold ores; pedal-driven lever stamp mill used on harvested crops (e.g. in Nepal for threshing rice), historically used in Japanese gold mining (tail hammers).

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high


with wooden stamp mills dust pollution, otherwise primarily noise pollution; for the construction of wooden stamp mills, wood consumption, which, however, is relatively negligible, since the wood is cut and formed on-site without much excess waste, and the life span of wooden stamp mills is quite long. The energy consumed during casting of steel stamp mills is much more environmentally deterimental.

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

for steel stamp mills: good metal manufacturers, possible production of stamps from old rails; for wooden stamp mills: carpenters, frequently working directly on-site; stamp shoes produced in metal foundries.

Lifespan:

very long |————|————| very short


wear almost exclusively limited to stamp shoe

Bibliography, Source: Treptow, Priester, Agricola, Calvor, Wagenbreth, Schennen, Reitmeier, Villefosse, Gaetzschmann, Rittinger, Cancrinus, de Hennezel, Diderot, Callon, Treptow/Sado, Clennell, DBM, Uslar, Kirschner.

OPERATING PRINCIPLE:

The stamp is raised by means of a camshaft and falls down, under its own weight, onto the stamp dle. The mill is constructed with a higher wall at the intake side to accommodate the feed input. The discharge side is equipped with slots, screens or weirs. The stamp die, where the crushing occurs underneath the stamp, is constructed of very hard material or of a sufficiently-thick layer of coarse material. In the recommended wet stamp milling, stamping is performed under water and the final ground product is flushed out by a supplementary stream of water. Multiple-stamp mills usually consist of four to six stamps.

AREAS OF APPLICATION:

For wet or dry crushing of coarse metalliferous ores.

SPECIAL AREAS OF APPLICATION:

For crushing and amalgamation of Au-ores (tray amalgamation).

REMARKS:

Sn, W, and other brittle ores are subject to overgrinding due to the high peak impact forces. For this reason, the use of the stamp mill in metal mining, except for gold ores, has been replaced by crushers.

Invented as a single-stamp dry stamp mill by Heinrich dem Jungerer (Henry the Younger, 1489 - 1568) in the Harz mining region of Germany.

Designed also as a tail hammer, front stamp, helve hammer etc.; this design with horizontally moving stamps is suitable for water-powered drive systems such as water levers or "Gnepfe", which are water see-saws equipped with a slowly-filling container at one end to raise the counterweight at the other end, whereby the water container abruptly empties Itself again.

Stamp mill drive-systems have traditionally almost always been hydromechanic, employing water wheels; exceptions were steam-operated mills.

The stamp shoe and stamp stem should always be independently constructed to permit easy replacement of worn shoes. However, the joint between the stem and the shoe must be rigid to prevent slippage and a resulting drop in efficiency.

Wooden stamp dies should be protected against wear by leaving a layer of already-crushed material in the die to buffer it from newly-added coarse feed; mills operated under these conditions then exhibit wear-resistant characteristics similar to steel stamps.

Of importance in the crushing process is the stamping frequency too low a frequency leads to sedimentation of the fine material and consequently a very fine milling with low throughput. Optimal stamp frequencies are in the range of approx. 30 min-1 for fine milling up to approx. 90 min-1 for coarse milling.

For stamp-mill processing in gold mine operations, it is important that the slurry does not contain any oil or grease, and therefore it is absolutely necessary to prevent lubricants from dripping into the stamp die. The presence of lubricants in the slurry causes immediate flotation of the fine gold in the successive separation processes.

In gold mining in Ghana and Ecuador, locally-produced mortars are used for manually-operated impact or stamp crushers. As stampers, car axles or axle stumps constructed of high-tensile steel can be used. The local name In Ecuador for these is "porron".

Fundamentally, the throughput of stamp mills is relatively low. Therefore, mechanized gold mines have chosen to replace them with crushers for coarse-crushing steps, and with Chilean (edge) mills for finer grinding requirements.

For use in gold mining, the stamp mill is equipped with a screen (e.g. in Colombia with perforated rubber, zarandas) on the discharge side, and with mercury, or even better silver-amalgamated replaceable copper plates, on the feed-intake side.

Coarse heavy material is often concentrated in the stamp die.

OPERATING EXPERIENCE:

In the Andean gold mining region of Colombia, locally-manufactured stamp mills are the most widely used crushers. These wooden stamp mills, made of chachajo-wood, are generally driven by primitive, overshot water wheels. The three to four catchers per stamp are located directly on the axis of the water wheel. Mills with between three and five stamps are in use. The time required to construct such a mill totals about three weeks for the complete installation. The stamp shoes are made of iron and are replaced approximately every 6 months; the bearings are predominantly slide bearings. Iron stamp mills can be purchased from local machine manufacturers, and are usually powered by diesel engines and a system of belts or chains. The catcher-equipped axle rests on rollers or ball bearings.

To avoid flotation caused by dissolved lubricants, the Colombian miner grinds pieces of sisal leaves (cabuya, fique, lat.: Fourcraea macrophylla Baker) in with the feed material (see Technique 15.2).

SUITABILITY FOR SMALL-SCALE MINING:

When stamp mills can be manufactured at low cost, and a hydromechanical, slow-moving direct drive system is available, they are advantageous compared to other, turbo-driven crushers (jaw crusher, roll crusher). Stamp mills are especially suitable for the grinding of tenacious gold ores.

Wooden stamp mill with three stamps and open stamp die, easily visible are the Inset iron stamp shoes, and above them the water wheel axle with catchers for driving the stamps. In the foreground, a blanket sluice with blanket-cover removed; La Llanada' Narino, Colombia

Iron stamp mill with drive-belt gear transmission from a diesel engine. At stamp mill discharge side, the perforated rubber strips serving as screens. In foreground, blanket sluice for gold sorting. La Llanada, Narino, Colombia.


Fig.: Functional diagram of a stamp mill. Source: Wagenbreth.

Wooden stamp mill with three stamps and open stamp die; easily visible are the insert iron stamp shoes, and above them the water-wheel axle with catchers for driving the stamps. In the foreground, a blanket sluice with blanket-cover removed; La Llanada, Narino, Colombia.


Fig.: Water-wheel-driven dry stamp mill. Source: Schennen.

Iron stamp mill with drive-belt gear transmission from a diesel engine. At stamp mill discharge side, the perforated rubber strips serving as screens. In foregound, blanket sluice for gold sorting. la Llanada, Narino, Colombia.


Fig.: Discharge installations in wet stamp mill. Source: Treptow.

Manual stamping mortar (porron) for crushing of rich gold ores in Guaysimi, Ecuador.
Left: discharge over the wall, middle: discharge throught a slit, right: discharge throught piston (stamp) displacement.


Fig.: Californian stamp mill with trimmed set of screens. Source: Treptow.


Fig.: Wet stamp mill. Source: Agricola.


Fig.: Wet stamp mill. Source: Schennen.


Fig.: Hammer mills. Source: Eckholdt.

a=AXLE, b=CATCHERS, c=STAMP LEVER JOINT, d=STAMP LEVEL JOINT HOLDER, e=STAMP LEVER, f=STAMP, g=ANVIL, h=OVERHEAD STABILIZER


Fig.: Tail hammer. Source: Cangrinus.

12.5 Chilean mill edge mill, roller mill

Ore Mining (Gold Ore, Sand and Gravel (colored clays))
Beneficiation Crushing

germ.:

Kollergang, Rollquetsche

span.:

trapiche, molino de muelas, molino chileno, milling track: solera, wheel casing: Llanta

Manufacturer:

Millan, Volcan/both in La Paz, Bolivia, Talleres J.G.

TECHNICAL DATA:

Dimensions:

approx. 2 × 2 × 2 m HWD + drive

Weight:

> 1000 kg

Extent of Mechanization:

fully mechanized

Power required:

5 - 7 kW + 15 kW starting motor

Form of Driving Energy:

electric

Alternative forms:

hydromechanic, animal-powered whim

Mode of Operation:

continuous

Throughput/Capacity:

approx. 1000 kg/in

Operating Materials:


Type:

water

ECONOMIC DATA

Investnment Costs:

approx. 5000 to 6000 DM (locally produced in Bolivia)

Operating Costs:

depends on type of drive system

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Personnel Requirements:

low

Gain Size:

up to 20 mm

Special Feed Requirements:

even hard abrasive feed materials can be crushed

Output:

very high degree of crushing; very fine ultimate grain size

Replaces other Equipment:

ball mills, amalgamating mills, stamp mills

Regional Distribution:

Chile, Ecuador, Bolivia; earlier worldwide, today mainly in agriculture for milling of oil producing fruits (oil mill)

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high


high when combined with amalgamation, otherwise low

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

metal manufacturers, foundry

Lifespan:

very long |————|————| very short

Bibliography, Source: Priester, v. Bernewitz, Gerth, Schennen, Schabel, Diderot,Gaetzschmann, Treptow

ECONOMIC DATA:

Investment Costs:

approx. 5000 to 6000 DM (locally produced in Bolivia)

Operating Costs:

depends on type of drive system

OPERATING PRINCIPLE:

The Chilean (edge) mill is a typical crusher used in gold beneficiation of primary gold-quartz veins. Two steel-rimmed concrete wheels, frequently weighing more than half a ton, roll around a circular milling track and grind the ore underneath them, yielding fine to very fine grain-sized products due to the high degree of crushing forces exerted. The final grain size is determined by the length of time the mineral is crushed or by the velocity of the water flowing through the mill.

AREAS OF APPLICATION:

For fine grinding and pulverizing. For grinding and amalgamation of Au-ore.

REMARKS:

The real advantage of the edge (Chilean) mill in ore beneficiation lies in its ability to simultaneously grind and amalgamate gold ore, whereby fine gold is kneaded into the mercury so that the amalgam is reached by fine gold particles, which would not otherwise be amalgamated without the kneading due to the mercury's high surface tension. At the same time, the surfaces of liberated gold particles are cleanest during milling, not yet becoming corroded again.

The extremely heavy weight of the wheels poses difficulties in overcoming intertia during the start-up phase, possibly requiring a stronger starting motor. The outer axle stump is sometimes supported by a chain in order to minimize the high lifting forces that occur.

In northern Chilean gold mining, when the grinding operation includes a simultaneous amalgamation, the cone-shaped rim of the grinding track is sometimes covered with copper plates to serve as an amalgamation table. This aids in the binding of finely-distributed "floured mercury".

In general, the Hg-losses during amalgamation in Chilean mills are somewhat high. The finely crushed, flushed-out mercury and amalgam require subsequent removal by gravimetric secondary separation, for example in a hydraulic trap.

In gold mining in Ecuador, copper plates for amalgamation directly suceed the Chilean mill in the beneficiation procedure.

SUITABILITY FOR SMALL-SCALE MINING:

Especially for small-scale gold mining, edge (Chilean) milling with simultaneous amalgamation is very suitable, provided that environmental damage is avoided. For other forms of ore mining, this system is suitable only in limited situations, such as for very finely intergrown ores. For all other types of feed material, the occurence of larger proportions of fines poses difficulties.


Fig.: Molino de arrastre, an early form of the edge (Chilean) mill. Source: Ulsar. Left: side view, Right: top view.


Fig.: Diagram of an edge (Chilean) mill. Source: Bernewitz.


Fig.: Early type of Chilean mill as roller mill with animal-powered whim. Source: Schennen. Left: side view, Right: top view.


Fig.: Edge (Chilean mill. Source: Schanabel.


Fig.: Construnction diagrams of an edge (Chilean) mill produced in Bolivia. Source: Priester.

12.6 ''See-saw'' crusher, ''rocker'' crusher

re Mining (Gold Ore, Sand and Gravel (colored clays))
Beneficiation, Crushing

germ.:

Wiegezerkleinerer

span.:

quimbalete, maray

TECHNICAL DATA:

Dimensions:

approx. 1.5 × 1 × 2 m HWD

Weight:

up to >= 2 t

Extent of Mechanization:

not mechanized

Form of Driving Energy:

manual

Alternative forms:

in Peru partly hydromechanic with water wheel

Mode of Operation:

semi-continuous

Throughput/Capacity:

0.7 - 1.5 kg/M × min

ECONOMIC DATA:

Investment Costs:

nominal since usually self-constructed

Operating Cost:

Iabor costs only

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Grain Size:

up to approx. 5 - 10 cm

Output:

degree of crushing very high, depending on duration of milling: normally 1: 5 to 1:20; final grain-size depending on mill design, of up to 100 % < 100 ym, homogeneous grain distribution in ground product

Replaces other Equipment:

mills, Chilean mills, stamp mills

Regional Distribution:

Bolivia, Peru, Chile, Honduras, Philippines

Operating Experience:

very good |————|————| bad


disregarding the work-intensity involved with the technique, very good

Environmental Impact:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

see-saw crusher made of hard rock material (granite, gneiss, etc.) or welded together from scrap Iron, possibly filled with stones or concrete, on a steel or stone plate, are primarily locally produced

Lifespan:

very long |————|————| very short


practically no wear

Bibliography, Source: Priester, Latin America Seminar Hannover, Ahlfeld, Hentschel, Rittinger

OPERATING PRINCIPLE:

Very heavy stone or steel see-saw or rocker crushers are rolled, with the help of a lever arm, over the material to be ground, which is placed on a stone or steel surface. This method of crushing is comparable to that of roll crushers. Through a slight rotation at the dead-canter lever-arm position, the wheels can be repositioned on the grinding surface.

AREAS OF APPLICATION:

Grinding of coarse to medium-grained ores as part of the beneficiation process. Many mining operations crush exclusively with see-saw or rocker crushers.

SPECIAL AREAS OF APPLICATION:

Concave circular stampers are used for fine-crushing/recrushing of fine-grained middlings (see photo opposite).

REMARKS:

Even hard abrasive material can be processed; the wear on the see-saw or rocker crusher remains very low, however the great physical effort required for the hand-crushing of this material poses difficulties. In gold mining in North-Peru, these crushers are sometimes driven by water wheels.

A well-formed grinding surface makes the crushing process significantly easier. The geometric center should be above the mass center.

See-saw or rocker crushing can be performed either as a wet or a dry process, whereby wet crushing produces a more homogeneous product with fewer fines and also minimizes the occurrence of airborne silicate dusts.

Wet crushing could possibly be performed in troughs or sluices, with the fine grains being carried out in the water flow.

According to Rittinger, very hard quartz-ores are sometimes burned prior to crushing in order to shatter the crystals. This in turn reduces the required output in the crushing step by approx. 15%.

In northern Chilean gold mines, poured-concrete milling wheels called "marajes", which run in concrete or stone troughs and are moved by the use of branches or two simple wooden levers, are employed for wet crushing and amalgamation.

SUITABILITY FOR SMALL-SCALE MINING:

As a traditional and widely-used crushing apparatus in Latin American small-scale mining, the see-saw or rocker crusher can still be employed today whenever the quantity of feed material is low, such as for secondary grinding of middlings. Despite its being a highly work-intensive technique, the see-saw crusher is the most effective of the non-mechanized crushing processes.

CLOSE THIS BOOKTools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)
Technical Chapter 13: Classification
VIEW THE DOCUMENT13.1 Set of rigid screens
VIEW THE DOCUMENT13.2 Screen riddle, vibrating screen
VIEW THE DOCUMENT13.3 Cantilever grizzly
VIEW THE DOCUMENT13.4 Sizing drum, classifying drum
VIEW THE DOCUMENT13.5 Cone classifier
VIEW THE DOCUMENT13.6 Countercurrent hydraulic classifier
VIEW THE DOCUMENT13.7 Hydro-cyclone
VIEW THE DOCUMENT13.8 Log washer, spiral classifier
VIEW THE DOCUMENT13.9 Rake classifier
VIEW THE DOCUMENT13.10 Sluice, sluice box, washing sluice

Tools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)

Technical Chapter 13: Classification

13.1 Set of rigid screens

Mining General
Beneficiation, Classification

engl.:

screening gate, grizzly

germ.:

Siebklassierung in starren Sieben, Durchwurf, Reibgatter

span.:

clasificacion en tamices fijos, clasificacion por tamano en tamiz

TECHNICAL DATA:

Dimensions:

starting at 30 × 40 cm screen area for single screen, up to 2 × 2 m for coarse screens (grizzly)

Weight:

starting at 5 kg per screen

Extent of Mechanization:

not mechanized

Form of Driving Energy:

manual feeding, possible manual drawing as well

Mode of Operation:

semi-continuous

Throughput/Capacity:

very dependent on grain-size of feed

Operating Materials:


Type:

water for wet screening

ECONOMIC DATA:

Investment Costs:

example: for three screens 300 DM

Operating Costs:

labor costs only

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Location Requirements:

water availability

Grain Size:

100 ym up to several decimeters separation cut-off size (screen openings)

Special Feed Characteristics:

no clay-containing' sticky material

Replaces other Equipment:

other classifiers

Regional Distribution:

worldwide

Operating Experience:

very good |————|————|bad

Environmental Impact:

low |————|————|very high

Suitability for Local Production:

very good |———|————|bad

Under What Conditions:

frames are very suitable for local production by carpentry or metal workshops; screens are generally imported since they are subject to extreme abrasive forces and must therefore be constructed of high-quality material.

Lifespan:

very long |————|————| very short

Bibliography, Source: Stout, Schennen, Stewart, Priester, Reitemeier, Villefosse, Gaetzschmann, Cancrinus

OPERATING PRINCIPLE:

Screen classification with rigid (stationary) screens can be performed either wet or dry. Dry screening is applied for dry coarse-grained material and occurs in an inclined screen. Wet classification is conducted in "screening gates", or a series of successive stationary screens built into a sluice or trough, sequentially going from coarser to finer screen openings from the top (feed end) to the bottom (discharge end) of the trough. The screened unders are transferred to the next (one degree finer) screen via the processing water.

AREAS OF APPLICATION:

For classifying material of coarse and medium granulation prior to its entering the main separation facility.

SPECIAL AREAS OF APPLICATION:

Selective classification of products from sorting and comminution processes.

REMARKS:

The dry screening process with the inclined screen is disadvantageous in that it has a low separation precision as a result of undesired separation of adhesive grains.

Wet screening in rigid screens and distributing the material over the screen by means of a spatula leads to inhomogeneity in the slurry comprised of the screened unders. When the classification processes, which are sensitive to changes in the feed slurry, directly succeed the wet screening, then special equipment (such as pinched sluices) for homogenizing the slurry flow must be placed between these two steps. Screens were already being applied in antiquity in Greek mining. For acidic process water, it is absolutely necessary that the bottom of the screens be constructed of stainless steel or plastic. During wet screening, care should be taken to either catch the fines in sedimentation basins, or immediately separate them in sludge ponds, to avoid high losses of valuable minerals.

Grizzlys, used for coarse-material separation, should be installed with a minimum inclination of 25° - 30°, allowing the coarseest fractions to roll down the grid and be collected for subsequent crushing.

SUITABILITY FOR SMALL-SCALE MINING:

Wet screening is a low cost, simple, quick and precise alternative for sorting feed material of medium to coarse grain-size. Especially when only smaller quantities of feed require processing, a mechanized classification is not necessary.


Fig.: Screening gate or screened grid-washer for wet classification with rigid screens. Source: Schennen.


Fig.: Simple hand screen with sprinkling device. Source: Stewart.

Screening gate for wet classification of course-grained material. Clearly visible are the outles for the screened unders , wich then directly enter the next (finer) subsequent sorting step; Mina Candelaria, Sud lipez, Bolivia.


Fig.: rigid, fixed grate for separating out large boudles, made of rails. Source: Stout.

Wooden grizzly for separating coarse coal underneath an unloading ramp for end-loading mine cars; Colliery in Region Rio Checua, Cundinamarca, Columbia.

13.2 Screen riddle, vibrating screen

Mining General
Beneficiation, Classification

germ.:

Ruttelsiebe, Schwingsiebe, Ratter

span.:

criba vibradora, instalacion de tamices con movimiento circular

Manufacturer:

Schenk, Jost, Mogensen, Eduardo, INCOMEC, Milag, Met. Cancha, Volcan, Alquexco, Eq. Ind. Astecnia, IAA, INCOMAQ, COMESA, FAHENA, Telsmith, FIMA, FAMINCO, Famia, fund. Callao, H.M., MAGENSA, MAENSA, MAEPSA, Met. Callao E.P.S.

TECHNICAL DATA:

Dimensions:

from 30 × 40 cm upwards, 10° - 20° inclination, 80 - 100 min-1 vibrating or shaking frequency

Weight:

from approx. 50 kg up to several thousand kg

Extent of Mechanization:

fully mechanized

Power:

low, maximal 1 PS/m² screen area

Form of Driving Energy:

hydromechanic impact mechanisms, manual impact mechanisms

Alternative forms:

pedal drive

Mode of Operation:

continuous

Technical Efficiency:

comparably higher than that of rigid screens

Operating Materials:


Type:

water

Quantity:

60 - 80 % by volume of feed quantity

ECONOMIC DATA:

Investment Costs:

manual, starting at 100 DM per screen when locally produced

Operating Costs:

usually labor costs only, possibly energy costs

Related Costs:

drive system

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————————| high


depending upon degree of mechanization

Maintenance Expenditures:

low |————|————| high


the removal of adhesive (sticky) grains in the feed is necessary

Location Requirements:

water availability

Grain Size:

> 50,um up to < 50 mm

Replaces other Equipment:

rigid screens

Regional Distribution:

not known in semi-mechanized processes in small-scale mining in Latin America; only used for wet classification in Jig operations

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

wood and metal manufacturing shops

Lifespan:

very long |————|————| very short

Bibliography, Source: Calvor, Agricola, Fischer, Schennen-Jungst, Liwehr, Villefosse, Delius, Gaetzschmann, Rittinger, Cancrinus, de Hennezel, Gerth

OPERATING PRINCIPLE:

In contrast to rigid, fixed screens, the bottom of vibrating screens (screen riddles) oscillates either longitudinally or laterally, shaking the material on the bottom of the screen and enhancing the flow through the screen openings. This results in a separation between the oversized (screen overs) and undersized (screen unders) grain fractions.

AREAS OF APPLICATION:

Dry or wet classification of coarse, medium or fine-grained feed fractions.

REMARKS:

Deflection with vibrating screen 55 - 80 mm
Deflection with impact screen 25 - 55 mm

The space requirement for vibrating screens is much less than that for rigid screens. Colotten placed underneath the screens for catching the individual fractions allow the screens to be staggered vertically on top of each other.

Car springs can be used as shaking devices and buffers.

Optimal ratio of screen length to width is approx. 2.7: 1

SUITABILITY FOR SMALL-SCALE MINING:

Even slightly-mechanized forms of vibrating screens are preferable to rigid screens due to their higher efficiency, lower space and water requirements, and finer degree of separation.


Fig.: Manual shaking screen. Source: Cancrinus.


Fig.: Operating principle of a vibrating screen (left) and impact screen (right). Source: Treptow.


Fig.: Self-vibrating screens made of railroad rails which start swinging upon impact of the feed material. Source: ITDG.


Fig.: Multiple-step screen riddle. Source: Liwehr.


Fig.: Two-step impact screen. Source: Schennen.

13.3 Cantilever grizzly

Mining General (pit and quarry)
Beneficiation, Classification

germ.:

Antriebslose Schwingsiebe

span.:

criba vibradora sin fuerza motriz (parrilla)

Manufacturer:

Mogensen

TECHNICAL DATA:

Dimensions:

separable grain-size cut-off: 25 - 40 mm minimum, approx. 300 mm maximum

Weight:

from approx. 200 kg

Extent of Mechanization:

not mechanized

Form of Driving Energy:

uses impact of falling feed material to induce shaking

Alternative forms:

as vibro-sizer for material that is very difficult to screen, but then mechanized

Mode of Operation:

continuous

Throughput/Capacity:

> 100 t/h

ECONOMIC DATA:

Investment Costs:

minimum of 20.000 DM fob location of manufacture in Germany

Operating Costs:

very low

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Location Requirements:

none

Grain Size:

< 1000 mm

Output:

precise screening

Replaces other Equipment:

vibro-screens

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high

Suitability for Local Production:

very |————|————| good bad

Under What Conditions:

Mogensen holds a patent for its product "rod-sizer". Other forms of powerless self swinging screens can be locally constructed from old rails or by using old drilling rods.

Lifespan:

very long |————|————| very short

Bibliography, Source: Company's Information, Mogensen

OPERATING PRINCIPLE:

Screening occurs through the use of one-sided and divergently attached rods, inclined so as to allow the feed material to flow over the "grate". The impact of the material flowing over the grate causes the rods to swing, which in turn prevents the grate from becoming clogged.

AREAS OF APPLICATION:

Coarse screening prior to coarse crushing Screening of gold-containing conglomerates Screening of coarse coal Classification of construction material in industrial minerals (pit and quarry) operations

REMARKS:

For local production, old drilling rods are very suitable; they are inexpensive, very resistant to wear, highly elastic and available on the local market.

The lower separable grain-size limit lies around 50 - 100 mm.

SUITABILITY FOR SMALL-SCALE MINING:

For non-mechanized coarse-grain classification, the "rod-sizer" is very suitable for application in vein ore mining, In alluvial mining and in pit and quarry mining due to its high throughput and simple construction.


Fig.: Non-powered "rod-sizer" for coarse screening. Source: Mogensen company information.

13.4 Sizing drum, classifying drum

Mining of partly consolidated loose material
Beneficiation, Classification

germ.:

Klassiertrommel

span.:

tromel clasificador, criba rotativa

Manufacturer:

Milag, Met. Lacha, Alquexco, IAA, Buena Fortuna, FAHENA, FIMA, MAGENSA, MAEPSA, Met. Callao E.P.S.

TECHNICAL DATA:

Dimensions:

18 - 25 min-1 rpm, circumferential speed < 1 m/s, diameter 2 0.5 m, length 2 m for single drum with three sizing grades

Weight:

starting at approx. 100 kg for smaller types


Extent of Mechanization:

semi-mechanized

Driving Capacity:

starting at 0.5 kW

Form of Driving Energy:

hydromechanic

Alternative Forms:

internal combustion engine, electric drive, manual operation for small models

Mode of Operation:

continuous

Throughput/Capacity:

minimum 1 t/h;



for dry screening:

0.27 t/m²h per mm screen opening


for wet screening:

0.45 t/m²h per mm screen opening

Operating Materials:



Type:

water


ECONOMIC DATA:

Investment Costs:

starting at approx. 1500 DM

Operating Costs:

mainly energy costs

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Location Requirements:

water availability

Grain Size:

< 50 mm

Replaces other Equipment:

screens and vibrating screens

Regional Distribution:

locally applied in small-scale mining in Latin America

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

good-quality perforated plates or screens must be available on the national market

Lifespan:

very long |————|————| very short

Bibliography, Source: Gerth, Priester, Treptow, Fischer, Callon, Stifft, Schubert, Rittinger

OPERATING PRINCIPLE:

The sizing or classifying drum is a mechanized form of wet screening in which several screens or perforated plates (arranged finer to coarser from intake to discharge) are aligned so as to form a drum. The drum is rotated by an external belt-drive transmission. The material moves from finer to coarser screens, during which the undersized grains are discharged via cones and distributed to the various sorting devices, such as hand jigs or sludge ponds.

Water is sprayed after 100 to 120 degrees rotation (from deepest point) to clean the screens and improve material transport.

REMARKS:

The sizing drum is characterized by its highly synchronous operation. The throughput quantity greatly depends upon size of the screen openings, with coarser screens delivering a higher throughput. Double-shell or triple-shell screens require less electrical energy and water consumption, have higher throughput, and are subject to less wear. Reference has also been made to manually-driven classifying drums (Stifft).

Two different types are in operation:

- drums with cylindrical screens and inclined axis and
- drums with conical screen housings and horizontal axis

Angle of Inclination: 4° - 5°

Lifespan: with wet screening up to 20.000 t throughput; with dry screening up to 100.000 t.

The disadvantages of sizing drums are the comparably high energy consumption and low self-cleaning effect

To process tenacious, sticky or clay-containing materials, a preliminary sorting with a screenless drum-unit, equipped only with catchers, should be performed. In this unit, the material is precrushed autogenously.

Drums constructed without an axis also exist. Such drums must have a load-bearing housing which also enables the load to be carried on rollers (such as, for example, four car wheels), a construction which then permits a simpler drive-system design,

SUITABILITY FOR SMALL-SCALE MINING:

Sizing drums are most suited in small-scale mining for classification of coarse and medium-grained feed material. Advantages lie in the high throughput quantities, continuous mode of operation and low space requirements.


Fig.: Concentric multi-step drum with conical screens for easy screen replacement. Source: Treptow.


Figures

Fig.:Conical sizing drums, above with screen housing, below with concentric screens. Source: Fischer.
Fig.: Conical drum: longitudinal and cross-section views. Source: Treptow


Fig.: Double-shelled drum. Source: Gerth.


Fig.: Construction for inserting screen plates into a concentric drum. Source: Treptow.

13.5 Cone classifier

Mining General
Beneficiation, Classification

engl.:

box classifier, settling box

germ.:

Spitzkasten

span.:

clasificador de caja en punta, caja en punta

Manufacturer:

FIMA

TECHNICAL DATA:

Dimensions:

from about 1 × 0.8 × 2 m up to several m in width and over 10 m in length

Weight:

from approx. 40 kg

Extent of Mechanization:

not mechanized

Form of Driving Energy:

only processing-water current

Mode of Operation:

continuous

Operating Materials:


Type:

water

Quantity:

slurry with < 40 % by vol. solids

ECONOMIC DATA:

Investment Costs:

approx. 200 DM when locally produced

Operating Costs:

labor costs only

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Location Requirements:

water necessary

Grain Size:

fines up to 1 mm

Output:

Separates into several different grain-size fractions, for example a 3-chamber settling box into 3 distinct fractions plus fines. Settling-box classification leads to more precise separation results in later processes (concentrating tables, sludge ponds, chutes, etc.) than does screen classification.

Replaces other Equipment:

screen classification

Regional Distribution:

rare

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

simple carpentry workshop

Lifespan:

very long |————|————| very short

Bibliography, Source: Treptow, Quittkat, Priester, Callon

OPERATING PRINCIPLE:

A cone classifier or settling box is comprised of several settling chambers, in the form of inverse pyramids, with outlets at the bottom. The slurry-feed flows through this series of chambers, and depending upon the retention period, intake and discharge flow velocity, volume of the settling chamber, etc., specific grain fractions settle out onto the bottom of the chamber (according to the principle of equal settling velocites) and are removed. The remaining slurry flows into the succeeding basin, where the next finer fraction is separated via sedimentation.

AREAS OF APPLICATION:

Classification of medium and fine-grain feed material for subsequent processing in hydromechanic gravimetric separating facilities.

REMARKS:

- lost fines can be avoided by the use of a back (underscreen) water flow (settling boxes with clean water countercurrent)
- the walls have > 50° inclination
- Rittinger provides the following dimensioning and calculation guidelines:

Per m³ slurry input per minute, the following dimension relationships for single chambers are applicable:

Slurry flow should be approx. 45 l per minute and m water surface.

No.

width

length

� discharged material

1

1 m

2 m

40 % of the weight

2

2 m

3 m

20 % of the weight

3

3 m

4 m

18 % of the weight

4

4 m

5 m

10 % of the weight

in sludge overflow 4 %

SUITABILITY FOR SMALL-SCALE MINING:

As non-powered fine-grain classifiers, settling boxes (cone classifiers) are very suitable for small-scale mining beneficiation of fine material due to their sturdy construction, continuous mode of operation and low investment costs.


Fig.: Wooden cone classifier (settling box). Source: Priester.


Fig.: Cone classifier (settling box). Source: Treptow.


Fig.: Cone classifiers and cone classifier with fresh water countercurrent. Source: Quittkat.


Fig.: Cone classifier with countercurrent. Source: Otero.

13.6 Countercurrent hydraulic classifier

Mining General
Beneficiation, Classification

engl.:

chamber classifier

germ.:

Aufstrom-Hydroklassierer, Kammerklassierer

span.:

hidroclasificador de corriente ascendente, clasificador hidraulico, clasificador de cameras

Manufacturer:

Denver Peru, TMM Potosi Bolivia

TECHNICAL DATA:

Dimensions:

60 × 60 × 100 cm HWD

Weight:

approx. 50 kg

Extent of Mechanization:

not mechanized

Form of Driving Energy:

only processing water and supplementary water

Mode of Operation:

continuous

Throughput/Capacity:

> 0.5 t/h

Technical Efficiency:

high separation precision

Operating Materials:


Type:

water

ECONOMIC DATA:

Investment Costs:

3-chamber, cif La Paz: 9000 US$; Taller Metal Mecanico Potosi: 500 DM

Operating Costs:

very low, low labor costs

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Personnel Requirements:

operating experience necessary

Location Requirements:

water and vertical gradient required

Grain Size:

< 1 mm

Output:

separates, according to equal-settling velocities, into 3 fractions plus fines-overflow

Replaces other Equipment:

screen classification, cone classifiers (settling boxes)

Regional Distribution:

worldwide

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

qualified carpentry or metal workshop, high-quality screens must be available on the national market

Lifespan:

very long |————|————| very short

Bibliography, Source: Priester, Quittkat, Schubert, EP 0012740

OPERATING PRINCIPLE:

The countercurrent hydraulic classifier separates the feed into three or more fractions plus a fines-overflow by means of a cassifying chamber with partitioning walls of varying height. For each fraction to be separated, a bottom screen is provided through which an added underwater flow builds a fluidized bed or turbulent layer. Classified products are removed from the fluidized bed through pipe drains, located in the center of the bed and regulated by cone-shaped valves. In the direction of slurry flow, continually finer products, or products with increasingly slower settling velocities, are separated out. The process is regulated by both the added underwater current and the adjustable valves.

AREAS OF APPLICATION:

Classification of fine-grained feed into several fractions in a continuous operation.

REMARKS:

The precision of separation is higher than with cone classifiers (settling boxes). Extensive experience is required to optimally regulate the process in correlation with the particular feed material. The processing of sulfide ores requires that the equipment be of high-quality materials, especially the screens, since the processing waters are usually acidic and lead to extremely rapid corrosion.

The latest patent literature refers to a cross-current hydro-classifier serving as the basis for an analytical apparatus for examining the grain-size distribution in cement. This classifier has a very narrow and high cross-section, a small classifying-chamber volume, and comparably low throughput, but can continuously or semi-continuously separate the feed material into as many as seven fractions. This operating principle could be applied to hydraulic chamber classifiers for use in ore beneficiation as well.

SUITABILITY FOR SMALL-SCALE MINING:

Countercurrent hydraulic classifiers are very suitable for use in small-scale mining beneficiation operations. Low Investment costs, suitability for local production, drive-less operating systems, and high throughput characteristize this apparatus. Sufficient experience in regulating the apparatus is a prerequisite for optimal utilization; when newly Introduced, its proper use can only be achieved through on-thejob-training (educational requirements).


Fig.: Construction design of a hydro-classifier, type Taller Metal Mecanico, potosi. Source: Priester.


Fig.: Chamber classifier: 1) slurry feed inlet, 2) underwater inlet, 3) sand outlet, 4) sludge overflow, 5) overflow weir, 6) cam shaft, 7) performed bottom. Source: Quittkat.


Fig.: Patented classifier for cement samples; longitudinal and cross-section (patent no. EP 0012740).

13.7 Hydro-cyclone

Mining General (Gold, Ore)
Beneficiation, Classification

germ.:

Hydrozyklon

span.:

hidrociclon

Manufacturer:

AKW, Schauenburg, Dorr-Oliver, Warman, Mozley, Eduardo, Met. Lacha, Voican, Eq. Ind. Astecnia, IAA, INCOMAQ, Buena Fortuna, COMESA, FAHENA, FIMA, MAGENSA

TECHNICAL DATA:

Dimensions:

single cyclones with 10 - 1000 mm 0

Weight:

starting at approx. 1 kg

Extent of Mechanization:

not mechanized when operated only by hydrostatic pressure from the slurry

Power:

pressure of slurry

Form of Driving Energy:

hydrostatic, higher pressures only with the use of a pump, 0.3 - 40 bar

Alternative Forms:

pump with electric or hydromechanic drive system

Mode of Operation:

continuous

Throughput/Capacity:

throughput of slurry up to > 100 t/h, 100 - 2000 g acceleration, throughput is f (nozzle diameter for influent and overflow, and influent pressure). Grain-size of separation between 5 and 2150 ym (maximum 500 ym)

Operating Materials:


Type:

water

ECONOMIC DATA:

Investment Costs:

< 1000 DM

Operating Costs:

low

Related Costs:

pipelines for pressurized water and possibly slurry pump

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Personnel Requirements:

low

Location Requirements:

water and elevation difference (Dh) must be available

Grain Size of Feed:

separation cut-off grain-size up to 500 ym

Special Feed Requirements:

the higher the grain-size to be separated, the larger the diameter of the cyclone has to be.

Output:

depending on type of hydraulic cyclone, more classifying (acute-angled cyclone) or more sorting (obtuse-angled cyclone) occurs.

Replaces other Equipment:

classifiers and sorters for fine fractions

Regional Distribution:

rare in Latin America, otherwise widely distributed

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

metal manufacturing workshop, or workshop for special plastics used in low-pressure cyclones

Lifespan:

very long |————|————| very short


depends upon abrasiveness of the feed material

Bibliography, Source: AKW, Shoukry, Schubert

OPERATING PRINCIPLE:

The slurry feed flows into the cyclone under acceleration (due to hydrostatic pressure) through a tangential inlet-nozzle. Inside the cyclone, the whirling slurry-flow is divided into two currents - an outer sinking portion and an inner ascending portion - as a result of a damping effect from the cyclone's lower conical section. Under these conditions, the heavier or coarser grains comprise the descending slurry-flow and are removed with the underflow, whereas the finer-grained material enters the ascending slurry-flow and is carried out with the overflow (see sketches).

Hydro-cyclones are differentiated according to their areas of application:

- acute-angled hydro-cyclone: solid-fluid-separation (thickening, solids separation), cone angle 10° - 20°,

- intermediate design: classification (cone angle < 20°), - cylindrical hydro-cyclones: sorting, pre-concentration, etc. (CBC-cyclones).

AREAS OF APPLICATION:

- thickening of finest (silty) slurries, suspensions, etc. - desliming

- classification, for example in conjunction with carefully-controlled comminution involving preliminary and intermediary classifying in the milling process

- selective classification, such as for two materials of varying fineness (e.g. quartz sand, kaolin)

- sorting or classifying separation in order to pre-concentrate fine heavy-mineral fractions, e.g. gold, tin or tungsten ores.


SPECIAL AREAS OF APPLICATION:

Sink-and-float method in a heavy-medium cyclone with ferro-silicon.

In this process, separation occurs in a slurry of magnetite or ferrosilicon (FeSi) of a defined density. The dense material can be removed later by magnetic separation. Best results are achieved using atomized dense material due to the rounded grates and also the production process, which lead to:

- low viscosity of slurry
- greater resistance to corrosion
- lower mechanical abrasive wear of the powder
- lower mechanical abrasive wear of the machine
- lower surface adhesion of the beneficiated product

Slurry densities of between 2.0 and 3.8 kg/1 can be achieved with FeSi, enabling ores of iron, manganese, chromite, lead, tin and zinc, as well as fluorite, barite, diamonds, gravel and scrap-iron to be separated.

REMARKS:

A hydro-cyclone classification performed prior to separation with spiral separators, concentrating tables, settling basins, etc., whereby grains are sorted primarily according to their surface area exposed to flow forces, produces a more precise separation than with screen classification.

DESIGN CONSIDERATIONS:

The hydro-cyclone component most susceptible to wear is the underflow nozzle, which is subjects to coarse grains flowing through at relatively high pressure. Various designs for underflow nozzles exist which can extend the lifespan of a cyclone:

- hard-porcelain lining

- replaceable underflow nozzle made of wear-resistant material (rubber, PU, hard
porcelain)

- pneumatically-controlled rubber discharge nozzle - manually-controlled rubber discharge nozzle

For normal acute-angled cylindrical-conical cyclones with intake angles of 10°- 20°, the following dimensions can be recommended:

Di = (0.15 - 0.25) Dc where

Dc : diameter of cyclone

Do = (0 20 - 0-40) Dc where

Di : diameter of intake nozzle

Da = (0.15 - 0.80) Do where

Do : diameter of overflow nozzle


Da : diameter of underflow nozzle

The finer the separaion cut-off grain size, the smaller the diameter of the cyclone and the higher the intake pressure must be.

SUITABILITY FOR SMALL-SCALE MINING:

Due to the diverse areas of application for purposes of desliming or desilting, classifying or sorting, the hydro-cyclone is very suitable for small-scale mining. Prerequisite for drive-less operation is the minimal elevation gradient of 3 - 10 m. Even considering that hydro-cyclones can only be locally produced in exceptional cases, they are still appropriate particularly for sorting classification purposes. Hydro-cyclones are comparably simple in design and low in cost.


Fig.: Diagram of flow pattern in a hydro-cyclone. Source: AKW.


Fig.: Various types of cyclones for desliming (left, classifying (middle) and sorting (right). Source: AKW.


Figures
Fig.: Pneumatically-controlled under-flow nozzle for hydro-cyclones, made of elasomer. Source: Guelt

Fig.: Modular construction of a hydro-cyclone. Source: Shoukry.

13.8 Log washer, spiral classifier

Mining General
Benefication, Classification

germ.:

Logwasher, Spiralklassierer

span.:

atrisionador, clasificador de espiral

Manufacturers of spiral classifiers:

FUNSA, Volcan, IAA, COMESA, FAHENA, FIMA, Famia, Fund. Callao, MAGENSA, MAEPSA, Met. Mec. Soriano, PROPER, FAMESA

TECHNICAL DATA:

Dimensions:

1 × 1 × 8 m HWD, inclination 1: 20, shaft diameter 18", length of shovel 9", also smaller dimensions possible

Weight:

several tons

Extent of Mechanization:

semi-mechanized

Power:

up to 25 PS, double-classifier up to 30 PS, 15 - 20 min-1

Form of Driving Energy:

belt transmission from internal combustion engine, electric motor

Alternative Forms:

turbine/water wheel

Mode of Operation:

semi-continuous

Throughput/Capacity:

up to 100 t/24 h

Operating Materials:


Type:

water

Quantity:

up to 200 I/min

ECONOMIC DATA:

Investment Costs:

when locally produced 1000 to 5000 DM

Operating Costs:

depends on drive system

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Location Requirements:

water requirements must be met

Grain Size of Feed:

< 5 - 10 cm

Output:

cclassified into underflow (silt and fine fraction) and overflow (coarse fraction)

Replaces other Equipment:

sppiral classifier

Regional Distribution:

USA, Australia

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad


if hard lumber is available

Under What Conditions:

wood and metal-manufacturing workshops

Lifespan:

very long |————|————| very short

Bibliography, Source: v. Bernewitz, Schennen

OPERATING PRINCIPLE:

Analogous to spiral classifiers. The slurry, fed onto the lower one-third of the shaft, is separated by means of the shovels into an upward-flow containing the coarse, heavy grains and a downward-flow containing the light-weight grains. The classification box of rectangular cross-section fills with material at the start of the process before the actual classification begins.

AREAS OF APPLICATION:

Desliming, classification, drainage, and separating of the ground product in grinding circuits.

REMARKS:

Construction does not require that the housing be adjusted to the cross-section of the shaft since gaps are filled with minerals.

Separation cut-off grade is determined by angle of inclination.

SUITABILITY FOR SMALL SCALE MINING:

In smaller dimensions log washers are also appropriate for small-scale mining classification purposes if a suitable drive-system is available at low energy costs. Log washers are very suitable for local production.


Fig.: Schematic diagram of a log washer. Source: Bernewitz.



Fig.: Design of a single spiral classifier: 1) motor, 2) drive, 3) gear wheel, 4) spiral, 5) lifting device, 6) outlet, 7) feed intake, 8) flow (transport) direction, 9) discharge, 10) traverse. Source: Schiedchen.

13.9 Rake classifier

Deep Mining General
Beneficiation, Classification

germ.:

Rechenklassierer

span.:

clasificador transportador a rastrillo

Manufacturer:

Volcan, Eq. Ind. Astecnia, IAA, COMESA, FAHENA, MAENSA, FAMESA

TECHNICAL DATA:

Dimensions:

1.2 × 3.5 × 1.0 m HWD for a small rake classifier, working frequency 10 - 30 min-1, minimum angle of inclination 12 Weight: approx. 600 kg

Extent of Mechanization:

ully mechanized

Power:

1.5 PS

Form of Driving Energy:

mechanical via electric motor, internal combustion engine, turbine

Mode of Operation:

continuous

Throughput/Capacity:

0.5-1 t/h

Operating Materials:


Type:

water

ECONOMIC DATA:

Investment Costs:

minimum of 10.000 DM when locally produced

Operating Costs:

low, primarily energy costs

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————|high

Location Requirements:

none, except water

Grain Size of Feed:

high proportion of fine grains (0.1 - 0.5 mm) necessary to guarantee stability of the suspension. Only under these conditions can a rake classifier separate with high precision.

Special Feed Requirements:

30 - 50 % by vol. solids in the slurry

Output:

the classifying is regulated by controlling the slurry density

Replaces other Equipment:

spiral classifier

Regional Distribution:

very rare

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

national machinery manufacturers

Lifespan:

very long |————|————| very short

Bibliography, Source: Gerth

OPERATING PRINCIPLE:

In a declined trough, the coarse material is scraped upwards by a rake. At the return point, the rake is lifted, moved back down to the initial position and lowered onto the bottom of the trough. The fine material remains suspended and flows out over a weir at the lower end of the trough. The slurry-feed intake is located about a third of the way up from the lower end of the trough.

AREAS OF APPLICATION:

For intermediary classification of milled material in a closed grinding circuit.

REMARKS:

Very low wear, limited to the rake.

The rake has a very long lifespan due to the possibility to adjust its height. For lead-zinc ore, Gerth estimates a rake lifespan of approx. 30.000 t throughput (rake height worn from 60 down to 20 mm).

SUITABILITY FOR SMALL-SCALE MINING:

Rake classifiers are characterized by their simple construction and low wear' and are suitable for small scale mining if they can be nationally manufactured.


Fig.: Schematic diagram of a rake classifier. Source: Schmiedchen.


Fig.: Simplified elevation drawing of a rake classifier. Source: Schmiedchen.

13.10 Sluice, sluice box, washing sluice

Mining General
Beneficiation, Classification

germ.:

Lauterrinne, Ablauterrinne, Waschrinne

span.:

canaleta de lavado, canaleta de relavado, canaleta de limpieza .

TECHNICAL DATA:

Dimensions:

inclination: approx. 10°, several stepped sections approx. 50 - 60 cm in width and 50 cm in depth, 4 - 5 m total length

Weight:

masonry construction, built into the ground

Extent of Mechanization:

not mechanized

Form of Driving Energy:

uses the energy of flowing water, possibly supported by turning the material with rakes, shovels, etc.

Throughput/Capacity:

several tons of material per hour

Operating Materials:


Type:

water

Quantity:

at least ten times the feed quantity

ECONOMIC DATA:

Investment Costs:

very low since the sluice is built into the ground with minimal effort

Operating Costs:

labor costs only

Related Costs:

beneficiation equipment for the fine slurry, e.g. settling basins or buddies

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Location Requirements:

water must be available in large quantities

Grain Size of Feed:

from silt fraction (fines) to approx. 200 mm

Special Feed Requirements:

washing (i.e. dissociation of strongly baked, partially solidified grain bonds) must occur during beneficiation of conglomerates and breccia, or during re-processing of old waste deposits or abandoned workings

Output:

coarse fraction is sufficiently cleaned to allow hand-sorting

Replaces other Equipment:

washing drum, autogenous mill

Regional Distribution:

found rarely in small-scale mining, e.g. in Bolivia/Potosi

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high


depending on type of feed, sludge (fines) loading can occur, requiring a subsequent fines separation, when necessary with sludge pond or settling basin.

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

local production is easily possible since only simple masonry work is involved

Lifespan:

very long |————|————| very short

Bibliography, Source: Rittinger

OPERATING PRINCIPLE:

The feed material in the washing sluice is separated into its individual components through the energy conveyed by the flowing water and through supplementary agitation (manually-operated shovels, rakes, etc.).

AREAS OF APPLICATION:

For crushing and classifying slightly-solidified conglomerates and breccia as well as cemented crude ore from underground mines, old deposits or abandoned workings.

REMARKS:

To process feed with high clay content, e.g. from abandoned works, the material is mixed with water in a basin or pit and is repeatedly kneaded by means of stamping or worked with scrapers or picks. In this way, the adhesive and cohesive forces of the cemented clay fractions are broken down. This process is called ch'etachado in Quechua. It is very work intensive, but in combination with subsequent washing in a sluice, it is the only possibility for non-mechanized mines to process feeds with high clay contents.

SUITABILITY FOR SMALL-SCALE MINING:

Washing in sluices is the simplest method of crushing and classifying slightly-solidified feed or feed materials of high clay content.

CLOSE THIS BOOKTools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)
Technical Chapter 14: Sorting
VIEW THE DOCUMENT14.1 Jig screen, hand-jigging
VIEW THE DOCUMENT14.2 Simple hand jig, moving bed(percussion) jig
VIEW THE DOCUMENT14.3 Hand piston jig
VIEW THE DOCUMENT14.4 Piston jig, ''harzer'' jig
VIEW THE DOCUMENT14.5 Pulsator classifier pan american jig
VIEW THE DOCUMENT14.6 Sluices with or without linings/insets, long tom
VIEW THE DOCUMENT14.7 Ground sluice
VIEW THE DOCUMENT14.8 Pinched sluice, fanned sluice
VIEW THE DOCUMENT14.9 Air separator, dry blower
VIEW THE DOCUMENT14.10 Settling basin, buddle
VIEW THE DOCUMENT14.11 Circular buddle
VIEW THE DOCUMENT14.12 Dolly tub
VIEW THE DOCUMENT14.13 Bumping table, concussion table
VIEW THE DOCUMENT14.14 Racking table, tilting frame
VIEW THE DOCUMENT14.15 Sweeping table, belt table
VIEW THE DOCUMENT14.16 Vibrating table
VIEW THE DOCUMENT14.17 Humphrey's spiral, spiral separator
VIEW THE DOCUMENT14.18 Spiral concentrator

Tools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)

Technical Chapter 14: Sorting

14.1 Jig screen, hand-jigging

Metal Mining, Gem Mining
Beneficiation, Sorting

germ.:

Handsetzen im engen Sieb, Setzsieb

span.:

concentracion gravimetrica manual en cribas pequenas, criba pequena pare concentracion

TECHNICAL DATA:

Dimensions:

15 × 30 × 20 cm HWD

Weight:

approx. 0.5 -1 kg

Extent of Mechanization:

not mechanized

Form of Driving Energy:

manual

Mode of Operation:

intermittent

Throughput/Capacity:

0.5 - 1.5 kg/M × min

Operating Materials:


Type:

water

Quantity:

small

ECONOMIC DATA:

Investment Costs:

< 10 DM

Operating Costs:

low, only labor costs

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Personnel Requirements:

low

Grain Size of Feed:

(50) 200 ym · 2 mm

Special Feed Requirements:

high density difference between valuable mineral and host material

Recovery:

relatively high, since process can be precisely regulated

Replaces other Equipment:

sluice

Regional Distribution:

Bolivia

Operating Experience:

very good |————|————| bad

Difficulties:

very low efficiency

Environmental Impact:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

screen material has to be available

Lifespan:

very long |————|————| very short

Bibliography, Source: Priester, Agricola, Lohneyss

OPERATING PRINCIPLE:

Manual Jigging operation achieved through up-and-down movements of the screen in water. Separation occurs through the oscillating movements of the Jigged material: concentrate on the bottom, then the middlings, and on top, the waste material. The valuable mineral is concentrated through repeated jigging of the feed material with simultaneous removal of the waste with a spatula

AREAS OF APPLICATION:

Refining/secondary cleaning of fine and medium-grained products.

REMARKS:

Very work-intensive technique with very low efficiency.

SUITABILITY FOR SMALL-SCALE MINING:

This manual Jigging technique using Jig screens is only suitable for special application such as prospecting and exploration, or for processing small quantities of feed requiring a very precise separation cut-off, due to the high level of strenuous physical work involved and the low specific output.


Fig.: Work-chronogram of manual jigging operation with jig screen. Source: Priester.

14.2 Simple hand jig, moving bed(percussion) jig

Metal Mining, Coal Mining
Beneficiation, Sorting

germ.:

Einfache Handsetzmaschine, Stauchsetzmaschine

span.:

maritate

TECHNICAL DATA:

Height of Jig:

5 cm to max. 10 cm, jig dilluing depth 2" for coarser feed, < 1" for finer feed, frequency 80 min-1 (coarse feed) up to 120 min-1 (fine feed material)

Dimensions:

approx. 2 × 1 × 3 m HWD

Weight:

approx. 100 kg

Extent of Mechanization:

non mechanized

Form of Driving Energy:

manual

Alternative Forms:

pedal-drive, hydromechanical

Mode of Operation:

intermittent

Throughput/Capacity:

5 - 10 kg/M × min

Operating Materials:


Type:

water

Quantity:

small

ECONOMIC DATA:

Investment Costs:

approx. 250 DM, lower when self-constructed

Operating Costs:

very low, practically only labor costs

Related Costs:

none

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Personnel Requirements:

low

Location Requirements:

none

Grain Size of Feed:

500 ym - 10 mm (30 mm)

Special Feed Requirements:

high density difference between valuable mineral and host material

Output:

concentrate approx. 30 %, middlings approx. 50 %; secondary separation leads to higher total recovery

Replaces other Equipment:

mechanized types of jigs

Regional Distribution:

Bolivia

Operating Experience:

very good |————|————| bad


when employed for production of pre-concentrates or coarse-grain separation

Environmental Impact:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

wood manufacturer, good screen quality is a prerequisite

Lifespan:

very long |————|————| short

Bibliography, Source: Priester, Taggert, Stewart, Treptow, Schennen, Bernewitz, Liwehr, German Museum, Cancrinus, Callon, Stifft, Rittinger

OPERATING PRINCIPLE:

In manual moving-bed (percussion) jigs, the feed material undergoes pulsating movements in water which produces a vertical differentiation according to density; the heaviest material lies on the bottom, the medium-weight material in between, and the light material on top. Concentration of the valuable mineral is achieved through repeated feeding of the jigged material and removal of the light material.

AREAS OF APPLICATION:

for

- production of pre-concentrates


- sorting of coarse grains

SPECIAL AREAS OF APPLICATION:

For wet classification, whereby the undersized-pre-concentrate is removed from the Jig box.

REMARKS:

In the Harz mining region of Germany, mechanized moving-bed (percussion) Jigs were employed up until the 19th century.

Jigs suspended from spring-mounted wooden beams anchored at one end; with guides.

Percussion Jigs are characterized, contrary to all other types of jigs, by their extreme low consumption of processing-water, which is an Important advantage. A shortage of water at beneficiation-plant locations in Latin American small-mining operations often restricts the possibilities to employ wet mechanical settling processes or wet classification in moving-bed (percussion) jigs.

Additionally, moving-bed Jigs can handle larger throughput quantities than piston Jigs.

A further advantage is the minimal loss of valuable minerals through the fines, since they are removed from the Jig box.

For all types of jigs, it is absolutely necessary that the screens are of the highest quality. Even surface-tempered screen material remains abrasion and corrosion resistant only for a short period before rusting, which leads to clogging especially of the fine-meshed screens. Especially during processing of sulfide ores, or through the use of mine water in beneficiation, the screens are subject to such strong corrosion from acidic water that screens of inferior quality can become useless after Just one application.

SUITABILITY FOR SMALL-SCALE MINING:

Due to its simple operating principle and suitability for local production, the hand Jig is knowngood traditional ore-beneficiation tool which has become widely distributed throughout the small-scale mining industry. The manual extraction of the product provides a high degree of separation precision, which, however, is offset by the disadvantages ofintermittent operation and low throughput. Use of the hand jig is suitable where water availabilily is limited.


Fig.: Work-chronogram of a simple hand jig, or "maritate" to produce pre-concentrate from feed material of low valuable-mineral content. Source: Priester.


Fig.: Sketch of a simple hand jig (see above). Source: Priester.


Fig.: Plan view of double-chambered hand jig. Source: Priester.


Fig.: Cross-sectional view of double-chambered hand. Source: Priester.


Fig.: Hand jing attached to a spring-mouned wooden beam. Source: Cancrinus.


Fig.: Hand jig from the Harz mining region (Germany) design. Source: Treptow.


Fig.: Simple hand jig. Source: Schennen


Fig.: Hand jig. Source: Stewart

14.3 Hand piston jig

Metal Mining, Coal Mining
Beneficiation, Sorting

engl.:

manual diaphragm jig, pedal diaphragm jig

germ.:

Kolbenhandsetzmaschine, Membran-Handsetzmaschine, Membran Pedalsetzmaschine

span.:

maritate de embolo, maritate con diafragma, maritate a pedal con diafragma

Manufacturer:

manual diaphragm jig: Taller Metal Mecanico, Campo Nuevo, both Bolivia

TECHNICAL DATA:

Dimensions:

hand piston jig: approx. 1.5 × 1 × 2 m HWD; manual diaphragm jig: approx. 1.5 × 1 × 1 m HWD

Weight:

hand piston jig: approx. 100 - 150 kg; manual diaphragm Jig: 50 - 100 kg

Extent of Mechanization:

not mechanized

Form of Driving Energy:

hand piston jig: manual; manual diaphragm jig: manual or pedal-drive

Mode of Operation:

hand piston jig: semi-continuous; manual diaphragm jig: intermittent

Throughput/Capacity:

hand piston jig: 0.5 - 1 t/Mh

Operating Materials:


Type:

water

Quantity:

hand piston jig: approx. 100 I/min; manual diaphragm jig: small quantities

ECONOMIC DATA:

Investment Costs:

hand piston jig: approx. 350 DM, lower if self- made; manual diaphragm jig: 300 - 550 DM

Operating Costs:

low, practically only labor costs

Related Costs:

none

CONDITIONS OF APPLICATION:


hand piston Jig

Operating Expenditures:

low |————————| high


manual diaphragm jig

Maintenance Expenditures:

low |————|————|high

Personnel Requirements:

low

Location Requirements:

hand piston jig: flowing water necessary; manual diaphragm jig: none

Grain Size of Feed:

hand piston jig: 1 mm - 30 mm; manual diaphragm jig: (50) 200 µm - 2 mm

Special Feed Requirements:

high density difference between valuable mineral and host material

Output:

hand piston jig: approx.concentrate 30 %


middlings 50 %


waste: 20 °/0

Replaces other Equipment:

hand piston jig: mechanized jigs; manual diaphragm jig: jig screen, washing sluice

Regional Distribution:

hand piston jig: Bolivia and worldwide; manual diaphragm jig: in Potosi, Bolivia as proto-type


hand piston jig

Operating Experience:

very good |————|————| bad


however often replaced by simple hand jigs;


manual diaphragm jig: information not yet available


hand piston jig

Environmental Impact:

low |————————| very high


manual diaphragm jig


manual piston jig: environmentally detrimental due to sludge/silt load; can be solved through use of a thickener or clarifying basin


hand piston jig

Suitability for Local Production:

very good |———|————| bad


manual diaphragm Jig

Under What Conditions:

hand piston jig: wood manufacturer; manual diaphragm jig: wood and metal-manufacturing shops


hand piston jig

Lifespan:

very long |————————| very short


manual diaphragm jig

Bibliography, Source: Priester, Treptow, Callon, de Hennezel, Rittinger, Hunter, Stewart

OPERATING PRINCIPLE:

Hand piston jig:

Manually-operated pulsating Jig with double jig box. Operating principle is analogous to that of a hand Jig, with the addition of a lateral component generated by the longitudinal flow of the slurry through the jig. Thus the purely up-and-down motion with various vibrational amplitudes is overlaid by a longitudinal motion, which creates density-dependent particle flow-paths of varying vibrational amplitudes and wavelengths. This results in a faster transport of lighter (lower specific weight) particles and slower transport of heavier particles (higher specific weight). Consequently, in the semi-continuous operation, the heavier concentrate grains remain in Screen 1 due to their lower vibrational amplitude, while the middlings and tailings land in Screen 2, with the tailings subsequently being carried out of the jig with the slurry flow.

Manual diaphragm jig:

Manual pulsating jig or pulsating jig with pedal drive. An oscillating motion is induced in the process water flow by means of a car-tire pulsator. The jig feed moves up and down and is sorted via vertical density differentiation.

AREAS OF APPLICATION:

Hand piston jig:

The sorting process is interruped to allow removal of the products. Employed for pre-concentration of coarser material.

Manual diaphragm jig:

Used to perform simplified jigging of fine and medium-sized grain fractions as an improvement over manual screen Jigging.

REMARKS:

Hand piston jig:

Wet classification: relatively low recovery of finer grain fractions due to the high velocity of slurry flow which also carries valuable-mineral particles out with the discharge. To achieve high recovery values, a wet classification in pulsating Jigs should be avoided. Alternatively, the fines should be caught in sedimentation basins and reprocessed (secondary separation).

A small bucket elevator (conveyor) - manual or mechanized - can be used to extract the product from the settling basin.

The density distribution of the feed must be regarded as the most important parameter in controlling the jigging process. The higher the density difference between the valuable mineral and host rock or waste material, the more successful the material can be separated in a jig. Schubert ( 1978) offers the following formula for estimating the sortability of the feed:

dS= specific density of the heavy mineral, or density of the ore or valuable mineral in beneficiation

d1= specific density of the light mineral, or density of the gangue (waste material or host rock) in beneficiation

d= density of the medium, usually water, density = 1

For determining the suitability of jigging in water, the value of q indicates the following:

q over 2.5:

separation by jigging is possible up to a lower grain- size limit of 100 ym

q over 1.75:

separation by jigging is possible up to a lower grain-size limit of 200 ym

q over 1.5:

separation up to 1.5 mm is possible, but difficult

q over 1.25:

separation by jigging is not possible

Manual diaphragm jig:

Proto-types exist, but results of operation are not yet known.

Difficulties can arise during operation concerning the homogeneity of the water flow over the jig bed; inhomogeneities must be minimized through the use of metal chutes to prevent disruption of the processing. Further need for research and development efforts.

Additional problems: sealing between the tire and the housing as well as between the tire and the reflecting plate. The use of counter-weights can minimize the leverage forces.

SUITABILITY FOR SMALL-SCALE MINING:

Hand piston jig:

As a purely manually-operated machine, the hand piston jig is suitable only under special circumstances. Since large quantities of water are needed to operate the hand jig, it should be investigated whether a hydromechanization as a "Harzer" Jig would be possible. Advantages of the hand Jig are its simple design and suitability for local construction.


Fig.: Work-chronogram of jigging in a piston jig. Source: Priester.


Fig.: Front view, side view and plan view of pulsating hand jig with car-tire pulsator. Source: Priester.


Fig.: Plan view and cross-section of a hand piston jig. Source: Priester.

14.4 Piston jig, ''harzer'' jig

Metal Mining, Coal Mining
Beneficiation, Sorting

germ.:

Kolbensetzmaschine, Harzer Setzmaschine

span.:

jig de embolo, jig tipo Harz, maritate tipo Harz, jigger

Manufacturer:

Millan. Met. Lacha, Eq. Ind. Astecnia, Buena Fortuna, COMESA, FAHENA, FIMA, Famia, MAGENSA

TECHNICAL DATA:

Dimensions:

approx. 2 × 2 × 2 m

Weight:

starting at 200 kg

Extent of Mechanization:

semi-mechanized

Power Required:

starting at 3 - 5 kW

Form of Driving Energy:

mostly electric or with internal combustion engine via transmission


(mechanical)

Alternative Forms:

hydromechanical

Mode of Operation:

semi-continuous

Throughput/Capacity:

> 1 t/h

Operating Materials:


Type:

water

Quantity:

> 100 1/min

ECONOMIC DATA:

Investment Costs:

starting at 500 DM without drive-system

Operating Costs:

depends on type of mechanization and primary energy source

Related Costs:

handling of sludge

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————————| high

Personnel Requirements:

low

Location Requirements:

flowing water required

Grain Size of Feed:

1 - 30 mm

Special Feed Requirements:

high density difference between valuable mineral and host material

Output:

approx. 30 % as concentrate


50 % as middlings


20 % as waste

Replaces other Equipment:

all other types of jigs

Regional Distribution:

Bolivia, Peru, historically worldwide

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————————| very high


environmental pollution through sludge/silt loading; solved by using thickeners or sedimentation basins

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

wood manufacturer; high quality screens necessary

Lifespan:

very long |————|————| very short

Bibliography, Source: Fischer, Liwehr, Treptow, Callon, Kirschner

OPERATING PRINCIPLE:

Mechanized pulsating jig which works analogous to a hand piston jig, but is equipped with a mechanized drive-system via an eccentric shaft. Mechanized Jigs operate efficiently only when the extraction of concentrate and middlings occurs so as to ensure a continuous operation.

AREAS OF APPLICATION:

Production of pre-concentrate. Sorting of coarse grain fractions.

SPECIAL AREAS OF APPLICATION:

In addition to hydromechanical-gravimetric sorting also for wet classification.

REMARKS:

In wet classification, relatively low recovery of fines.

Various constructions for discharge of products which also offer continuous operation are of great advantage:

- pipe and bell, installed in the center of the screen bottom, convey the product out of the water- filled jig box. Adjustment of slot width and height of pipe supports allows the proportion of concentrate to be regulated;

- side slits and discharge devices in retained water

- side-mounted sliding plug in conjunction with an inclined jig bottom which functions as a discharge in retained water.

Kirschner gives the following design data for the piston stroke relative to the grain-size of the feed:

Grain Size
(mm)

Frequency
(min-1)

Grain Size
(mm)

Amplitude
(mm)

Grain Size
(mm)

Amplitude
(mm)



20 - 30

75

3 - 5

35

1.5 - 3

140

13 - 20

60

2 - 3

25

3 - 8

130

8 - 13

50

1.5 - 2

15

8 - 30

110 - 120

5 - 8

40



SUITABILITY FOR SMALL-SCALE MINING:

The high throughput quantities achievable in conjunction with a continuous mode of operation, as well as the ability to easily regulate product quality, make "Harzer" Jigs very suitable even for use in larger small-scale mining operations. In combination with a hydromechanical waterwheel drive, they present an ideal classifying method.


Fig.: Sliding drive transmission for the jig piston. Source: Treptow.


Fig.: Adjustable eccentric (cam) of "Harzer" jig. Source: Treptow.


Fig.: Various forms of discharge devices for "Harzer" kigs. Above left: weirs in a jig with inclined jig bed (Source: Fischer), side-slots in retained water (Treptow), pipe and bell (Treptow) and funnel and pipe (Treptow).


Fig.: "Harzer" jig with discharge through a pipe out the side; discarge outlet in detail. Source: Liwehr.


Figure
Fig.: "Harzer" jig with hoisting device for discharge of the heavy component. Source: Liwehr.
Fig.: Detail of coal jig discharge. Source: Treptow.


Fig.: Detail of central discharge throught pipe and bell from "Harzer" jig. Source: Liwehr.


Fig.: Discharge with slotted weir and counter-current water. Source: Liwehr.

14.5 Pulsator classifier pan american jig

Metal Mining, Coal Mining
Beneficiation, Sorting

engl.:

diaphragm jig

germ.:

Pulsatorsetzmaschine, Membransetzmaschine

span.:

jig de diafragma, jig de ague, jig con pulsador

Manufacturer:

Denver, Svalcor

TECHNICAL DATA:

Dimensions:

approx. 1 × 1 × 1 m HWD

Weight:

starting at around 150 kg

Extent of Mechanization:

semi-mechanized

Form of Driving Energy:

water pressure

Alternative Forms:

pneumatic jigs

Throughput/Capacity:

approx. 20 t/h × m² jig bed

Operating Materials:


Type:

water

Quantity:

420 - 6601/min × m2 pg bed

ECONOMIC DATA:

Investment Costs:

minimum 500 to 1000 DM when self-constructed

Operating Costs:

low, mainly labor costs

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Location Requirements:

water and elevation gradient necessary

Grain Size of Feed:

approx. 0.5 - 10 mm

Special Feed Requirements:

high density difference between valuable mineral and host material

Output:

analogous to other coarse-grain jigging processes

Replaces other Equipment:

under certain conditions, the mechanized jig

Operating Experience:

very good |————————| bad


mostly unknown

Environmental Impact:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

welding and metal workshops

Lifespan:

very long |————|————| very short

Bibliography, Source: Priester, Schubert

OPERATING PRINCIPLE:

Hydromechanic pulsating jig, whereby the water flow is induced by a diaphragm-spring system. Analogous to "Harzer" Jig. Continuous-drive, semi-continuous operation. Pan-American jigs are operated with a jig bed and the screen throughput of the concentrate.

AREAS OF APPLICATION:

Sorting and pre-concentrating coarse-grained feed material.

REMARKS:

- other forms of discharge devices may be possible

- pulsators can be simply constructed of rubber diaphragms (car tires)

- a buffer of air at the charging side underneath the pulsator elastically suppresses the water movements.

SUITABILITY FOR SMALL-SCALE MINING:

Given sufficient water and vertical elevation gradient, and when the construction permits continual operation, this type of jig appears to be suitable for the sorting of coarse and medium-grained feed in small-scale mining operations.


Fig.: Pulsating jig (Pan-American jig): a) jig, b) pulsator; 1) jig box, 2) funnel, 3) pulsator, 4) water supply line, 5) spring, 6) diaphragm, 7) flutwater valve, 8) brake sieve 9) concentrate dis-charge. Source: Schubert.

14.6 Sluices with or without linings/insets, long tom

Metal Mining, Alluvial Gold Mining
Beneficiation, Sorting

germ.:

Rinnenwasche mit und ohne Einsatze

span.:

canaleta para la concentracion , canal eta, chap a lavadora, canalon prefabricado, mesas rayadas, canoe

Manufacturer:

Keene

TECHNICAL DATA:

Dimensions:

inclination of sluice depends on mode of operation and grain-size of feed: 2° - 8° for semi-continuous pre-concentration of heavy mineral feed; 14.8° in Bolivia for reprocessing of narrowly classified concentrates in intermittent operation. Depending on the individual situation, sluices ranging from 2 × 0.5 × 0.5 m (Bolivia) to > 100 × 2 × 2 m (Thailand) are in use.

Weight:

depends on type of construction, either as masonry built into the ground, or as wooden construction

Extent of Mechanization:

not mechanized

Form of Driving Energy:

only processing water

Alternative Forms:

possibly mechanical vibrators/shakers

Mode of Operation:

intermittent/semi-continuous

Throughput/Capacity:

between 10 - 100 kg/in in a discontinuous operation; around 20 - 50 t/h in a semi-continuous operation

Operating Materials:


Type:

water

water


in intermittent operation

in semi-continuous operation

Quantity:

up to 351/min

6-10: 1 ratio of fluid volume: solids volume

ECONOMIC DATA:

Investment Costs:

up to 10 DM/m

Operating Costs:

labor costs only; with turf lining higher costs due to frequent replacement

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Personnel Requirements:

experience is necessary

Location Requirements:

flowing water necessary, minimum elevation gradient Dh of 0.5 m

Grain Size of Feed:

(100) 500 - 2000 ym (3 mm)

Special Feed Requirements:

high density difference between valuable mineral and host material

Output: .

approx. 60 % as concentrate, 40 % as waste in re-concentration of tin concentrates. Recovery is increased by re-sorting. Gold-sluices yield around 90 % in optical operation; the major problem is the loss of fines and of the flat, flour-like (float) gold particles, which can reduce the recovery to less than 50 % of the valuable mineral in some instances.

Replaces other Equipment:

fine-grain jigs, jig screens, flotation cells

Regional Distribution:

Bolivia; in gold mining worldwide

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|———()—| very high


when accompanied by flotation in the sluice, high contamination of receiving stream through acids, diesel oil and reagents

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

depending on construction, simple wood working, tin-smithing (sheet metal) or masonry work

Lifespan:

very long |————|————| very short


when using sluices with turf lining, these have to be replaced every 2 - 6 weeks, depending on throughput quantities.

Bibliography, Source: Pirester, Stout, Treptow, Schanbel, Kirschner, Ambio, manufacturer infromation, Silva.

OPERATING PRINCIPLE:

Sluices of different longitudinal profiles (e.g. straight, bent, inclined to varying degrees, concave, etc.) with water flowing through in which, at the location of separation, the flow conditions are so regulated as to allow further conveyance of the light material but sedimentation of the heavier valuable-mineral particles.

AREAS OF APPLICATION:

For sorting of medium-sized grain fraction; for secondary processing of concentrates.

SPECIAL AREAS OF APPLICATION:

Flotation in sluice washers to eliminate sulfide impurities (e.g. pyrite, arsenopyrite, etc.) from oxidic concentrates (e.g. tin ore (cassiterite) or wolframite) .

Reagents: sulfuric acid, diesel oil, xanthate.

Feed: coarser than in hydromechanic-gravimetric sorting.

In gold mining, amalgamation is also frequently performed in sluices, whereby mercury is placed in the riffle channels. This technique leads to high Hg-losses (5 - 30 % of the Hg used per round) as a result of the mercury being broken down into small perls that are then flushed out with the slurry. In Brazilian mining, pieces of soap are packed into the riffle channels along with the mercury in an attempt to minimize the Hg losses. In any event, the practice of conducting amalgamation in sluices is extremely detrimental to the environment.

REMARKS:

Turf lining improves the separation precision in sluices (Bolivian name for this type is "Champalvadora") by increasing adhesive forces at the bottom. The following plant varieties are used in Bolivia for vegetative linings:


- Plantago tubulosa Decne
- Distichia muscoides

Both are proliferous ground-covering plants indigenous to the Andean moor ecosystem (bofedales).

Besides vegetative linings, other riffles and inserts are also being used to enhance the sorting characteristics of sluices by altering the bottom-surface and flow conditions. Known methods include:

- wooden cross-riffles
- stone packing
- rubber matting (car footmats)
- sisal (hemp) mats
- fine and coarse textiles (e.g. corduroy)
- Venetian window-blind arrangement of split bamboo rods
- structural metal/iron grid
- expanded metal mesh (biscocho, malla rombica)
- nets/mesh made from knotted ropes (e.g. hemp or grass), coarse screen mesh, or a combination of these.

Such sluices already characterize the transition to blanket sluices (corduroy tables) especially since such sluices mostly operate semi-continuously.

The higher the proportion of heavy minerals in the feed, the larger the sluice must be. In tin-ore mining in Thailand, sluices (palong) with lengths up to 120 m are in use, whereby the length also serves to homogenize the slurry flow.

The higher the proportion of heavy minerals in the feed, the larger the volume of the sedimentation chambers behind the riffles needs to be in order to permit a sufficiently long operating period without interruption for removal of concentrate.

The finer the grain-size of the valuable minerals in the feed, the smaller the sluice inclination must be to prevent the slurry velocity from becoming too high. In mining of alluvial deposits in Southeast Asia, sluice inclinations of 3°- 6 can be observed (slurry speed: 0.7 to 3.0 m/s).

The latest state of technology for sluice sorting is the use of artificially-induced vibrations in sluice-bed proximity, generated through electric or pneumatic vibrators. The high-frequency motions contribute toward improving the separation precision and allow reduction of the sluice length. To minimize the required energy consumption, only the sluice bottom, mounted with flexible rubber seals, is vibrated.

In gold beneficiation, the successful sorting in sluice washers with riffles or stone packing requires an exact setting of the sluice inclination. If the sluice is installed too flat (a common error), the riffle channels or spaces between the packed stones become filled up with sediment, preventing flow turbulence behind the riffles, and consequently sedimentation of gold, from occurring. On the other hand, if the sluices are set too steep, gold is flushed out of the sedimentation chambers, leading to increased losses and decreased recovery.

Also of importance is the avoidance of fluctuations in the feed quantity. Whenever only pure water flows through the sluice following separation, already-sedimented gold is partially carried back out.

Long wooden riffle sluices (about 4 m) are found frequently in gold mining, succeeding delivery chutes and washing sluices in the processing sequence. These so-called "long toms" are in use worldwide. Their average inclination is about 8%; throughput quantities total around 3.5 m gold-containing feed per day.

An interesting new development is a small tandem sluice in which the slurry feed flows over a screen (3/16") and separates into an underflow of the -450 ym grain-fraction and an overflow of the coarser grains. These two divided slurry streams then run over two riffled sluices, stacked on top of each other; the throughput (flow volume) of the fine slurry can be regulated by adjusting the slurry-feed level of the upper sluice, accomplished by restricting the cross-section of the discharge.

Another form of sluice washer was invented for processing magnetic and slightly-magnetic valuable minerals. This is a combined sluicing/magnetic separation process where magnets are placed underneath the sluice bottom near the riffle channels.

One method applied in gold ore mining involves the flow of slurry feed through a sluice with a concave depression for extracting fine gold. Mercury Iying in this cavity is stimulated by ultrasound, leading not only to a more precise density differentiation, but also to a strong activation of the Hg surface and resulting heating. The micro-sized Hg begins to evaporate and selectively precipitates onto the gold surface, a process which enhances amalgamation. Cooling is achieved by the water flowing through the sluice. The proper adjustment of the sluice incline is complicated; it should prevent mercury from being carried out while at the same time assuring optimal surface contact for amalgamation.

Riffles for sluices used in gold mining are between 1 and 3 cm in height and installed at distances of 1 - 10 cm from the riffle grid inserted in the sluice.

Gold recovery from sluices increases if riffle grids are cleaned sufficiently often. During longer periods of operation there is a tendency for riffles to become filled or clogged with heavy minerals, causing a loss in recovery of the fine-grained material.

Studies in Brazil showed that Hg losses from amalgamation processes in sluices comprise around 40 - 50 % of the total Hg emissions in that country.

SUITABILITY FOR SMALL-SCALE MINING:

Sluices with a discontinuous charging of feed, and therefore low throughput despite very precise separation in some cases, are only suitable for processing small ore quantities, such as in secondary cleaning of concentrates. Sluices for semi-continuous operation are exceptionally well suited for producing pre-concentrates.


Fig.: Various forms of wood and metal or iron riffles and their installation in the source. Source: Silva.


Fig.: Construction designs of sluice washers for intermittent operation; tin and tungsten mining in Bolivia. Source: Priester.


Figures

Fig.: Sluice for semi-continuous operation. Source: Bernewitz.
Fig.: Various types of wooden of stone riffles. Source: Stout.

14.7 Ground sluice

Metal Mining, Alluvial Gold Mining
Beneficiation, Sorting

germ.:

Erdrinne

span.:

canaletas naturales, suceo in Potosi, canalon natural

TECHNICAL DATA:

Dimensions:

approx. 1.5 × 1.5 × 200 - 300 m, up to 100 m elevation drop

Weight:

built into the ground

Extent of Mechanization:

not mechanized

Form of Driving Energy:

water and slurry flow

Mode of Operation:

intermittent

Throughput/Capacity:

approx. 10 t/min (ground sluices in Potosi)

Operating Materials:


Type:

water

Quantity:

large quantities

ECONOMIC DATA:

Investment Costs:

high construction costs

Operating Costs:

possibly high water costs

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Personnel Requirements:

low

Location Requirements:

large elevation difference (vertical drop) and water necessary

Grain Size of Feed:

unclassified waste-dump material

Special Feed Requirements:

high density difference between valuable mineral and host material

Recovery:

very low, estimated value: < 10 % in Potosi, < 50 % in Colombia

Regional Distribution:

Potosi,Bolivia; alluvial-gold mining in Colombia

Operating Experience:

very good |————|————| bad


locally good

Environmental Impact:

low |————————| very


high relatively high quantities of waste sludge, very large space requirements

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

masonry work only

Lifespan:

very long |————|————| very short

Bibliography, Source: Priester

OPERATING PRINCIPLE:

Sluice washing with fluctuating ground and elevation characteristics in which unclassified feed flows torrentially downward as sludge. The material which settles out onto the ground serves as a pre-concentrate for further processing.

AREAS OF APPLICATION:

For production of pre-concentrate from unclassified waste-dump material at Cerro Rico de Potosi, Bolivia.

For production of pre-concentrate in alluvial gold mining In Colombia.

REMARKS:

Due to the low degree of liberation of the sluiced material, it can only be expected that this process yields to a very low recovery of valuable minerals. In addition, processing activities in ground sluices burden the receiving stream with high sludge loading. Only a few topographical conditions allow the construction of ground sluices, since the sluice feed-input point must lie within close proximity to the raw-material deposit. Any necessity to transport the raw-material renders this already inefficient process uneconomical.

In gold mining In Colombian Barbacoas, similar ground sluices (canalones naturales) are likewise being used for the production of pre-concentrates. Gold-containing sediment, rinsed with low-pressure water, flows as a muddy slurry through the ground sluice, which is subdivided by stone riffle-like barriers. The pre-concentrate which collects in front of these stone barriers is repeatedly loosened and cleaned with the help of almocafres (scraping hooks) and cachos (wooden scrapers for removing the stones).

SUITABILITY FOR SMALL-SCALE MINING:

Applicable only under the special conditions present in Potosi, Bolivia; not transferable to other beneficiation plants or local conditions.

14.8 Pinched sluice, fanned sluice

Metal Mining, Alluvial Gold Mining
Benefication, Sorting

germ.:

Facherrinne

span.:

canaleta en forma de abanico, canaleta abanica

Manufacturer:

Taller Metal Mecanico

TECHNICAL DATA:

Dimensions:

0.5 × 0.5 × 1.5 m HWD

Weight:

approx. 25 kg

Extent of Mechanization:

not mechanized

Form of Driving Energy:

only processing water

Mode of Operation:

continuous

Technical Efficiency:

concentrates to a factor of 2 or 3 per charge (processing cycle)

Operating Materials:


Type:

water

Quantity:

< 50 I/min; 30 - 45 % by weight

ECONOMIC DATA:

Investment Costs:

approx. 150 DM

Operating Costs:

low

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Personnel Requirements:

low

Location Requirements:

water and Dh (elevation gradient) required

Grain Size of Feed:

100 µm - 1 mm

Special Feed Requirements:

Proportion of clay fraction in the feed should be < 5 %; valuable mineral grains between 50 ym and 0.5 mm; high density difference between valuable mineral and host material required

Recovery:

depends on degree of concentration

Replaces other Equipment:

other sluice washers, fine-grain Jigs, settling basins or buddies

Regional Distribution:

only as proto-type in Potosi, Bolivia

Environmental Impact:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

wood manufacturer

Lifespan:

very long |————|————| very short


depends on abrasive hardness of feed

Bibliography, Source: Priester, Helfricht, R. Leutz (heavy mineral sand) in: Erzmetall 42, Nr. 9, peg. 383 ff, Silva

OPERATING PRINCIPLE:

Sluices with converging cross-section in which a wide, shallow slurry stream is transformed into a deep, narrow stream. In this process, the heavy material separates out towards the bottom. A dividing blade at the outflow diverts the material flow into light-particle slurry (upwards) and heavy-particle slurry (downwards).

AREAS OF APPLICATION:

For pre-concentration of medium, fine and finest grain fractions.

SPECIAL AREAS OF APPLICATION:

For homogenizing and pre-concentrating of slurry prior to sedimentation in settling basins. The use of pinched or fanned sluices can eliminate peaks in flow during classification.

REMARKS:

The small relative difference in velocity between the slurry-material and the processing water allows precise separation even of the fine-grained fractions.

The pinched sluice can be very finely adjusted by varying the inclination, slurry feed and dividing-blade (experience necessary, possibly accompanied by quality-control measures via panning during processing). Rubber or plastic wear-resistant coatings increase the sluice lifespan. Pinched or fanned sluices are in use even in the technologically modern large-scale mining facilities (Cannon, Carpo-Schneider, Reichert Konus).

Concentration with pinched sluices or cone separators is only possible up to levels of 70% heavy-mineral content, since beyond this amount they no longer operate selectively.

The "tray tester" is a system of vertically-stacked pinched sluices, connected in series, in which tailings and concentrate are multiply re-sorted.

In addition to the simple gravity-based pinched sluices described above, these gravimetric-sorting sluices can also be used In combination with other separating processes. One example is the flotation fan-separator which vertically differentiates the material into float and non-float components through the use of reagent additives (to enhance flotation selectivity) and by injecting air through a fine metal mesh in the upper portion of the sluice where the slurry-feed flow is still flat; at the end of the sluice, these two flow components are separated by a dividing blade. Another example is found in the beneficiation of magnetic iron ores, where a magnetic pinched sluice is employed which is equipped with magnets installed underneath the sluice bottom to intensify the separation of heavy and magnetic ore particles into the underflow.

SUITABILITY FOR SMALL-SCALE MINING:

Pinched or fanned sluices are well suited for various processes in small-scale mining (production of pre-concentrate, homogenizing of settling-basin feed, etc.). Continuous, drive-less operation and a simple construction which can easily be produced locally are essential characteristics of pinched sluices.


Fig.: Special types of pinched sluices: left, flotation pinched separator; right, magnetic pinched sluice. Source: Helfricht.


Fig.: Side view, top view, and front view of pinched sluice. Source: Priester.


Fig.: Operating principle of a cone separator. Source: Robinson.


Fig.: Flow-path of material (slurry) in a cone separator. Source: Silva.

14.9 Air separator, dry blower

Metal Mining, Alluvial Gold Mining
Benefication, Sorting

engl.:

dry washer, pneumatic sluice, pneumatic table

germ.:

Aerorinnen

span.:

canaleta neumatica

Manufacturer:

Keene, Oliver Manufacturing Comp., Berry Neu

TECHNICAL DATA:

Dimensions:

2 × 1 × 1.5 m HWD

Extent of Mechanization:

not mechanized

Form of Driving Energy:

manual drive or pedal drive, drive 250 min-1 approx. 10 cm amplitude

Alternative Forms:

mechanized with internal combustion engine

Mode of Operation:

semi-continuous

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————————| high

Maintenance Expenditures:

low |————————| high

Location Requirements: .

none, employable even in arid regions

Grain Size of Feed:

< 5 mm; in pneumatic tables between approx. 1 and 50 mm

Special Feed Requirements:

feed must be completely dry; high density difference between valuable mineral and host material necessaryOutput: recovery in fine grain-size range is relatively low

Regional Distribution:

Australia, USA

Environmental Impact:

low |————|————| very high


low pollution from airborne-dust

Suitability for


Local Production:

very good |————|————| bad

Under What Conditions:

wood manufacturer

Lifespan:

very long |————|————| very short

Bibliography, Source: de Bernewitz, Hunter, Stout, Silva

OPERATING PRINCIPLE:

Feed is classified by screening into several fractions. The screens are inclined, and air is blown through them from underneath by means of bellows. This blown air picks up the screened oversize material lying on the screens cloth bottom and suspends it in a turbulent air layer where it is differentiated according to density. The material flow is induced by the screens inclination, whereby the heavy fraction is caught by riffles and the lighter material is discharged over the riffles.

AREAS OF APPLICATION:

Pre-concentration of liberated (comminuted) mine ore in arid regions.

REMARKS:

By mounting the screens onto a flexible steel construction, a shaking movement can be incorporated into the system.

Besides dry blowers, dry vibrating sluices are also used in arid regions. Since a fluidized bed (turbulent air layer) is not generated in these sluices, the separation precision and recovery of valuable minerals are correspondingly lower.

Pneumatic tables:

Pneumatic tables are used for benefication of dry feed (e.g. gold sands in arid regions or coal) in high throughput quantities. Pneumatic tables consist of a screen bottom permeated by a forced-air current which suspends the feed material in a stable turbulent air-layer (fluidized bed). The inclination of the screen as well as applied impact-forces cause the suspended feed material to separate into a light-material zone and heavy-material zone. The comparably high energy consumption as well as the high proportion of airborne dust generated which characterize this process call for the use of a closed-circuit air-flow system, or an intermediary cycloning or dust removal in a dust-collecting chamber with dust collector. The fact that pneumatic gravimetric-separated concentrates do not require subsequent drying is advantageous; the low separation precision is disadvantageous.

Air separation:

Another important pneumatic sorting technique is air classification. The material falls through an air current, whereby the lighter particles are deflected over a greater distance due to their larger surface: weight ratio than are the heavier particles. The flow components can be separated by the use of dividing blades. Air classification can be employed for separating narrowly. classified (narrow-band), totally dry, fine feed; however, the extremely large quantities of dust generated during processing pose enormous environmental problems. The use of cyclones, wet air-washing, or completely covered plants where the processing air flows in closed circuits can reduce dust pollution, but raise processing costs accordingly.

Pneumatic dry washer:

Pneumatic benefication, for example for use in arid regions, can be performed by means of pneumatic pinched sluices where air is blown through a cloth bottom creating a fluidized bed which suspends the feed material and classifies it analogous to the pinched hydro-sluice principle. High density difference and narrowly-classified feed granulation are prerequisites for successful sorting. Pneumatic pinched sluices are employed for pre-concentrating.

SUITABILITY FOR SMALL-SCALE MINING:

Well suited for application in arid regions, especially for the processing of low-grade precious-metal ores (such as the recovery of gold from laterites); simple apparatus which can be locally manufactured.


Fig.: Sorting in air current; left, air classifer for grain; right, mineral sorting in air classifer. Source: Fischer.


Fig.: (right) Pneumatic sluice. Source: Silva.


Fig.: (below) Pneumatic table. Source: Ackthun.


Fig.: Manual pneumatic sluice. Source: Stewart.


Fig.: Dry vibrating sluice. Source: Bernewitz.

14.10 Settling basin, buddle

Metal Mining, Coal Mining
Beneficiation, Sorting

engl.:

conical table

germ.:

Schlammgrube, Sandrundherd, Kegelherd, runder Liegendherd, liegender Rundherd

span.:

buddle redondo, rumbulo, rumbo, phurmuchina, plataforma conica, plataforma, redonda de concentracion

TECHNICAL DATA:

Dimensions:

approx. 2 m 0, 1 m H, 6.3° angle of opening

Weight:

mostly built into the ground; above-ground parts approx. 20 kg

Extent of Mechanization:

not mechanized

Form of Driving Energy:

only processing water

Mode of Operation:

semi-continuous

Throughput/Capacity:

up to approx. 1000 kg/h

Operating Materials:


Type:

water

Quantity:

up to 751/min

ECONOMIC DATA:

Investment Costs:

approx. 300 - 350 DM, less expensive if self made

Operating Costs:

insignificant, labor costs only

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Personnel Requirements:

low

Location Requirements:

water and min. Dh of approx. 1 m necessary

Grain Size of Feed:

50 ym - 2.000 ym

Special Feed Requirements:

high density difference between valuable mineral and host material

Recovery:

Averages about 50 % as concentrate, 25 % as middlings, 25 % as waste material, whereby the material is frequently recycled (reprocessed) in order to increase concentrate contents.

Replaces other Equipment:

tables, sluices

Regional Distribution:

Peru, Bolivia

Operating Experience:

very good |————|————| bad


in association with flotation in settling basin

Environmental Impact:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

maasonry construction, wood manufacturer

Lifespan:

very long |————|————| very short


extremely long

Bibliography, Source: Priester, Alfeld, Gaetzschmann, B+H.Z 1865, Linkenbach, Callon

OPERATING PRINCIPLE:

The slurry-feed is placed into the center of a flat sedimentation cone (conical table, buddle). The geometrical form of the sedimentation chamber causes a decrease in slurry velocity as it flows outward toward the table perimeter, which results in a sedimentation of the slurry material: fine heavy-material (with small surface-area exposed to the flow forces) settles in the middle, then coarser heavy-material, further out the fine light-material and at the periphery coarse light-material. The silty fines remain suspended and are carried off. Homogeneous conditions for sedimentation are achieved by damming or retaining the slurry in order to regulate the feed level. The products are extracted manually, with shovels, in concentric rings following completion of the separation process and after the material has dried.

AREAS OF APPLICATION:

Sorting of fine feed. Sorting of waste from sorting tables.

SPECIAL AREAS OF APPLICATION:

Flotation to separate sulfide impurities from oxidic concentrates using sulfuric acid, diesel oil and xanthate. Air-water interfaces occur in the centrally-located slurry feed input.

REMARKS:

- for homogenizing and slowing the slurry flow, bundled grass stalks (chorros) are place at the slurry input point,

- to simplify the damming of the slurry flow in the sedimentation chamber, weirs made from metal sheets or wood can be employed.

- throughput can be increased by simply dividing the slurry feed and processing the separate flows simultaneously in parallel-arranged buddies,

- invented about 1840 in England by Hughes/Ball (Zeitschrift fur das Berg-, Hutten- und Salinenwesen 1865, 22), 1842 by Taylor (Gurlt),

- the round buddle (Linkenbach table) is similar to the type of conical table used in Bolivia; it varies regarding feed Input and homogenization, which are performed by means of a rotating mechanism from which cloths or brooms are hung. This reduces the extent of turbulence at the feed-input point.

To assess the quality of the product, the traditional mill worker uses a shovel as a panning dish to analyze the contents of the heavy minerals at the perimeter of each respective sedimentation ring. In this way the diameter of the respective concentric rings of concentrate, middlings and waste material can be established for product extraction.

The inclination of the cone angle significantly influences the concentrate content and the recovery. Optimal values can be achieved when the inclination of the conical table (buddle) equals that of the growing sediment cone. This varies depending on grain size, distribution of minerals and throughput of slurry. The finer the feed or the smaller the density difference between valuable and non-valuable minerals, the flatter the inclination of the sediment cone becomes towards the perimeter.

In Bolivian tin and tungsten-ore vein deposits the optimal cone angles are around 6.3°.

Regarding the processing procedure, the process flow sheets vary according to whether classification occurs before or after separation processing; i.e. whether an already-classified feed of narrow grain-size range is fed into the separation equipment (Harzer method), or whether a feed of broad-ranged granulation is processed, in which case classification is subsequently performed to remove the host or waste material (screened overs) from the concentrate (Anglo-Saxon method).

SUITABILITY FOR SMALL-SCALE MINING:

In general, the settling basin or buddle is very suitable for wet mechanical fine-grain sorting in small scale mining. It is also quite suitable for secondary separation of sorting-table tailings. The settling basin is characterized by its simple, low-cost construction which does not involve any moving parts.


Fig.: Conical table or buddle. Source: Callon.


Fig.: Top view and cross-section of a Bolivian setting basin. Source: Priester.


Fig.: Work-chronogram of sorting process in Bolivian setting basin. Source: Priester.


Fig.: Mechanized buddle. Source: Linkenbach.

14.11 Circular buddle

Metal Mining
Beneficiation , Sorting

germ.:

Hundt'scher Trichterherd, mechanisierte Schlammgrube

span.:

buddle conico de Hundt, buddle conico, buddle circular

TECHNICAL DATA:

Dimensions:

star-form with four or six channels/cloths, approx. 4 m in diameter, 2 m in height, 3.2° inclination, volumetric capacity approx. 7 - 14 m³

Weight:

mainly built into ground, above-ground components approx. 300 kg

Extent of Mechanization:

semi-mechanized

Power:

approx. 0.5 - 1 PS, 11 min-1

Form of Driving Energy:

mechanical via transmission from electric motor

Alternative Forms:

hydromechanic

Mode of Operation:

semi-continuous

Throughput/Capacity:

300 - 1000 kg/in at relatively low concentration factors

Operating Materials:


Type:

water

Quantity:

up to 100 I/min.

ECONOMIC DATA:

Investment Costs:

minimum of 1000 DM without drive unit if self-constructed

Operating Costs:

energy costs, labor costs, very low wear

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Personnel Requirements:

low

Location Requirements:

running water and min Dh of approx. 1.5 m necessary

Grain Size of Feed:

10 ym - 200 ym

Special Feed Requirements:

high density difference between valuable mineral and host material

Recovery:

probably lower than in settling basin due to small grain sizes

Replaces other Equipment:

settling basin, buddle

Regional Distribution:

currently only rarely found in Bolivia

Operating Experience:

very good |————|————| ad

Environmental Impact:

low |————|————| very high


large space requirement

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

metal and wood workshops, masonry construction

Lifespan:

very long |————|————| very short

Bibliography, Source: Priester, Gurlt, Liwehr, Hundt, Pieler, Koecke, Rittinger

OPERATING PRINCIPLE:

Buddle with peripheral input of slurry feed by means of a star-shaped, slowly-rotating hub with radial channels. The slurry flows down the outer wall into the funnel-shaped sedimentation chamber. The very low slurry velocity allows sedimentation and sorting of the finest-grained feeds. In mechanized buddies the heavy material sediments at the outer perimeter, with light material and water discharging at the center.

AREAS OF APPLICATION:

Sorting of finest feed. Secondary separation of tailings from sorting tables.

REMARKS:

Long work-cycles are possible due to the large volumetric capacity. Parallel-connected mechanized buddies increase the plant throughput Extremely well suited for gravimetric-hydrodynamic beneficiation of the finest fractions, which especially In tin and tungsten ore processing contain high proportions of the valuable mineral.
Invented by Hundt in 1858 in Siegerland (Germany) and tested in Ramsbek. Results indicated higher throughput quantities than with non-mechanized buddies (settling basins) as well as significantly higher valuable-mineral content In the concentrate, but only slightly higher total recovery. Apart from a few minor details (slurry feed input, non-linear separation-chamber profile), the mechanized buddies in Bolivia have exhibited the same design for 130 years!!

According to Hundt, only one person is required to operate 3 to 4 circular buddies.
Advantages compared to non-mechanized buddies are:

+ low water requirements
+ low motive power required
+ low cost for masonry construction

Driven by 2-meter high water-wheel with a very low quantity of propelling water (Pieler).
The selectivity of buddies sinks in direct proportion to the solid feed content of the slurry, which makes circular buddies more suitable for pre-concentrating purposes than for final sorting. To achieve concentrate with high valuable-mineral contents, the feed has to be reprocessed as much as six times.

SUITABILITY FOR SMALL-SCALE MINING:

Mechanized buddies represent the only known wet-milling, fine-grain sorting processincluded in traditional small-scale mining beneficiation techniques. A drive system is necessary for mechanization.


Fig.: Mechanized buddle. Source: Liwehr.


Fig.: Buddle from Bolivian tin mining. Source: Priester.

14.12 Dolly tub

Metal Mining
Beneficiation, Sorting

engl.:

tossing tub, kieve, agitator

germ.:

Raffinationstonne nach dem Schanzverfahren, Schlammfa�, Engl. Ruhrfa�, Ruhrwerk, Stauchkasten

span.:

tine de refinacion, tine de levante, tine de refinacion segun el proceso de Schanz, tine de deslame, cajon de asentamiento

TECHNICAL DATA:

Dimensions:

metal barrel or tub, 50 - 150 lifers in volume

Weight:

approx. 10 - 30 kg

Extent of Mechanization:

not mechanized

Form of Driving Energy:

manual

Alternative Forms:

possibly hydromechanic ?

Throughput/Capacity:

1 - 6 kg/min

Operating Materials:


Type:

water

Quantity:

< 51/min

ECONOMIC DATA:

Investment Costs:

nominal Operating Costs: labor costs only

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Personnel Requirements:

low

Location Requirements:

none

Grain Size of Feed:

20 - 2,000 µm

Special Feed Requirements:

density difference between valuable mineral and host material

Output:

an average of 60 % as concentrate, tailings are reprocessed

Replaces other Equipment:

sluices, buddies

Regional Distribution:

Bolivia, formerly widespread throughout Central Europe, initally as sorting apparatus, later used only for drainage purposes

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Lifespan:

very long |————|————| very short

Bibliography, Source: Priester, Schennen, Treptow, Villefosse, Althaus, Zirkel

OPERATING PRINCIPLE:

Feed is mixed with water (at a ratio of 1: 1 by weight) and homogenized by agitating. Through impact pounding on the barrel the sediment becomes thixotrope and begins to flow. A sink-float process then begins in the high-density slurry, with lighter material floating upward and heavier material sinking downward. After several minutes, the water is decanted. The consolidated sediment is vertically differentiated according to density' end is selectivly removed by means of a spatula.

AREAS OF APPLICATION:

Secondary cleaning of concentrates from sluices and settling basins or buddies.

REMARKS:

As a result of the very minimal motion of the water, the finest grains can also be selectively separated with a high degree of precision. Even materials exhibiting a low density difference between valuable and waste material can successfully be processed with this technique.
Results can be improved if a suitable bottom material, such as rubber matting, is used (less wave adsorption as when directly on the ground).

In mechanized form, the dolly tub by Villefosse (from England) is known. The impact forces were induced by means of a camshaft, initially driven hydromechanically, later via steam engines.
Shock-absorbing devices appropriate for vibrating presses can be made from car springs (need for research and development).

Establishing the boundary between middlings amd tailings and between concentrate and middlings is determined by product control with a batea (panning principle).

SUITABILITY FOR SMALL-SCALE MINING:

The "Schanz-method" dolly tub is suitable for use in non-mechanized mines as a secondary-cleaning or dewatering apparatus for processing valuable concentrates (e.g. tin, wolframite, or silver concentrates). Investment costs are extremely low and the separation precision very high even for fine grained material.


Fig.: Work-chronogram of sorting steps in tossing tub with "Schanz" method. Source: Priester.


Fig.: Tossing tub. Source: Schennen.


Fig.: Tossing tub. Source: Treptow.

14.13 Bumping table, concussion table

Metal Mining
Beneficiation, Sorting

engl.:

concussion table, percussion frame

germ.:

Sto�herd

span.:

mesa de concentracion a golpes, mesa de sacudimientos, mesa de concentracion, mesa de golpe

TECHNICAL DATA:

Dimensions:

3 m in length, 1.2 m in width

Form of Driving Energy:

hydromechanical drive most appropriate due to the relatively low rated speed of the shaking table

Alternative Forms:

electromechanical drive, mechanical drive via internal combustion engine, manual drive, pedal drive

Throughput/Capacity:

approx. 250 kg/Mh (including charging of feed and drawing of products)

Technical Efficiency:

higher than in vanners (belt table); very fine heavy materials, for example < 20 µm gold-ore grains, are also recovered in the concentrate.

Operating Materials:


Type:

water

Quantity:

approx. 50 - 80 % by weight

ECONOMIC DATA:

Investment Costs:

bumping tables can be produced locally at very low cost. For example, in a Colombian pilot-plant, a bumping table with 0,65 × 1,5 m table-size could be constructed for 250 DM without camshaft or drive-unit.

Operating Costs:

energy costs, labor costs

Related Costs:

possibly thickener

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high


lower in comparison to vanners (belt tables)

Maintenance Expenditures:

low |————|————| high

Personnel Requirements:

one man can operate three bumping tables; table adjustment requires experience.

Grain Size of Feed:

between around < 10 µm and 1,000 µm - 2,000 µm

Output:

According to test results by Althaus, the concentrate-contents, recovery and throughput quantities are higher than with vanners: 3 bumping tables: 3300 kg ore, 48 h, 552 kg Pb-concentrate with 53.0 % Pb (296 kg Pb) 1 M/3 h 3 vanners: 3300 kg ore, 60 h, 643 kg Pb-concentrate with 45.5 % Pb (292 kg Pb) 2 M/3 h

Replaces other Equipment:

shaking tables, buddies, some sluices

Regional Distribution:

earlier widely known

Operating Experience:

very |————|————| good bad

Environmental Impact:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

good wood manufacturer

Lifespan:

very long |————|————| very short

Bibliography, Source: Gurlt, Schennen, Treptow, Wagenbreth, Fisher, Villefosse, Althaus

OPERATING PRINCIPLE:

A bumping table (percussion frame) is a flat rectangular sedimentation basin. At the feed-input side, the slurry is homogeneously distributed onto the table with the help of a knubbed wooden board. The slurry then flows over the longitudinally-inclined table. Heavy material settles out in proximity of the feed input-point whereas lighter material remains suspended and is carried out with the float. To increase the precision of separation, the material is loosened by pounding on the table surface in the longitudinal direction. In so doing, the suspended table is deflected by a camshaft and swings back under its own weight against a buffer. The impact forces are transmitted with varying intensity to the feed material on the table. Consequently,the horizontally density-differentiated material comprises separate counter-current flow components: the heavy material Iying directly on the table surface receives the strongest impulse and is set into upward motion against the slurry flow. The overlying lighter material receives a dampened impulse, which combined with its closer proximity to the overlying water current, causes it to be moved in a downstream direction with the flow. From time to time, the entire material on the table should be swept upstream toward the feed-input end to avoid possible undesired loss of valuable mineral.

After a sufficiently long sorting duration, the input of slurry feed is interrupted so that the concentrate can be extracted by shovels, spatulas or brooms and stockpiled for reprocessing.

AREAS OF APPLICATION:

Bumping tables are used for sorting of medium and fine-grained feed containing heavy minerals such as galena, wolframite, tin ore, gold, etc.

REMARKS:

Bumping tables were developed from enlarged bateas (panning dishes) and originate from Bohemia, having expanded to Hungary by 1770; also known in Germany by 1772 through the mining engineer Schmidt in Freiberg silver mining.

Bumping tables were employed until the beginning of this century in Central Europe, primarily in the German mining regions of the Harz Mountains and Saxony.

A very significant design detail of the bumping table is the installation of a wooden board at the feed input point in an attempt to achieve a homogeneous distribution of slurry over the entire width of the table. Typical historic designs for these boards are shown on the following page.

The great advantage of bumping tables are their easy regulation of the processing conditions through the very quickly adjustable table inclination, through the frequency and intensity of impacts, and the quantity of feed slurry.

Of importance for high separation precision is to maintain a homogeneity in the slurry-feed quantity and particularly in the density, since fluctuations in these parameters cause variations in transport conditions of the discharge flow.

Bumping tables are differentiated according to those with solid buffers and those with elastic buffers. The bumping tables equipped with solid buffers operate with comparably greater separation precision when density differences In the feed (valuable mineral vs. host material) are sufficiently high; however, they consume more energy with lower throughput quantities.

SUITABILITY FOR SMALL-SCALE MINING:

Bumping tables are very suitable for filling the technical gap between buddies and shaking tables. The simple and stable construction combined with simple (but inefficient) drive systems permits local manufacture of the apparatus at low investment costs compatable with small-scale mining budgets.


Fig.: Bumping table (Freiberger Langsto�herd or "long bumping table"). Source: Treptow.



Fig.: Various designs of boards for homogenizing and distributing the feed. Source: Schennen (left); Liwerhr (right).


Fig.: Bumping (concussion) table. A: table; B: roller to adjust table inclination; C: rod that is moved by spiral disc D; E and E': buffer, E on table and E' on frame, G: sluice (washing trough), K: ore concentrate, shoved to right side when table rebounds and when E and E' strike; T: barren material flushed our by water into G. Source: Wagenbreth.


Fig.: Bumping (concussion) table. Source: Schennen.

14.14 Racking table, tilting frame

Metal Mining
Beneficiation, Sorting

germ.:

Kippherd

span.:

mesa de concentracion inclinable

TECHNICAL DATA:

Dimensions:

similar to vanner (belt table), approx. 2 - 6 m in length, 1 - 2 m in width

Extent of Mechanization:

not mechanized

Form of Driving Energy:

only processing water or slurry

Mode of Operation:

semi-continuous

Throughput/Capacity:

low, can be increased with multiple-deck table

Operating Materials:


Type:

water for flushing

ECONOMIC DATA:

Investment Costs:

approx. 1500 DM if self-made

Operating Costs:

labor costs only

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures

low |————|————| high

Personnel Requirements:

operating experience required

Location Requirements:

large quantities of water must be available

Grain Size of Feed:

0.1 - 2 mm

Special Feed Requirements:

high density difference between valuable mineral and host material

Recovery:

comparable to that of vanners (belt tables); throughput is higher due to ease of extracting products

Replaces other Equipment:

vanner (belt table), mechanized buddle

Regional Distribution:

historic technique

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

wood manufacturer

Lifespan:

very long |————|————| very short

Bibliography, Source: Zirkel

OPERATING PRINCIPLE:

Racking tables or tilting frames function similar to vanners (belt tables): the feed material settles out onto a slightly-inclined (longitudinally) sedimentation surface, with grains of higher specific density sedimenting closer to the feed-input point and grains of lower specific density settling out further downstream, the distance being proportional to the density. When the table-surface capacity is reached, the charging cycle is interrupted and the table tipped along its longitudinal axis. Supplementary water rinses the surface free of material, whereby the grains are separated by dividing plates into various catching compartments. Upon completion of the rinsing step, the table is tipped back into the original horizontal position and the process continues with renewed input of feed.

AREAS OF APPLICATION:

Tables of this type were widely used in tin mining in Cornwall (England) in the last century.

REMARKS:

Zirkel describes a design in which the table is connected to a water channel by a chain, so that the tipping action automatically releases the supplementary water used to flush the products from the table.

Modern racking tables with multiple-deck (vertically stacked) and possibly a swinging system (Bartles-Mozley table) are employed for sorting the very finest heavy-mineral feeds (5 - 100 ym).

SUITABILITY FOR SMALL-SCALE MINING:

Racking tables (tilting frames) in the form of multiple-deck tables are appropriate for small-scale mining for extraction of valuable minerals from the finest grain fractions.


Fig.: Operating principle of a simple racking table. Source: Priester, according to Zirkel.

14.15 Sweeping table, belt table

Metal Mining, Gold Mining
Beneficiation, Sorting

engl.:

vanner, blanket (corduroy) table, Brunton table, animal pelts

germ.:

Kehrherd, Planenherd, Bruntonherd, Tierfelle

span.:

mesa de concentracion de limpieza manual, bayetas, pangs, tableros, mesas rayadas, mesa de concentracion con pano, mesa de concentracion brunton, pieles de animal

TECHNICAL DATA:

Dimensions:

7 m in length, 1.2 m in width, Brunton table 3 × 1 m

Extent of Mechanization:

not mechanized/semi-mechanized/fully-mechanized

Form of Driving Energy:

only slurry flow, Brunton table by electric or mechanical drive, with or without vibrator

Mode of Operation:

intermittent/semi-continuous

Throughput/Capacity:

according to Althaus: approx. 100 kg/Mh Including feed input, product extraction, etc.; 3 m corduroy table: approx. 100 t/24 h

Operating Materials:


Type:

water

ECONOMIC DATA:

Investment Costs:

approx. 200 DM when self-made

Operating Costs:

labor costs only (excluding powered Brunton table)

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————————| high

Maintenance Expenditures:

low |————|————| high

Personnel Requirements:

experience in adjusting tables is necessary

Location Requirements:

water and sufficient elevation difference required

Grain Size of Feed:

approx. 0.05 - 2 mm

Special Feed Requirements:

high density difference between valuable mineral and host rock

Output:

the recovery from rigid tables is significantly less than that achieved with vibrating or shaking tables. The geometry of the sedimentation chamber creates practically constant settling conditions in the longitudinal direction. As a result, the separation precision of this sorting apparatus is highly limited; comparison can be made with the bumping (concussion) table (research results from H. Althaus).

Replaces other Equipment:

sluices, tables, amalgamation tables

Regional Distribution:

corduroy (blanket) tables widely distributed in gold mining in Ecuador and Colombia; historically distributed worldwide

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

simple carpentry or masonry construction

Lifespan:

very long |————|————| very short

Bibliography, Source: Schubert, Treptow, Reitemeier, Villefosse, Althaus, Ullmann, Crennell, Plinius en Moesta, Agricola, Priester, v. Bernewitz, Libro de Inventos 1890, Medina/Peru

OPERATING PRINCIPLE:

A separating table, slightly inclined along the longitudinal axis, serves as a sedimentation surface for valuable-mineral grains of high specific density and for those grains in the feed which exhibit mineral-waste intergrowths. Table inclination and slurry volume are the parameters influencing the cut-off density of the separation process. After completion of sedimentation, charging of feed is interrupted and the concentrate near the feed-input point is swept together and removed. Middlings settle out further downstream from the feed intake.

For sorting of the very finest fractions, the table surface is covered with coarse cloth towels which enhance the sedimentation of heavy material. The towels are washed following sedimentation and spread out again so that the entire table surface is covered. Corduroy was the commonly-used material for lining the corduroy or blanket table. Later, riffled rubber linings (thickness 10 mm, riffle depth 3 mm, riffle interval 6 mm) were widely used.

Mechanized processing plants employ endless rotating belts in the so-called Bruton tables, in which the sorting surface is inclined 11 and the belts move at around 0.4 m/min in the opposite direction to slurry flow. Above the slurry feed, the concentrate is continually rinsed. Continuous-operating belt tables have also been constructed as slow-rotating drums (e.g. 3.6 m length, 0.9 m 0, 3.75° inclination) with riffled rubber linings.

Cow hides are used for the winning of cassiterite (tin ore), analogous to the "Golden Fleece" of the Kolchier for winning gold, they are employed during beneficiation of very fine sludge or silt to recover the valuable minerals. The heavy ,-trains are trapped between the hairs of the hide and are recovered during subsequent washing of the hide. After several applications, the hide is then burned and the ashes further processed to extract any remaining valuable-mineral fines.

Sludge trough, German square buddle (in Bolivia: buddle quadrado)

Sluice-type buddle with square or trapezoidal cross-section measuring approx. 2 × 1 × 1 m and a preceeding sedimentation chamber. Coarse concentrate settles out in the first sedimentation chamber, and sedimentation and classified sorting of fine. grained feed (100 - 2000 ym) occur In the second sedimentation chamber, analogous to settling basins (round buddies). Due to the geometry of the grains in the slurry feed, there is only a nominal change in the slurry velocity, resulting in poor separation precision.

AREAS OF APPLICATION:

For sorting of fine and finest grains from heavy-mineral slurries, e.g. tin, tungsten or gold mining. For extraction of heavy minerals from the finest mud or silt.

REMARKS:

Already at the time of the early Egyptians belt tables were employed for sorting silver, gold and copper ores.

The "buddle quadrado" that is applied in Bolivia represents a simple construction of a belt table.

Belt tables should be constructed in such a way that a simple mechanism allows the adjustment of table Inclination, for example by a one-sided suspension. This allows the inclination to be adjusted according to feed parameters or the desired separation cut-off size. Inclination angles range between about 1: 10 (approx. 6°) and 1: 120 (approx. 0.5°). The finer the grain-size of the feed or the lower the separation density, the smaller the sedimentation inclination angle needs to be.

In place of animal hides, industrially-produced textiles such as corduroy or similar material are suitable. This technique was widely distributed in North American gold mining for a while. Animal hide or corduroy sluices or tables are independent of the pH-value of mine water, contrary to amalgamation tables.

Cow hides were used for winning gold from alluvial deposits in Brazil up until the beginning of this century.

Reports of artisan gold mining in Peru mention the extraction of pre-concentrate from "empedrados", which are simple artificial gold traps built by packing stones together in the river bed during periods of low water level. These "chacras de oro" are then collected following the rainy season, and this pre-concentrate then further concentrated with the help of sheepskins spread on sorting tables. In this way, as much as 4 9 of gold could be won from each m² of "empedrados" or stone barrier.

SUITABILITY FOR SMALL-SCALE MINING:

Fixed, rigid tables are suitable especially for processing low-grade ores with high-density valuable minerals (e.g. in the beneficiation of tin-ore, tungsten or gold). For the processing of high-grade ore feed or pre-concentrates, the discontinuous operation which is characteristic of this techniques offers only limited throughput.


Fig.: Sluice-type buddle, simple belt table. left: from Treptow; right: from Priester.


Fig.: Belt table (left) and corduroy table (right). Source: Agricola.


Figures

Fig.: Concentrating table. Source: Treptow
Fig.: Endless-belt table, Bruton table. Source: Schennen


Fig.: Concentrating table. Source: Callon.


Fig.: Sweeping table. Source: Agricola.

14.16 Vibrating table

Metal Mining, Gold Mining
Beneficiation, Sorting

engl.:

shaking table, wifley table

germ.:

Schwingherd, Wilfleyherd, Schuttelherd

span.:

mesa de concentracion vibradora, mesa concentradora, mesa de concentracion de Wilfley

Manufacturers:

Millan, Denver, Keene, Mineral Deposits, Wedag, Wilfley Mining, Mozley,Svalcor, Talleres J.G, Eq. Ind. Astecnia, Buena Fortuna, COMESA, FAHENA, FIMA, Magensa, SOTEEL

TECHNICAL DATA:

Optimal technological characteristics and operating parameters of vibrating tables for the processing of tin, tungsten and similar ores (by Isaev):

Characteristics

Sand table

Fine sand table

Slime table


(1 - 3 mm)

(0.2 - 1 mm)

(<0.2mm)


(shaking or bumping table)

(bumping table)

(bumping table)

Ratio of length to width of table

approx. 2.5

approx. 1.8

< 1.5

Lift in mm

16 to 26

12 to 18

6 to 12

Number of strokes in min-1

200 to 270

270 to 320

320 to 420

Lateral inclination of table surface in degrees

4 to 10

2 to 4

1 to 2.5

Longitudinal inclination of table surface in mm

20 to 30 (incline)

10 to 20 (incline)

1 to 10 (decline)

Fluid-solid ratio (vol) of feed

3.5:1 to 5:1

3.5:1 to 4:1

3.5:1 to 4:1

Cross-flow water quantity (fluid-solid volumetric ratio)

1:1 to 1.5:1

1.5:1

2:1

Height of riffles at drive-side in mm

26 to 18

18 to 12

12 to 8

Interval between riffles in mm

30 to 45

25 to 40

30 to 45

Throughput in t/h

4 to 2

2 to 0.9

0.8 to 0.2

Dimensions:

approx. 4.3 × 1.9 × 1 m LWH, also smaller as bench-scale, laboratory scale, or special tables

Weight:

approx. 500 - 1000 kg for large concentration tables

Extent of Mecanization:

fully mechanized Driving Energy Required: 0.2 - 2 Kw

Form of Driving Energy:

electrical

Alternative Forms:

turbine, internal combustion engine

Mode of Operation:

continuous

Operating Materials:


Type:

water

Quantity:

80 - 85 % by volume

ECONOMIC DATA:

Investment Costs:

9600 US$ (Denver cif La Paz), 2000 US$ (Millan, somewhat smaller)

Operating Costs:

labor costs, energy costs

Related Costs:

milling necessary, hydraulic classification

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Personnel Requirements:

trained personnel

Location Requirements:

water and elevation difference Dh

Srain Size of Feed:

150 µm - 1.5 mm

Special Feed Requirements:

High density difference between valuable mineral and host material is necessary; preliminary hydro-classification of the feed, for example with a cyclone, counter-current classifier, pyramidal cone classifier, etc. is recommended.

Recovery:

only high if tailings are re-sorted by finest-grain sorting equipment such as buddies or mechanized buddies

Replaces other Equipment:

sluices, buddies, spiral separators

Regional Distribution:

worldwide, the most widely distributed sorting system for hydromechanic-gravimetric processing of medium and fine grainded feed; manual tables are rare

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high

Suitability for Local Production:

very good |————————| bad

Under What Conditions:

good carpentry or metal workshops, welding shop, knowledge of vulcanizing, etc. possibly including the use of components made of plastic, rubber, fiberglass, etc.

Lifespan:

very long |————|————| very short

Bibliography, Source: Taggert, Schubert, Manufacturer information, Hunter, Stewart,

OPERATING PRINCIPLE:

Vibrating tables consist of a rectangular or parallelogram-shaped separating surface that is slightly inclined both laterally and in the direction of vibrational movement. The table surface is equipped with riffles which decrease in size with increasing distance in the direction of movement (away from feed input, which occurs at the highest point on the table surface). Supplementary water is applied across the table in a lateral direction along the entire length. Explained simply, the heavy material is less subject to cross-flow forces than the lighter material, so that the feed is differentiated into strips according to density with the heavy material discharging as concentrate over the end, middlings near the lower corner and tailings over the long side.

AREAS OF APPLICATION:

Medium and fine-grain sorting of heavy-mineral feed in solid-rock and alluvial mining of:

- gold
- tin
- tungsten
- antimony
- lead-silver
- zircon

and for separation of industrial-minerals (sand and gravel) pre-concentrates in monacite (cryptolite) and xenotime products.

REMARKS:

Concentration tables made of fiber glass in which the riffles are preformed as negative impressions and inverted during construction are very suitable for local production.

A miniature table is being offered on the prospecting-equipment market (Keene) which operates on 12 V, weighs a total of about 15 kg, and has a throughput of 250 kg/in maximum, making it suitable for secondary sorting of Au-concentrates (price approx. 600 US$).

The table's angle of Inclination has a crucial effect on the separation results. It could often be observed that the table inclination was set incorrectly.

Particularly for beneficiation of gold-containing ores, black rubber-lined tables have proven to be highly advantageous (good visual contrast to gold).

Concentration tables are capable of processing relatively wide-band classified feed (wide grain-size range).

The maximum grain-size of the feed must be smaller than riffle height and smaller than one-third of the interval between riffles.

A disadvantage of this technique, when large throughput quantities or feed containing high proportions of fine-grained material are being handled, is that valuable-mineral fines are carried out with the tailings. In such cases, a subsequent fine-grained separation process must be performed.

Consequently, special gold tables operate with extremely low throughput quantities (for example the Gemini 60 table with 25 kg/m² × h).

Concentrating-table feed should always be hydro-classified prior to sorting to assure adequate separation precision.

The lowest grain-size that can still be sorted with sufficient precision ranges between 20- 100,um, depending on the feed material, whereby the grain shape of the valuable mineral and the density distribution of the minerals play an important role.

The industry has been trying for a long time to develop table sorters that separate in the centrifugal field in order to reduce the sizes of the grains which can be processed (EP 0247 795, EP 0323 447, DE 3309 385). For this purpose, the table surface is rolled to a truncated cone with small opening angle and set into rapid rotation (160 - 240 min-1), creating 10 - 50 kg centrifugal acceleration. Finally the drum is positioned with the opening on top (0° - 5°). The entire unit is subject to a vibrating frequency of 240 - 450 min-1 parallel to the rotational axis and an oscillation amplitude of 1 - 35 cm. The only supplier (Mozley) lists a throughput of approx. 0.2 t/h with a feed grain-size range of 1 to 250 ym.

The very complicated technique for removing the tailings, which involves a rotating raking device and high investment costs of approx. 150.000 DM, render this machine unsuitable for small-scale mining purposes despite the fact that experience from Cornish tin-ore mining, where the multi-gravity separator was employed as a substitution for traditional table separating, shows that comparably high throughput, high recovery and high-grade concentrates can be achieved.

SUITABILITY FOR SMALL-SCALE MINING:

Vibrating tables, employed for mechanized sorting of medium and fine-grained heavy mineral feed, are very suitable for small-scale mining application due to their low energy requirements, high throughput, flexibity and ease of adjustment, and comparably simple operating principle.


Fig.: Wilfley table. Source: Otero.


Fig.: Shaking table. By Schmiedchen.


Fig.: Distribution of the products over the table. Source: Silva.


Fig.: Manual shaking table. Source: Stewart.

14.17 Humphrey's spiral, spiral separator

Metal Mining, Gold Mining
Beneficiation, Sorting

germ.:

Humphreyspirale, Wendelscheider, Spiralscheider

span.:

espiral de Humphrey, espiral de separacion por gravedad, separador helicoidal, espiral

TECHNICAL DATA:

Dimensions:

approx. 1 × 1 × 3 m / 5 to 6 windings / 1 to 3 discharge outlets

Weight:

approx. 200 kg

Extent of Mechanization:

not mechanized

Form of Driving Energy:

velocity of slurry/processing water

Mode of Operation:

continuous

Throughput/Capacity:

0.5 12 t/h depending on dimension of channel (launder) and grain size of feed

Operating Materials:


Type:

processing water, slurry water

ECONOMIC DATA:

Investment Costs:

approx. 8000 DM

Operating Costs:

low

Related Costs:

possibly slurry pumps

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Location Requirements:

minimum Dh (without pump) of 5 m

Grain Size of Feed:

(50 ym) 100 µm - 2 mm

Special Feed Requirements:

density difference between valuable mineral and tailings

Recovery:

solids-content of the slurry: 14 - 20 % by vol.

Replaces other Equipment:

other sluice washers

Regional Distribution:

in small-scale mining in Latin America very rare; widely employed in mining in South East Asia (alluvial tin deposits) and Australia

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

metal foundry

Lifespan:

very long |————|————| very short


when lined with wear-resistant rubber

Bibliography, Source: Kirchner, DBM

OPERATING PRINCIPLE:

Spiral separators vertically separate the feed slurry in the launder (channel) according to density differences. The heaviest feed particles fall to the bottom of the launder, where frictional forces slow their velocity. As a result, the slower, heavier grains are less subject to the centrifugal forces (generated by the flow of slurry through the spiral-formed channel) than are the lighter, faster grains higher up in the flow. This creates a horizontal density differentiation of the feed grains, with the heavy particles flowing along the inside walls of the channel, and the faster, lighter particles travelling higher up towards the outer rim. The discharge outlets are located on the inside of the channel for removal of the heavier particles (concentrate). Separation precision can be improved by adding additional water during the sorting process.

AREAS OF APPLICATION:

Production of concentrates or pre-concentrates from medium-grained Feed.

REMARKS:

The launders (channel) are made of rubberized cast-iron or cast-steel or, in more modern constructions, also of fiberglass or ceramic. The design involves numerous pipes for supplementary-water intake and discharge outlets, making the spiral separator a fairly complicated construction.

Critical construction parameters are: launder (channel) cross-section and spiral diameter, number of windings, inclination and number of discharge outlets.

Spirals of this kind were first manufactured by Humphreys in 1943.

SUITABILITY FOR SMALL-SCALE MINING:

The complicated pipe-system for input of auxiliary water and removal of concentrate makes the Humphrey's spiral less suitable for small-scale mining, although as a continual, non-powered sorting apparatus with high throughput it achieves good separation results.


Fig.: Distribution of mineral particles in the Humphreys' spiral. Source: Silva


Fig.: Humphrey's spirals left, Source: Kirchner, right, Source: Silva.

14.18 Spiral concentrator

Metal Mining, Gold Mining
Beneficiation, Sorting

engl.:

centrifugal spiral classifier, Reichert cone

germ.:

Wendelscheider, Reichertspirale Mark 6+7, Zentrifugal-Fallherd

span.:

concentrador en espiral, separador helicoidal, espiral de Reichert, mesa centrifuge

Manufacturer:

Mineral Deposits, AKW, Svalcor

TECHNICAL DATA:

Dimensions:

3.5 × 1 × 1 m HWD / Fiber glass PU coated

Weight:

43 kg (single channel) - 105 kg (triple channel)

Extent of Mechanization:

semi-mechanized

Form of Driving Energy:

hydrostatic pressure

Mode of Operation:

continuous

Throughput/Capacity:

up to 2 t/h slurry; up to 0.3 t/h concentrate

Operating Materials


Type:

water

Quantity:

40 - 80 % by weight

ECONOMIC DATA:

Investment Costs:

approx. 6000 DM

Operating Costs:

low

Related Costs:

possibly pumps for transport of slurry

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Personnel Requirements:

low

Location Requirements:

water and vertical elevation difference required

Grain Size of Feed:

0.03 - 2 mm

Special Feed Requirements:

depends on type of spiral, e.g., type LG (low grade) < 10 % heavy minerals

Recovery:

according to the Colorado School of Mines Research Institute, concentrates contain between 75 and 98% gold

Replaces other Equipment:

Humphrey spiral, sluices, buddies, fine grain jig

Regional Distribution:

worldwide for mining of alluvial deposits, chromite, etc.

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

difficult, fiber glass construction

Lifespan:

very long |————|————| very short


depends upon abrasiveness of the feed

Bibliography, Source: AKW, C.N. Robinson, Cziernioch, Gaetzschmann, EP 0075563, EP 0074366, EP 0123501, EP 149518

OPERATING PRINCIPLE:

In a 6-phase spiral, density-differentiated side-streams develop as the slurry flows: the heaviest material (concentrate) collects in the deepest part (inside rim) of the channel as a result of being slowed by frictional forces due to scraping against the channel bottom, the medium-dense grain fraction collects in the middle, and the lightest particles (tailings) concentrate at the highest, outermost portion of the channel. The latter grains have the highest flow velocity are are therefore mostly affected by centrifugal force (large radius, high speed). The three stream components are split apart by dividing blades.

AREAS OF APPLICATION:

Processing of pre-concentrate from:

alluvial gold-ore deposits
tin sands and primary tin ore veins
titanous sands (ilmenite, rutile)
zirconium sands
pyrite and other sulfides for leaching
gold from gold-quartz veins
scheelite
chromite

REMARKS:

In contrast to the Humphrey's spiral, this type of spiral (Mark 7) has a much simpler design, lacking the complex pipe system for water intake and concentrate discharge. The slurry flow is first divided into concentrate, middlings and tailings at the end of the spiral channel.

Several channels (2 or 3) can be combined to form a composite of nested spirals.

Gaetzschmann describes a precursor of the spiral concentrator: The centrifugal spiral, invented by Hundt in 1863, had a spiral with a 15° - 25° inclined channel which rotated around a vertical axis whereby the products were differentiated according to density and discharged into separate concentric catchment basins for concentrate (inside), middlings (middle) and tailings (outside).

The most modern design for Reichert cones is characterized by the channel shape which is relatively flat at the deepest point (where the concentrate collects) and becomes wider as the spiral continues downward. This results in a displacement of the separation boundary further toward the outer rim, where the increased centripetal forces have a greater effect on the material being sorted. Simultaneously, the depth of the slurry flow in the region of the channel where the concentrate flows is reduced, causing tangential waves to develop which in turn increase the separation precision by carrying lighter grains outward away from the concentrate region.

In the event that, in the deepest portion (Inner wall) of the channel, a large enough increase in slurry density occurs 60 as to disrupt the sorting process, wedge-shaped reflector or dashboards can be mounted onto the outer channel rim which cause the outer slurry flow to be sprayed evenly over the entire width of the channel (EP 123501).

SUITABILITY FOR SMALL-SCALE MINING:

In poorly mechanized operations, the Reichert cone provides a good opportunity for increasing the efficiency of pre-concentrate production from heavy-mineral feed. Despite comparably high investment costs, it remains suitable for small-scale mining application.


Fig.: Centrifugal spiral, a precursor of the spiral separator. Source: Gaetzschmann.


Fig.: Illustrations of spiral separators: above, left: Triple spiral; above, right: Spiral separator with varying channel channel diameter; below: Dividing plates (splitting devices) for withdrawal of products. Source: Patent No. EP 0075563 and No. EP 0074366.

CLOSE THIS BOOKTools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)
Technical Chapter 15: Gold Benefication
VIEW THE DOCUMENT15.1 Amalgam press
VIEW THE DOCUMENT15.2 Amalgamating table
VIEW THE DOCUMENT15.3 Amalgamating barrel
VIEW THE DOCUMENT15.4 Rocker, cradle
VIEW THE DOCUMENT15.5 Mechanized, compact gold processor
VIEW THE DOCUMENT15.6 Hydraulic gold trap
VIEW THE DOCUMENT15.7 Retort for, amalgam
VIEW THE DOCUMENT15.8 Centrifugal separator
VIEW THE DOCUMENT15.9 Gold pan, batea
VIEW THE DOCUMENT15.10 Jigs with jig bed, russel jig
VIEW THE DOCUMENT15.11 Gold leaching
VIEW THE DOCUMENT15.12 Gold separation by smelting
VIEW THE DOCUMENT15.13 Gold-coal-agglomeration

Tools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)

Technical Chapter 15: Gold Benefication

15.1 Amalgam press

Gold Mining
Beneficiation, Gold Processing

germ.:

Amalgampressen

span.:

prensa de amalgama

Manufacturer:

ASEA, Zutta

TECHNICAL DATA:

Dimensions:

starting at approx. 0.5 × 0.5 × 1 m

Weight:

approx. 40 kg

Extent of Mechanization:

not mechanized

Form of Driving Energy:

manual

Mode of Operation:

intermittent

Throughput/Capacity:

very high, several 100 kg of Amalgam-Hg-mixture per day

Technical Efficiency:

very high degree of separation in comparison to amalgam extrusion performed in cloths without the assistance of a press; residual amalgam contains about 50 - 65 % HgOperating Materials:

Type:

possibly hot water

ECONOMIC DATA:

Investment Costs:

when locally produced approx. 100 DM

Operating Costs:

low

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Effects on Personnel:

high health hazard due to handling of toxic operating materials

Recovery:

very high, < 0.2 % Au remains in the Hg, which is recycled back into the process with the Hg

Replaces other Techniques:

simple extruding without auxiliary apparatuses

Regional Distribution:

very seldom used, to date unknown in developing countries

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————————| very high

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

metal manufacturing

Lifespan:

very long |————|————| very short

Bibliography, Source: Schnabel, Schennen, Villefosse

OPERATING PRINCIPLE:

The Amalgam Press takes advantage of differences in viscosity between pure metallic mercury and the gold amalgam alloy (Au3Hg and Au2Hg, viscous masses). The mixture is pressed through leather (chamois or deer) or dense cloth (such as linen) whereby the amalgam remains completely in the press while pure mercury, with an insignificant quantity of gold (< 0.2 %), is forced through the filter cloth/leather and collected.

AREAS OF APPLICATION:

Separation of amalgam from amalgam-mercury mixtures from amalgamating processes in order to reduce feed quantities entering the distillation retort.

REMARKS:

In small-scale mining in Latin America, the amalgam and Hg are often separated without the use of an Amalgam Press. This involves manually removing the mercury from the thick, paste-like amalgam by squeezing it out the side with the fingers. The amalgam is then wrapped in a damp cloth and wrung, whereby the Hg beads are forced out through the cloth and collected In a batea (pan). The high toxic effects of mercury, combined with the low recovery values obtained, advise against the use of this method.

In Colombian gold mining, the mixture is warmed up in hot water prior to pressing it in order to improve the separation of the amalgam from the mercury. The rise in temperature leads to a reduction in the viscosity of the compound and consequently to a better separation of the individual components as it is forced through cloth or squeezed in a press.

SUITABILITY FOR SMALL-SCALE MINING:

A simply-constructed amalgam press can be produced locally at low cost. Its use reduces health and ecological risks associated with the handling of mercury. For this reason, the small-scale mining industry should implement the use of amalgam presses in combination with distillation wherever amalgamation is being performed.


Fig.: Amalgam Press. Source: Rittinger.

15.2 Amalgamating table

Gold Mining
Beneficiation, Gold processing

engl.:

copper plates

germ.:

Amalgamierherd, Amalgamiertisch

span.:

place de amalgamacion, place electroplateada, mesa de amalgamacion, planca de cobre

TECHNICAL DATA:

Dimensions:

4 × 2 × 1 m WDH and smaller; 2.5° - 12° inclination angle

Weight:

several 100 kg as free-standing apparatus with stand, otherwise constructed on the ground

Extent of Mechanization:

not mechanized

Form of Driving Energy:

only processing water

Mode of Operation:

semi-continuous

Throughput/Capacity:

3 t/d per m², table surface area

Operating Materials:


Type:

water

Hg see comments below

Quantity:

slurry density 20 % solids

>= 50 g/m²

ECONOMIC DATA:

Investment Costs:

when of imported construction with stand, high costs due to copper or muntz metal plates, approx. 10.000 DM; when locally produced with copper plates in masonry sluices built on the ground, less than 1000 DM

Operating Costs:

relatively low, almost exclusively costs of reagents

Related Costs:

subsequent hydraulic heavy-material trap for recovery of discharged amalgam and Hg; sun shade above plates to reduce mercury evaporation.

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Effects on Personnel:

high health risk from handling toxic material

Location Requirements:

water necessary

Grain Size of Feed:

50 µm - 1 mm; good classification necessary to avoid mechanical wear (abrasion) of the amalgam

Special Feed Requirements:

Au must exist as liberated free gold; gold may not be encrusted, for example by limonite; a slightly basic pH-value of the slurry improves the amalgamation

Recovery:

60 - 80 % of the free gold, in the fine grain-size range generally higher than with gravimetric sorting

Replaces otherEquipment:

sluices, tables, amalgamating barrels

Regional Distribution:

earlier widely distributed especially in the USA

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————————| very high


possible sources of environmental contamination are: discharge of large quantities of Hg due to mechanical abrasion of the amalgam and to discharge of foreign-metal amalgams, such as antimony and arsenic amalgam; evaporation of Hg through the water film into the air; discharge of reagents during preparation of the copper plates prior to the amalgamation, e.g., cyanide and silver nitrate

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

good copper plates must be available

Lifespan:

very long |————————| very short

Bibliography, Source: Schnabel, von Bernewitz, Schennen, Clennell, Treptow, Hentschel, Amalgamation ABC, Taggert. Hypolito, Escobar Alvarez and Echeverri Villa

OPERATING PRINCIPLE:

A slurry composed of the liberated, ground feed material flows along the flat, inclined copper plates. The angle of Inclination must be so chosen as to prevent sedimentation of the mineral particles (dependent on the specific density of the heaviest accompanying minerals). Gold flows at the bottom of the slurry flow and is amalgamated by the mercury. The table surfaces are cleaned of the gold amalgam several times daily and prepared anew for the next amalgamation processing.

AREAS OF APPLICATION:

The amalgamation of finely stamped or ground Au ores. The recovery of Hg following amalgamation in stamp mills or Chilean mills.

REMARKS:

- Besides copper plates, muntz metal plates (60 % Cu, 40 % Zn) are recommended.

- The pre-treatment of the plates is complex and time-consuming:



- Polishing with fine sand
- Degreasing using a 1 % Na- or K-cyanide solution
- Polishing with fine sand
- Use of salmiac solution to remove the oxides of non-precious metals
- Coating with mercury


- Silver amalgam is more effective than pure mercury in amalgamating gold. This is produced either by adding silver nitrate solution to the Hg or alloying with silver foil. Alternatively, the copper or muntz metal plates can be activated by plating them with a thin layer of silver. Pure copper tends to oxidize on the surface. Upon the application of Hg, the Hg surface is made inert by the partly soluble copper salts. Furthermore, these hydrated layers prevent the mercury from adhering to the surface of the plates. The application of silver on the surface prevents this.

- Acidic mine water is detrimental to the amalgamation. By grinding limestone in with the feed, this effect can be neutralized. Correspondingly, It is recommended that this be done only in deposits which have ores containing little or no sulfidic accompanying minerals.

The development of the amalgamation occurred in the 1st century AD. during the reign of Emperor Nero (54 - 68 AD.) in Bosnia.

The inclination of the table has a critical effect on Au recovery. Tables should be inclined just enough so that heavy-material grains do not settle out. The slurry should flow with small periodic waves over the table surface. Small steps improve the amalgamation. The plates comprising the table surface must, in any case, be completely smooth.

To avoid evaporation of mercury especially when the flow of slurry is turned off, the amalgamation table should always be protected from direct sunlight.

- Soluble lead minerals, arsenic (in arsenopyrite, arsenic sulfphides etc.), antimony, and bismuth react either with the mercury, forming amalgam or chemical coatings, or dissolve Hg or precious metal amalgam out of the compound, which lead to substantial losses of precious metals and mercury. Fresh pyrite and copper pyrite, to the contrary, do not affect amalgamation. Barite, talc, steatite and viscous hydrogenized magnesium and aluminum silicates also cause disruptions or losses during amalgamation.

- Oils, grease or lubricants are extremely deleterious and instantly lower the recovery achieved from the amalgamation.

- Prior to amalgamation on the amalgamation table, the feed must be thoroughly classified to ensure that no coarse grains flow over the table which could cause mechanical abrasive wear of the amalgam.

Contaminated, impure mercury is much less active than fresh mercury. While the latter forms ideal beads, almost perfectly round with a bright metallic glow, the contaminated mercury can be recognized by its dull surface, deformed shape of the beads, and the tendency of the beads to adhere somewhat and form a tail when rolled over a smooth inclined surface.

There are several methods of cleaning and reactivating contaminated mercury;

- by screening with a very fine-mesh screen (~ 200 mesh)

- by washing with wood ashes and water (whereby calcium carbonate contributes to the saponification of impurities)

- by washing the mercury with water containing tensides or with special plant-sap solutions, both of which are capable of saponifying grease and greasey substances and bringing them into solution

- by washing with reagents such as ammonia, ammonium chloride, cyanides, hydrochloric acid, nitric acid, etc.

- by distilling the mercury in the retort, which removes slightly volatile impurities

- by admixing sodium amalgam with the mercury, whereby the Na-amalgam is transformed into NaOH upon contact with water, which in turn dissolves surface components of the impure mercury. An effective solution concentration is 1 part sodium to 2000 parts mercury. (The production of Na-amalgam through electrolysis is performed as follows: A vessel is filled with mercury and brought into contact with a carbon cathode placed inside an insulated tube (e.g. glass or plastic). A sodium chloride bath (10 - 15 % solution), which is connected to a carbon anode, is poured over the mercury. Through the direct current of a car battery, Na+-ions are transferred onto the Hg surface and amalgamated as metallic sodium. After 10-15 minutes, sufficient concentrations are reached. The Na-amalgam obtained should be stored under air-tight conditions, for example under petroleum.

REPORTS OF OPERATING EXPERIENCES:

In gold mining in northern Chile, the copper plates are cleaned with urine before being coated with the mercury.

In gold mining in Colombia, amalgamating tables are widely distributed. The amalgamating tables are cleaned of amalgam every 6 hours and newly prepared for reuse. Cleaning of the copper plate, and then the mercury surface, is performed using either a strong detergent or the sap from sisal leaves (cabulla, fique). Sisal contains tenside-like substances which dissolve grease. At the same time, sisal sap helps prevent flotation of gold particles during the amalgamation process. This is accompilshed by placing a piece of leaf in the stamp mill and grinding it in with the ore feed' thereby releasing the sap.

SUITABILITY FOR SMALL-SCALE MINING:

For the processing of finely intergrown gold ores which do not have high sulfide contents, the amalgamation table represents a sorting method which is very effective, reasonably-priced and simple to operate. The use of amalgamation tables should, however, automaticallyinclude the use of devices for the recovery of amalgam and mercury (retorts and hydraulic heavy-material traps) for protection of both health and the environment.


Fig.: Amalgamating table directly behund a stamp mill. Source: Uslar.


Fig.: Amalgamating table. Source: Uslar.

15.3 Amalgamating barrel

Gold Mining
Beneficiation, Gold Processing

germ.:

Amalgamiertrommel

span.:

tromel de amalgamacion, chancho, amalgamadora, barril de amalgamacion

Manufacturer:

Svalcor

TECHNICAL DATA:

Dimensions:

Berdan pan: 1.0 × 0.6 × 0.6 m HOOD, inclination angle approx. 15°, 20 - 30 min-1

Weight:

from approx. 50 kg up to several 1000 kg

Extent of Mechanization:

not mechanized/semi-mechanized

Form of Driving Energy:

electric motor or internal combustion engine, hydromechanical, manual, pedal drive

Mode of Operation:

intermittent




Throughput/Capacity:

depends on size




Operating Materials:


Type:

mercury

possibly steel balls

water

reagents to activate surface of Hg, e.g. NaOH, sodium amalgam, ammonium chloride, cyanide, nitric acid, tensides

Quantity:

approx. 1 - 3 kg/kg Au

or stone pebbles



ECONOMIC DATA:

Investment Costs:

dependent on extent locally produced and type of drive-system, starting at approx. 100 US$

Operating Costs:

cost of reagents and energy

Related Costs:

amalgamating press, distillation retort, pre-concentrating equipment

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high


depends on power source

Maintenance Expenditures:

low |————|————| high

Personnel Requirements:

training in handling of Hg is necessary

Location Requirements:

very little water needed

Grain Size of Feed:

20 · 50 ym to 2 mm for Au-fraction

Special Feed Requirements:

free, liberated gold without crustations (for example by fine Fe-oxides); possibly treatment with reagents, no platy floured gold, low content of antinomy minerals, possibly prior flotation, but then problematic surface conditions (hydrocarbons)

Recovery:

very high under good working conditions; in some cases > 95 %

Grade of Concentrate:

amalgam contains up to 50 % Au, but lower concentrations of gold in the amalgam are practical, with subsequent concentration in an amalgam press

Replaces other Equipment:

manual amalgamation in batea (pan), amalgamation in combination with other processes

Regional Distribution:

worldwide in gold mining

Operating Experience:

very good |————|————| bad


compared to amalgamation in sluices, Chilean mills, stamp mills, etc., Hg-emissions can be kept at very low levels; in particular the addition of reagents and reduction of slurry velocity prevent the occurrence of floured mercury.

Environmental Impact:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

metal manufacturing involving pipe sections, sheet metal, bearings, etc.

Lifespan:

very long |————|————| very short

Bibliography, Source: Hentschel, Born, Bernewitz,

OPERATING PRINCIPLE:

The amalgamating barrel operates according to the same principle as the ball mill. The mineral feed consists of rich pre-concentrates. During rotation of the barrel, this feed material is extensively mixed with water, mercury (in a quantity about three times the amount of gold expected to be recovered), grinding bodies and the above-mentioned reagents. During the process, Au-particles come into contact with the mercury and amalgamate. Under influence of the grinding bodies, the gold is worked into the mercury; this occurs so effectively that even the finest gold-fraction, which otherwise could not be recovered In the amalgam due to the surface tension of the mercury, penetrate into the mercury. Upon completion of the rotation process, vibrations and pounding impact forces enhance the density differentiation, whereby the amalgam-Hg mixture collects at the deepest portion of the barrel and is removed following flushing or scimming off of the tailings.

AREAS OF APPLICATION:

For amalgamation of pre-concentrates in a closed reactor.

SPECIAL AREAS OF APPLICATION:

For the simultaneous grinding and amalgamation of non-liberated pre-concentrates in a non-continuous operation, which requtres, without exception, a higher filling-gradient (more grinding bodies) in the ball mill.

REMARKS:

Instead of a ball mill, small-scale mining operations often use cement mixers for barrel amalgamation.

The feed material for barrel amalgamation should always be thoroughly washed prior to amalgamating In order to wash out soluble minerals which could cause inactivation of the Hg-surface.

During a purely amalgamating process, the rotation speed of the amalgamating barrel lies at about 50 % of the optimal rotation speed for a mill of comparable size. At this low speed, the formation of floured mercury is avoided. In simultaneous grinding and amalgamation, an intermediate rotational speed must be applied as a compromise between losses in efficiency due to sliding of the grinding bodies and unfavorable conditions for the amalgamation.

The American "berdan pan" is a slowly-running one-ball mill equipped with a circular ecliptic track, whereby the mill shell rotates and the ball remains in the deepest portion of the track where it floats on the mercury.

The advantage of amalgamating barrels is their contribution to environmental protection by eliminating or reducing losses In metallic mercury (as floured mercury) during amalgamation. During processing, the surface characteristics of the Hg in the closed barrel can be maximized according to the feed material through the addition of reagents.

SUITABILITY FOR SMALL-SCALE MINING:

Amalgamating barrels can be highly recommended for their effectiveness in preventing the release of Hg during amalgamation. They combine the advantages of easy low-cost construction, diverse mechanization possibilities, and ability to control the surface activity of mercury through the addition of reagents with the utilization of the good separating characteristics of amalgamation. Pre-concentrating of the feed material is a prerequisite.


Fig.: Berdan pan, single-ball mill for amalgamation. Source: Bernewitz.


Fig.: Amalgamating barrel as rod mill. Source: Bernewitz


Fig.: Amalgamation in agitators, by Agricola. Source: Agricola.

15.4 Rocker, cradle

Gold Mining
Beneficiation, Gold Processing

germ.:

Rocker, Wiege, Wiegensieb

span.:

cuna, criba cuna, chinchola, cuna californiana, cuna siberiana, lavador, concentrador

Manufacturer:

Keene

TECHNICAL DATA:

Dimensions:

up to several m in length

Weight:

20 - 50 kg

Extent of Mechanization:

not mechanized

Form of Driving Energy:

manual

Mode of Operation:

semi-continuous

Throughput/Capacity:

500 - 1000 kg/MS including refining with batea (panning)

Technical Efficiency:

approx. 6 - 10 t feed with 2 persons in 10 h when solely pre-concentrating

Operating Materials:


Type:

water

Quantity:

400 - 3000 1/10 h

ECONOMIC DATA:

Investment Costs:

starting at approx. 200 DM if locally produced

Operating Costs:

mainly labor costs

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Special Feed Requirements:

lowest possible content of sticky, tenacious clays or partially consolidated sediments that cannot be crushed with the rocker during processing and therefore prevent liberation of the gold

Recovery:

somewhat low recovery in fine fractions, therefore suitable for high quantities of feed (high throughput) containing relatively coarse-grained gold (> 100 ym).

Replaces other Equipment:

sluices, batea (panning)

Regional Distribution:

Chile, Colombia

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

rockers can be manufactured in simple wood manufacturers using good screen material

Lifespan:

very long |————|————| very short

Bibliography, Source: Rittinger, Buch der Erfindungen 1890 ("Book of Inventions 1890", in German), Silva

OPERATING PRINCIPLE:

The rocker consists primarily of a classifying device and a trough washer. The classifying device has the form of a deep screen box for receiving the feed. Located underneath it is an Inclined wooden riffled trough with transverse slats. The inclination of the trough varies depending on the grain size of the feed material. For feed with high clay content, the angle of inclination is less than for material of coarse grain size. This entire unit is mounted on rockers, so that the whole upper portion can be rocked back and forth by means of a lever handle. The input and discharge of processing water for flushing is performed manually, requiring a total of four people for the mining and processing of gold using one rocker: one for mining the raw ore, one for transporting and feeding the ore into the rocker, one to do the rocking, and one for flushing with water.

AREAS OF APPLICATION:

For processing of loose or slightly-consolidated gold-containing sediments.

REMARKS:

The rocker represents the classic processing tool of North American gold miners and was used up until the present century.

In gold mining in North America, the pre-concentrates obtained from processing with the rocker (heavy-mineral sands with gold) were subsequently dried and sorted by wind-classifying.

The proper adjustment of the sluice's inclination greatly affects the recovery achieved with the rocker. The discussion presented for sluices is applicable here as well.

Rockers are particularly well suited for arid regions due to their low water requirements.

SUITABILITY FOR SMALL-SCALE MINING:

The advantages of a rocker (light-weight construction, portable non-powered technique, highly suitabile for local production) make it appropriate as a mobile beneficiation apparatus for processing sedimentary gold ores during prospecting and mining. Especially for loose materials which do not require crushing, the rocker offers the advantage of a combined classification and sorting.


Fig.: Elevation and plan views of a rocker. Source: Bernewitz.


Fig.: Design plans a rocker. Source: Silva

15.5 Mechanized, compact gold processor

Gold Mining
Beneficiation, Gold Processing

engl.:

gold saver, washplants

germ.:

Mechanisierte kompakte Goldaufbereitungen, z.B. Gold Saver, Prospektor

span.:

beneficios de oro mecanizados en forma compacta, por ejemplo gold saver, prospector

Manufacturers:

Denver, Goldfield, Svalcor, Buena Fortuna, Fima, Metal Callao E.P.S., Met. Lacha

TECHNICAL DATA:

Dimensions:

1 17x74x153 cm HWD

Weight:

270 kg

Extent of Mechanization:

fully mechanized

Driving Power:

3 PS

Form of Driving Energy:

internal combustion engine or electric motor

Alternative Forms:

hydromechanical ?

Mode of Operation:

seml-continuous

Throughput/Capacity:

2-3 m³/h

Operating Materials:


Type:

water

fuel

lubricants

Quantity:

20 - 351/min

approx. 2 - 5l/h

small quantities

ECONOMIC DATA:

Investment Costs:

approx. 4000 us$ if locally produced; approx. 25.000 DM fob factory

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————————| high


3 people: 1 to feed, 1 to remove tailings, 1 to operate

Maintenance Expenditures:

low |————|————| high

Grain Size of Feed:

< 100 mm

Special Feed Requirements:

relatively coarse gold grains

Recovery:

can be substantially increased with subsequent sluice or amalgamating table

Replaces other Equipment:

sluices, Long Tom

Regional Distribution:

Colombia

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high


depending on type of feed material, high sludge loading can occur

Suitability for Local Production:

very good |————|————| bad


according to Degowski, a Gold Saver has already been reproduced locally in Pasto, Colombia

Under What Conditions:

good metal and welding workshops

Lifespan:

very long |————|————| very short

Bibliography, Source: Degowski

OPERATING PRINCIPLE:

Washplants for gold processing, for example those offered by Denver or Goldfield, consist of a classification drum with a coarse screen for separating and autogenous crushing of consolidated chunks of host rock. Fine material is subsequently processed in a vibrating sluice at a frequency of 200 - 220 min-1. The over-flow can then be further processed, for example, in a sluice or amalgamating table.

AREAS OF APPLICATION:

Extraction of gold from non or slightly-consolidated sediments containing coarse lumps < 100 mm in size.

REMARKS:

A Gold Saver of similar construction as described above was locally produced and applied in a GTZ-project (German Technical Assistance) in Colombia.

Gold Savers may find little acceptance compared to traditional methods. Especially in the extraction of gold from fluviatile alluvial deposits' mine operators consider the following aspects as problematic: the dependency on fuels, the danger of rising water levels in the river which necessites relocation of the Gold Saver to higher ground at the end of each work day, and the very high throughput which requires a corresponding increase in production capacity.

SUITABILITY FOR SMALL-SCALE MINING:

The advantage of the Gold Saver is its compact and mobile construction, serving as a complete processinq unit for loose and slightly-consolidated sediments. For stationary application, however, or when powered hydromechanically. the employment of individual components is a more cost-effective solution.

15.6 Hydraulic gold trap

Gold Mining
Beneficiation, Gold processing

germ.:

Hydraulische Schwergutfalle

span.:

trampas hidraulicas pare material pesado

Manufacturer:

Zutta Hermanos, ASEA-Perini

TECHNICAL DATA:

Dimensions:

up to 60 × 60 × 60 cm depending on throughput capacity

Weight:

from approx. 2 - 20 kg

Extent of Mechanization:

not mechanized

Form of Driving Energy:

only processing water, no drive system

Mode of Operation:

continuous

Throughput/Capacity:

several t/d

Operating Materials:


Type:

water for counter flow

Quantity:

10 - 50 I/min with hydrostatic pressure of 0.1 - 0.5 bar

ECONOMIC DATA:

Investment Costs:

very low, approx. 100 - 200 DM depending on size

Operating Costs:

very low

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Location Requirements:

trap is built into sluice systems, water necessary

Grain Size of Feed:

range of grain size should have an upper limit of 1 - 3 mm

Output::

only coarse gold grains are separated from the mass flow, for example to prevent their being subject to further grinding; no amalgamation occurs, contrary to the similarly designed Jackpot where amalgamation occurs at the deepest point

Replaces other Equipment:

sluices for coarse fractions

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high


since no mercury is used

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

metal workshop

Lifespan:

very long |————|————| very short

Bibliography, Source: v. Bernewitz, Schennen

OPERATING PRINCIPLE:

The hydraulic gold trap functions like a small artificial sedimentation basin which is placed in the material flow. In so doing, the flow is not interrupted, so that only heavy particles sink down. The sedimentation chamber is kept free of light material by means of a supplementary underwater flow. Therefore, the hydraulic gold trap is comparable to a single-celled settling box with clear water countercurrent.

The concentrate can be withdrawn during processing by opening the outlet valve.

AREAS OF APPLICATION:

Separation of coarse gold and heavy-mineral sand fractions from beneficiation processing circuits, e.g. prior to further grinding, sorting, amalgamating, leaching, etc.

SPECIAL AREAS OF APPLICATION:

Also applied for separating amalgam and mercury after the amalgamating process, for example following a stamp mill to collect the amalgam.

Also appropriate for collecting jig-bed particles discharged from a Jig.

REMARKS:

Suitable only in deposits which contain coarse fractions of gold; not practical for use in deposits containing exclusively fine. grained gold fractions.

In addition to the above-described construction with cross-current flow, some hydraulic gold traps have a slurry-feed input through a centralized pipe under the slurry surface. This forces a reversal in the direction of slurry flow, allowing the gold to settle out. This system therefore functions analogous to the continuous (rake) thickener, or Dorr-type thickener.

SUITABILITY FOR SMALL-SCALE MINING:

Hydraulic gold traps are a simple, efficient, and inexpensive alternative for preliminary separation of coarse gold grates or nuggets. Hydraulic gold traps also play an important role as amalgam or mercury traps succeeding any type of amalgamating equipment.


Fig.: Simple hydraulic trap. Source: Schennen.


Fig.: Cross-section through a hydraulic trap. Source: Taggert.


Fig.: A hydraulic gold trap. Source: Bernewitz


Fig.: Basic operating principle of a simple hydraulic trap for mercury and amalgam. Source: Escobar Alvarez.

15.7 Retort for, amalgam

Gold Mining
Beneficiation, Gold Processing

engl.:

still, distillation retort

germ.:

Destillierkolben

span.:

retorta de destilacion, retorta de amalgama, matraz de destilacion

Manufacturers:

Keene, Svalcor, Talleres J.G., Taller "Centro del Muchacho Trabajador", ASEA, Zutta

TECHNICAL DATA:

Dimensions:

approx. 10 × 10 × 60 - 80 cm, crucible approx. 5 cm in diameter, 5 cm deep

Weight:

approx. 10 kg

Extent of Mechanization:

not mechanized

Form of Driving Energy:

thermal from biological fuels

Mode of Operation:

intermittent

Throughput/Capacity:

depending on design, between 0.5 and 70 or more kg capacity, duration of distillation approx. 15 - 25 min

Operating Materials:


Type:

water Heat by burning wood, coal, gasoline, diesel, gas, etc

Quantity:

small quantities For cooling

ECONOMIC DATA:

Investment Costs:

Retort: 100 to 500 DM if locally produced, serial production should be targeted to lower the cost of production, however amortization possible through recovery of Hg.

Operating Costs:

relatively high due to heating; however in open-circuit distillation, costs are also incurred for fuel

Related Costs:

blow torch approx. 30 DM

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Location Requirements:

even the distillation of amalgam in retorts should take place in sufficiently ventilated environments, preferably in open air

Special Feed Requirements:

the amalgam should be cleaned (see 15.2)

Recovery:

heating of the gold amalgam to a temperature above the boiling point of mercury (350° C) separates the amalgam into gold (residue) and mercury (vapor). Recovery is nearly 100 %.

Replaces other Techniques:

must replace separation processes openly exposed to the atmosphere!!

Regional Distribution:

widespread in beneficiation laboratories in Latin America, seldom found in production plants

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high


minimal Hg-vapor pollution due to opening of the crucible or loose cover/seal

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

simple metal manufacturer, produced from pipe sections (Rossi-Retort)

Lifespan:

very long |————|————| very short

Bibliography, Source: v. Bernewitz, Stout, Albes, Villefosse, Rittinger, Ullmann, Company Information

OPERATING PRINCIPLE:

Through the inparting of heat to the crucible, the gold-mercury-alloy is dispersed into its components at around 600°C and mercury is vaporized. In the condenser tube, the Hg-vapor condenses as droplets (counter-current cooling with water) and flows into a catchment vessel containing water (which prevents further evaporation).

AREAS OF APPLICATION:

For the separation of amalgam into mercury and the valuable metal (gold or
silver)

REMARKS:

Due to the short utilization period of distillation processes, the distillation retorts should, when possible, be cooperatively purchased and used in order to more widely distribute the investment costs.

Retort constructions which are built from steel-pipe sections are comparatively inexpensive and lend themselves to mass production without major cost or effort.

In all types of retorts, extra care must be taken that fittings, valves or closures are air-tight.

In cases where amalgamating with open Hg-circuits cannot be eliminated, then efforts should be taken to encourage the gold buyer to purchase the amalgam instead of the processed gold. The amalgam could then be distilled in the presence of the mine operator, the gold weighed, and payment made.

Before distillation, the amalgam is wrapped in paper. The ashes of the burned paper form a non-adhesive intermediate layer between gold and the bottom of the retort. It would be better to dust the lining of the retort with a thin layer of graphite, limestone, gypsum or talc prior to inserting the amalgam so that the gold does not stick to the bottom of the retort following distillation. In no case should greasy or fatty substances be used; these evaporate with the mercury and Inactivate its surface.

If a retort is not tightly sealed, the leak can be sealed prior to distillation with a mass made of fine, moist clay mixed with ash applied at the fitting between the cover and the bottom. The clay may not contain any grains, however.

It could often be observed that the acceptance of distillation devices in small-scale mining in developing countries is relatively low. Even when retorts are already present, amalgamation is still performed in open Hg-circuits, first because this proceeds faster, and secondly because the color of the gold produced after evaporating the mercury in a ceramic crucible is lighter, and therefore brings a higher price from the buyers. These disadvantages can possibly be counteracted by lining the Inner surface of the retort with a highly corrosion-resistant material. On the other hand, impurities in the amalgam are partly responsible for the discoloration. In small-scale mining in Ecuador, for instance, the gold concentrate is washed with the juice from sugar-cane oranges or lemons in order to complex silver and thereby increase the fine-gold content. Such impurities impart a black coating during air-tight distillation. A good washing of the concentrate or amalgam can remove these substances, which cause later discoloration, from the feed prior to distillation.

Finally, there are other amalgams, for instance amalgams of arsenic, antimony or copper, which cause impurities In the gold as well as in the Hg. Depending on the boiling temperature and the vapor pressure of the metal, these evaporate With the mercury during the distillation process, or remain as a crust on the gold. These amalgam impurities can be washed out before distillation. First, the amalgam is degreased using a milk of quick lime, then freed of iron chips, and finally washed with diluted hydrochloric acid.

In order to increase acceptance of disillation retorts in small-scale mining regions, the process can be demonstrated to the miners using glass retorts made of heatproof glass. These demonstrations would make the process understandable to the miners and remove their fears of allowing their gold or amalgam to be processed in a closed reactor. This type of retort could also be produced in developing countries by technically-qualified glass-blowers.

In constructing retorts, It is important that the condensation surface for the mercury is kept as small as possible. This minimizes the loss of mercury through cohesion of the finest beads on the inner wall of the retort. Therefore the cooling pipes should be of the least possible diameter, and must be made of iron or steel pipe sections since brass amalgamates with mercury, The inside surface of the pipe must be smooth, and seams should always face upwards to avoid losses due to dripping. Nevertheless, about 2 - 5 g mercury always remain in the device which can only be recovered by washing. For this reason it is advantageous to always collect larger quantities of amalgam for distilling together in one operation.

During operation, the distillation retort must always be heated so that the entire crucible and its lid, as well as the rising portion of the vapor tube, become hot enough to prevent a condensation of mercury in this zone. Otherwise, this liquid mercury runs down again Into the deepest part of the retort and has to be revaporized.

Instead of amalgamating in a distillation retort, the distilling process is unfortunately often conducted in an open-circuit process involving open flat clay or ceramic bowls which are heated by means of blow torches, allowing the mercury to evaporate out of the amalgam. Highly toxic Hg vapors develop.

In Ecuador, a fresh banana leaf is placed over the bowl or crucible in order to recover part of the mercury escaping as vapor from the amalgam. Hg condenses on the surface of the leaf and collects at the edges. Colombian miners use orange peels or cabbage leaves for this purpose.

Besides distillation in retorts, there are also chemical methods for separating mercury from the amalgam. Among these is the analytical method of dissolving Hg out of the amalgam with (diluted) nitric acid. The transformation reaction occurs as follows:

HgAu + 2 HNO3 ® Hg(NO3) + Au + H2

After the precipitated spongy gold-residue has been separated from the dissolved nitrate, the mercury can be recovered through ion exchange with copper or other non-precious metals, with the copper nitrate being discarded. In using chemical separation methods, the danger exists with silver-containing gold ores that Ag gradually concentrates in the mercury, which consequently requires a periodic cleaning by distillation. The chemical reaction for mercury separation is:

Hg(NO3)2 + Cu ® Cu(NO3)2 + Hg

Mercury losses through distillation in retorts are very minimal (< 0,1 %).

WARNING!!!

The separation of the amalgam in the atmosphere is endangering to life and toxic to the environment (Hg-vapors).

In all distillation retorts, care must be taken that, upon completion of heating, no water is sucked in which can penetrate inside the crucible during cooling. This can lead to an explosion of the still-hot crucible due to sudden evaporation. This danger can be prevented through the use of water sacks or similar devices, or by maintaining a minimal distance between the suspended cooling pipe and the catchment bucket.

SUITABILITY FOR SMALL-SCALE MINING:

For economic and especially ecological and health reasons, every amalgamation plant should, without exception, amalgamate in closed mercury circuits, i.e. employ distillation retorts.


Fig.: Design drawing of distilation retort. Source: Bernewitz.


Fig.: Retort for amalgam distillation, designed by Proiekt-Consult,made in Colombia.


Fig.: Retort for distilation of amalgam. Source: Ulsar.


Fig.: Types of retort constructions for distillation. Source: Stout.


Fig.: Simplest retort made of standard pipe joints, threaded couplings and pipe sections. Source: Apropriate Technology

Figure 1. The Hypolito retort or RHYP (above)
Figure 2. The condensation tube (1), tampion (2), elbow (3), and double nipple (4), wich together make up the retort (below).



Fig.: Design sketch of a distillation retort made of pipe sections. Source: Bernewitz.

15.8 Centrifugal separator

Gold Mining
Beneficiation, Gold Beneficiation

engl.:

Knelson concentrator, Knudson bowl

germ.:

Zentrifugalscheider

span.:

concentrador centrifugo, Knelson concentrador, Knudson bowl

Manufacturers:

Knelson International Sales Inc., Mineral Deposits, Steve and Duke's Manufacturing Co. or Lee-Mar Industries Ltd., Goldfield, Falcon Concentraters, FUNDEMIN, VARDAX, Met Lacha, INCOMEC


TECHNICAL DATA:


Knelson 7.5"

Knelson 12"

Knudson

Dimensions LWH

33" × 22" × 26"

31" × 31" × 34"

~ 860 × 760 × 585 mm

Weight

117 kg

154 kg

172 kg (without motor)

Driving Capacity

3/4 PS

1 PS

7.5 PS

Throughput

650 kg/in

5 m³/h

3 - 4 t/h

Quantity of Concentrate

1.5 kg

5 kg


Slurry

17 gal/min

30 gal/min


Backwater Quantity

20 gal/min

35 gal/min

-

Backwater Pressure

2 - 3 bar

aprox. 4 bar

-

Washing Water




Maximum Grain �

< 4 mm

< 4 mm

< 4 mm

Minimum Grain �

> 30 µm

> 30 µm

50 - 70 µm

RPM

~ 400

100 - 400

100 - 105

Centrifugal acceleration

60 g



Separation Cut-off




Mode of Operation

semicont.

semicont.

discont.


Falcon B 12

Falcon B 6

Vardax 801

Dimensions LWH

36" × 60" × 73"

19" × 20" × 32"

72" × 18" × 24"

Weight

800 kg

100 kg

110 kg with classifier

Driving Capacity

7.5 PS

1.0 PS

2 PS

Throughput

~ 6 t/h

0.5 t/h

- 2 t/h

Quantity of Concentrate

- 4.5 kg

~ 1 kg

~ 80 kg

Slurry


7 - 12 gal/min


Backwater Quantity

-

-


Backwater Pressure

-

-


Washing Water


5 gal/wash

2 gal/wash

Maximum Grain �

< 1.5 mm

< 0.9 mm

< 6 mm

Minimum Grain �

> 30 µm

> 30 µm


RPM








Centrifugal acceleration

300 g

300 g


Separation Cut-off

4 g/cm³



Mode of Operation

discont.

discont.

discont.

Extent of Mechanization:

fully mechanized

Form of Driving Energy:

electrical, optional internal combustion engine, possibly convertable to hydromechanical drive with difficulty

Technical efficiency:

concentration up to more than 1: 8000; comparatively very high recovery with well-liberated free gold

ECONOMIC DATA:

Investment Costs:

Prices from original manufacturer fob factory:


Knelson 7.5":

6850 US$

Knelson 12":

12500 US$


Knudson:

4500 US$

Falcon B 12:

34000 US$


Falcon B 6:

7000 US$

Vardax 801:

2400 US$


Vardax Sec.:

14500 US$



Operating Costs:

cost of energy and minimal labor costs

Related Costs:

possibly costs for thickener, sedimentation basin or sludge pond

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Location Requirements:

water

Grain Size of Feed:

< 6 mm

Special Feed Requirements:

the feed may only contain a small proportion of clay minerals or partly-consolidated sediments, since these envelope the gold and, due to their consistence, prevent it from existing in a liberated state.

Output:

According to the manufacturers, approx. 95 % free Au up to grain size > 500 mesh (approx. 30 ym). Mineral Deposits lists 50 - 70 µm as the lower grain-size limit for Knudson centrifuge. BGR in Burundi with Knelson concentrator, 95.5 % recovery, 0.63 - 0.063 mm grain size.

Replaces other Equipment:

sluices

Regional Distribution:

rare

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high

Suitability for Local Production:

verygood |————|————| bad

Lifespan:

very long |————|————| very short

Bibliography, Source: Beyer, Hersteller, BGR

OPERATING PRINCIPLE:

Knelson:

Centrifuge with radial acceleration up to 60 g. Slurry is fed through a pipe at the deepest point of the centrifuge and rotated in circular grooves within the drum. Counter-current water flow is forced into the circular grooves from the outside which loosens the material, similar to a fluidized bed. Light material flows over the wall into the next higher circular groove.

Knudson:

The similarly-built Knudson centrifuge operates without a counter-current flow, which greatly simplies the construction. Instead of the water, a vertical blade within the rotating drum assists in spinning the material In the circular grooves, leading to a purification of the concentrate material.

Falcon:

The Falcon centrifuge is comprised of a vertically rotating cylinder with a partially cone-shaped inner surface. A central slurry feed-intake pipe directs the suspended solids onto the rotating feed-intake disk. Under the influence of centrifugal acceleration, the material migrates outward onto the upward-widening conically-formed centrifuge wall. This effectively results in a radial density-sorting of the slurry in which the heaviest particles remain adhered to the smooth wall. The light material flows over the top of the upper cylindrical portion of the centrifuge and is carried out. A ring-formed zone of concentrate with a wedge-shaped cross-section develops. After cessation of feed input, this concentrate is washed off with supplementary rinsing water, whereby the solid materials between the feed-intake disk and the wall of the centrifuge are flushed through the hollow axis into a receptacle for collecting the concentrate.

AREAS OF APPLICATION:

Sorting of feed material containing high proportions of fine gold, specifically alluvial gold.

SPECIAL AREAS OF APPLICATION:

In addition to its application in gold deposits, the profitable winning of by-products with the Knelson centrifuge is also possible in some cases, such as obtaining gold from gravel pits or heavy industrial minerals from kaolinite deposits. The very high throughput capacity of the Knelson centrifuge concentrator allows it to be integrated directly into the processing circuit.

Knudson centrifuges have also been used in some instances for amalgamating.

REMARKS:

In Brazil, Knelson centrifuges have already been manufactured locally. A problem encountered with local production is the centrifuge bearings; worn bearings must be taken up or replaced if necessary.

It is extremely important that the feed material to be centrifuged is completely liberated or suspended prior to processing in the centrifuge. Clay-like sediments or gold occurring in laterites require a partially expensive pre-processing before sorting by centrifuging. Mineral components in the feed which have very heavy specific densities, particularly arsenic gravel, are also recovered with the concentrate. If the proportion of these minerals is very high, the separation accuracy of the centrifugal sorting is impaired.

The product of the centrifuge is a pre-concentrate which then requires subsequent cleaning (purifying) either by amalgamating, leaching or similar processing.

The counter-current water flow of the Knelson centrifuge must consist of clear water, otherwise the fine perforations in the centrifuge shell could become clogged, and consequently the centrifuged material in the circular grooves could not be loosened. Furthermore, it is absolutely necessary that the water pressure be kept constant, since even negligible increases in pressure can result in fine-grained concentrate, especially particles of high specific surface area, being carried out in the overflow. Likewise, the flow of feed should not be interrupted. These difficulties with process regulation do not arise in simply-designed centrifuges.

On account of their simple construction, Knudson concentrators and possibly Falcon centrifuges are quite suitable for local manufacturing.

In comparind fluid-bed centrifuges (Knelson) to simple centrifuges, Knelson has the advantage of being able to recover significantly smaller grains of the precious metals and achieving a higher degree of concentration, as a result of the fluidized-bed structure. Whereas the Knelson concentrator can operate continuously for many weeks and, as a result, yields high concentrations of gold, the construction of simple centrifuges allows these to operate semi-continuously with only brief pauses and to produce comparatively larger amounts of pre-concentrate (for example, turbulence can be generated in the Knudson centrifuge only very incompletely and the sorting barrel rotates at lower rpm).

SUITABILITY FOR SMALL SCALE MINING:

The Knelson centrifuge is a very suitable apparatus for winning even the finest fractions of gold from alluvial deposits. Despite relatively high investment costs and the necessity to import the equipment, the investment is amortized relatively quickly through the income from the high recovery of the gold fines. Suitable deposit characteristics are a prerequisite for successful application.

Simple centrifugal separators are, especially when they can be manufactured locally, the most suitable for small-scale mining due to their sturdier, simpler construction.


Fig.: Schematic cross-section diagram through the centrifuge of a Knelson concentrator. Source: Knelson.

15.9 Gold pan, batea

Gold Mining
Beneficiation, Gold Beneficiation

germ.:

Sichertrog, Waschpfanne, Schiffchen, Niersch, Saxe

span.:

batea, chua, challa, prune, zuruca (v.), sarten lavador, batea en forma de bote

Southeast Asia:

dulong, dulang

Manufacturers:

Krantz, Keene

TECHNICAL DATA:

Dimensions:

20 50 cm 0, 5 - 25 cm depth / 15 × 15 × 150 cm HWD / ca 45 - 50 cm diameter, 10 cm depth, 35°- 40° inclination (USA)

Weight:

0,5 - 5 kg

Extent of Mechanization:

not mechanized

Form of Driving Energy:

manual

Mode of Operation:

intermittent

Throughput/Capacity:

cat 1 - 5 kg/mini daily performance 100 pans at 20 lbs = 1 t/d

Operating Materials:


Type:

water

Quantity:

small (can be used in non-flowing water)

ECONOMIC DATA:

Investment Costs:

approx. 10 to 20 DM

Operating Costs:

labor costs only

Related Costs:

none

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Personnel Requirements:

lots of experience is essential for accurate sorting with high recovery

Grain Size of Feed:

< approx. 30 mm

Special Feed Requirements:

free Au as valuable mineral or valuable mineral with very high density

Recovery:

high, also in the fine grain-size range (lower grain-size limit 20 µm), flakes (flour gold) down to 50,um are recoverable in the gold pan

Regional Distribution:

worldwide

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

simple wood manufacturer or sheet-metal workshop for trays made of galvanized sheet metal

Lifespan:

very long |————|————| very short

Bibliography, Source: Treptow, Schnabel, Agricola, Calvor, Ramdohr, Lepper, Clennell, Silva, Treptow Collection/Freiberg

OPERATING PRINCIPLE:

Through shaking of the pan, gold settles at the deepest point on the pan's bottom. During washing, the tray is moved in such a way that the middle and deepest part, containing the heavy gold particles, remains almost stationary and the lighter tailings, carried along by the flowing water and subject to the radial acceleration forces near the pan's rim, are discharged. This procedure is repeated until only the gold or the black gold-containing sands remain. The final step performed by the gold penner is to slightly tip the pan and lightly knock on the back of the rim in the direction of inclination. This resembles the bumping-table effect whereby the gold accumulates at the highest point of concentrate fan.

AREAS OF APPLICATION:


- for analysis in almost all beneficiation processes
- for sorting of pre-concentrates, for instance, from sluices
- for sorting of gold-containing alluvial deposits
- for semi-quantitative analysis of contents exceeding around 10 g/t

REMARKS:

Gold pans are manufactured from various materials, such as:

- metal

- wood

- half-shell or rind of pumpkin, squash or melon

- PVC

- animal horn (poruna), historically from Argentina and Mexico (bull horn); still being used in arid mining regions in Chile

- rubber (car tires)

The best have proven to be those made of black PVC:

Advantages:

- cracks do not develop

Disadvantage:

- the surface repells water


- good gold visibility




- durable and long-lasting




- light weight



Chromite or ilmenite sands are recommended as contrast medium (added to the raw
material)

Gold tends to undergo flotation. 1 or 2 drops of detergent added to the water, or often also sap from plants (e.f. sisal, spanish: fique) can prevent flotation.

Panning was already described by the Swede Peter Mansson who died in 1536.

The number of individual particles per ounce of gold depends upon the grain size:

small nuggets

10 - 20 mesh:

2200/oz.

big flakes

20 - 40 mesh:

12000/oz. gold

fine flakes

< 40 mesh:

40000/oz.

The minimum particle size visible with the naked eye in a black pan is around 20 ym

The lower limit for manual removal of gold particles is 1 - 2 mm, smaller particles require amalgamation or leaching.

Gold pans are often clearly different in their design depending upon the type of feed to be processed: gold pans used In alluvial deposits are generally significantly flatter (shallower) than those pans used in vein ore mining.

For hand-sorting of fine pre-concentrates, small spray bottles with thin elongated nozzles for sucking up the grain are preferred.

In gold mining in Ecuador, for example, amalgamation is also performed in gold pans. The gold is worked in with a stone for about an hour, after which the mercury, divided into fine beads, is recombined by knocking on the rim of the gold pan. The finest beads, or floured mercury, cannot be refused, due in part to the high surface tension of the mercury or encrustations of fine oxidic mineral dusts, and is carried off and released into the environment during washing of the amalgam. For this reason, this procedure must be considered extremely dangerous and should not be used.

In large-scale facilities, the surface tension of the mercury is relieved by adding cyanide or nitric acid, or less frequently sodium amalgam, caustic soda or ammonium chloride. This is not possible when processing in a gold pan.

SUITABILITY FOR SMALL-SCALE MINING:

Gold pans are used in small-scale mining because of their high degree of separation in all areas of application (prospecting, exploration, analysis during processing, and beneficiation); their use is indispensible. In beneficiation they are primarily employed for cleaning of pre-concentrates. They are characterized by very low throughput quantities and investment costs.


Fig.: Different types of gold pans, above left: "Freiberger" pan, above right: "Salzburger" pan, below left: North American from, below right: Latin American form. Source: Treptow (above) and Schnabel (below).


Fig.: Gold pan designs form the Rhine gold mining region (Germany). Source: Lepper.

15.10 Jigs with jig bed, russel jig

Gold Mining
Beneficiation, Gold Beneficiation

germ.:

Setzmaschinen mit Setzbett

span.:

jig con came de boles de promo

Manufacturers:

Mineral Deposits, Denver, IHC Sliedrecht, Goldfield

TECHNICAL DATA:

Dimensions:

from 1 × 0,75 × 1 m up to 3,60 × 3 × 3 m LWH with 0,5 × 0,2 m (2 jig beds) up to several m jig bed sizes

Weight:

from 50 kg

Extent of Mechanization:

fully mechanized

Throughput/Capacity:

4 - 65 t/h

Form of Driving Energy:

electric

Power/Performance:

0,5 to several kW, 50 - 300 thrusts/minute, approx. 25 mm lift

Alternative Forms:

with internal combustion engine, possibly even manual operation for small machines

Operating Materials:


Type:

lead balls grease

Quantity:

8 - 10 DM/kg

ECONOMIC DATA:

Investment Costs:

from approx. 3000 DM when locally produced

Operating Costs:

mainly costs of energy and labor

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Location Requirements:

water must be available

Grain Size of Feed:

50 ym - 2.5 mm gold grain-size fraction is recovered; nuggets larger than 2,5 mm are concentrated on the screen bottom underneath the jig bed.

Special Feed Requirements:

gold must exist as liberated free gold

Replaces other Equipment:

troughs, sluices, other Jigs, Gold Saver

Regional Distribution:

available on the world market, widespread in gold mining in Australia, Indonesia

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high

Suitability for Local Production:

very good |————————| bad

Under What Conditions:

possibly as manual jig or jig with pedal-drive, can be entirely produced by local metal manufacturing shops. For motorized jigs, imported drive units are mostly used.

Lifespan:

very long |————|————| very short

Bibliography, Source: Manufacturer's information, Silva, Schubert, Horway

OPERATING PRINCIPLE:

The Russel Jig with Jig bed for processing gold is a two-staged diaphragm Jig with an internal double-action diaphragm membrane. In comparison to conventional Jigs, this type of construction substantially reduces the drive-power required. The pulsating water flows through a coarse screen mesh of, for example, 1.6 mm wire thickness and 2.5 mm screen openings. A Jig bed, consisting of lead balls (SPb approx. 11.3 g/cm³ ), rests on the bottom of this screen; the lead ball diameter of 4.1 mm has been dimensioned to correspond to the screen openings. Thereby, the Jig bed, which settles onto the screen bottom in the densest volumetric arrangement, is capable of completely closing the screen openings, resulting in higher separation precision and lower quantities of concentrate. The jig's pulse frequencies can be regulated between 50 and 300 min-1. Similarly, the pulse width and the quantity of supplementary water added can also be regulated. The addition of water occurs in the Jig bed above the screen. In this respect, jig types which operate with a constant water quantity (with suction) are differentiated from those in which water is added only during the respective suction-stroke of the diaphragm (without suction). The later is accomplished by regulating with a rotary piston valve.

AREAS OF APPLICATION:

Jigs of the above-described design are used to produce concentrates from alluvial gold or platinum ores. For larger quantities of feed material, the jig is used initially to achieve pre-concentrates, which are then refed into the jig for secondary processing to yield concentrates. Smaller feed quantities are jigged only once and then subsequently processed in an amalgam trap for secondary cleaning or to produce final concentrates.

SPECIAL AREAS OF APPLICATION:

Jigs with jig beds, or Russel jigs, are standard components of mobile pilot-scale beneficiation plants and small mobile production units.

REMARKS:

The simple construction and low specific-energy requirement of the diaphragm jig with Jig bed (Russel Jig) appear to support local production of a manually or pedal-driven Jig of this type. Jig bed size in the order of 2 × 40 × 20 cm should still permit manual operation.

Modern Russel jigs are of modular construction, consisting of several units. These are fashioned from circular segments which are assembled into a round unit. This has the advantage that, with a relatively simpler central feed input, large quantities of feed material can be processed and sorted. The geometry of the jig bed causes the cross-flow to become relatively smaller toward the rim, which increases the processing duration and therefore separation precision.

By modifying the bed material (balls of lighter specific-density), these fine-grain Jigs can also be used for winning well-classified tin or tungsten ores.

The thickness of the jig bed is determined by the granulation of the feed material: for coarse feed, the bed should be 7 to 12 times thicker than the upper grain-size of the concentrate, and for finer feed (< 2 mm) about 20 times the maximum grain-size. The diameter of the bed grains should be 3 to 4 times that of the upper grain-size in the concentrate.

If a Jig is operated with suction, fine fractions are quickly and accurately drawn through the processing, while coarse fractions migrate only very slowly through the jig bed and screen mesh. In jigs run without suction, the effect is reversed.

If several consecutively-arranged jig beds are used, the grain sizes of the jig-bed particles increase In the direction of feed input.

The length of duration of feed material in the jig can be varied by changing the ratio of cross-current flow: quantity of supplementary water.

The use of a heavy-material trap, such as a riffled sluice, installed in the light-material discharge outlet in the Jig bed is highly recommended for the recovery of jig-bed material which has been undesirably flushed out.

The large diaphragm dilations can be achieved by using a rubber car hose as the membrane element The complicated insertion of the diaphragm connecting-rod through the jig's settling-box wall can also be accomplished with the help of a locally-available standard part, namely the bellow which covers the gear-shift-lever slot in a car, which can be used to seal the opening around the rod.

As bed material for locally-manufactured jigs, lead buckshot (for hunting purposes) can be used, which is freely sold on the market in developing countries.

The concentrate or underflow valves in the jig bed should always be slightly open during operation and the concentrate continuously discharged in order to avoid sedimentation and clogging of drain outlets.

SUITABILITY FOR SMALL-SCALE MINING:

Jigs with Jig beds for producing gold pre-concentrates at high factors of concentration with comparatively high throughput are very appropriate for small-scale mining; they require, however, a motorized drive system.

15.11 Gold leaching

Gold Mining
Beneficiation, Gold Beneficiation

engl:

cyanide leaching, (agitation leaching, vat leaching, heap leaching)

germ.:

Goldlaugung, cyanidische Laugung (Ruhrlaugung, Behalterlaugung, Haufenlaugung)

span.:

lixivacion de oro, lixiviacion, lixiviacion con cianuro (lixiviacion por agitacion, lixiviacion en tanques, lixiviacion en piles)

Manufacturers:

HBS-Equipment (cell for electrolytic + absorptive separation), Denver

TECHNICAL DATA:

Dimensions:

leaching tanks several m³ in volume

Weight:

brick masonry basins

Extent of Mechanization:

fully mechanized

Mode of Operation:

semi-continuous, continuous

Power:

varies according to type of leaching procedure chosen, from 100 W for small percolation leaching plants (pump drive) up to several kW for larger agitation-leaching plants

Form of Driving Energy:

electric drive for pumps and filter

Technical Efficiency:

three various categories of efficiency are differentiated: leaching efficiency, adsorption efficiency (= f (activated carbon quality, etc.)), stripping efficiency (degree of stripping does not influence processing results if activated carbon is reused in the circuit because gold is not lost in the process) the sum of the different efficiencies leads to recovery values which lie at approx. 90 - 95 % for agitation leaching, approx. 80 - 90 % for vat leaching and ca 50 - 80 % for heap leaching.

Operating Materials:


Type:

sodium cyanide (NaCN) or calcium cyanide/black cyanide (Ca(CN)2)

Quantity:

Concentration: 1 - 5 kg/t (ave. 1,5), Consumption: up to 8 kg/t, compressed air, CaO, Zn and PbNO3 or activated carbon

ECONOMIC DATA:

Investment Costs:

for small percolation-leaching plants only minimal costs for the masonry construction of leaching basins, precipitating basins and leach collection containers, totalling approx. 1000 DM depending upon cost of materials. For industrial-scale plants, (e.g. CIP - carbon-in pulp process) costs are extremely high at 1.000.000 DM minimum.

Operating Costs:

high costs due to consumption of reagents, approx. 50 % of operating costs are for cyanide; also energy-intensive technique, especially the Merrill-Crowe-Procedure

Related Costs:

costs for sludge ponds, especially in leaching facilities where finely-ground ores are processed

CONDITIONS OF APPLICATION:


heap leaching

Operating Expenditures:

low |————|————| high


CIP

Maintenance Expenditures:

low—|high


depends on type of leaching

Personnel Requirements:

of extreme importance is a precise control of the process, especially with regard to the homogeneity of concentrations, feeds and slurry characteristics

Location Requirements:

very high space requirements for heap leaching

Grain Size of Feed:

< 0.1 mm for agitation leaching; <10 mm for vat leaching of 2 - 4 day duration; < 50 mm for heap leaching of 3 - 6 week duration

Special Feed Requirements:

minerals of arsenic, antimony, manganese and especially soluble oxidic copper, which are extremely deleterious and cause high cyanide consumption, high gold losses in organic CH-bonding, graphite, etc., require the use of CIL (carbon-in-leach process). Pyrrhotine (magnetic pyrite) is also a detrimental mineral: it binds cyanide ions and consumes oxygen during decomposition.

Replaces other Equipment:

all other methods of cleaning pre-concentrate in gold beneficiation, e.g. manual sorting, amalgamation, gravimetric processes, smelting

Regional Distribution:

worldwide more than 70 % of all gold is won by leaching. Cyanide leaching, however, is cost intensive, difficult to control and involves complicated technical equipment, restricting its application to large-scale mining operations.

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high


The dangers associated with leaching operation lie in the possibility of cyanide being released as a result of leaks, haphazard handling, etc. Cyanide is highly toxic; only trained personnel should operate leaching operations to ensure safe use; large space requirements heap leaching


heap leaching

Suitability for Local Production:

very good |————|————| bad


CIP

Under What Conditions:

for small percolation leaching plants, the simple brickwork provides very good possibilities for local construction

Lifespan:

very long |————|————| very short

Bibliography, Source: Krone/Erzmetall (German publication), Ullmann, Rollwagen in Erzmetall 41/2, Beyer, Bugnosen, DE 3429458 Al, Seeton, Meza S.

OPERATING PRINCIPLE:

Agitation leaching

The cyanide gold leaching exploits the ability of gold to build soluble cyanide complexes. Specifically, the ore is subject to the following procedure: After grinding of the raw ore to < 0,1 mm, the resulting slurry is treated with CaO as lime milk to bring the pH-value to around 10 · 11,5 and then thickened to 40 - 50 % solids (by mass). Sodium cyanide is added to the slurry in the agitation tank at a concentration of 100 ppm NaCN; the solids are held in suspension either by means of a stirrer or by injected compressed air (In Pachucas). At a pH-value of between 10 and 1 1,5, at which point the dissociation balance shifts In favour of the cyanide ions, the following chemical reaction takes place:

2Au + 4NaCN + 1/2 O2 + H2O ® 2NaAu(CN)2 + 2NaOH

The leaching duration lasts between 12 and 24 hours, producing solutions containing gold. concentrations of about 4 - 6 ppm.

Vat leaching

In vat leaching, pre-crushed or agglomerated ores in containers (vats) are flooded with a cyanide leaching solution of specified pH-value. The leaching process proceeds analagous to the above-described chemical process. At the end of the exposure time, a clear leachate solution is withdrawn through a filter tube.

Percolation leaching

Tailings derived from gravimetric beneficiation processes are often leached by percolation leaching. Large open tanks (of up to more than 100 m in volume) are equipped with a leachate outlet on the bottom, sometimes constructed as a double bottom with filter cloth or gravel. These tanks are filled with the ores to be leached, the leachate solution is alternately added and then allowed to seep down through the ore: the trickling speed should exceed 8 - 10 cm/h; rates below 2 cm/in are very disadvantageous, and indicate that the feed material requires prior desilting or desliming. After sprinkling of the leachate solution, the solution level sinks to the bottom, during which air and therefore oxygen for oxidation penetrate into the ore layer. This process is repeated daily for the duration of leaching, which ranges from a few days to more than a month.

The leachate can be added in varying concentrations, that is: first, highly concentrated, then less concentrated, and later as washing leachate.

Heap leaching

Depending upon the leachability, coarsely-crushed ore is placed onto a leakproof basin on the ground which has been sealed with clay, asphalt and/or a tarp covering. The ore is then doused with leachate solution. Upon completion of the leaching process, a clear gold-containing cyanide complex solution is drawn off.

Depending upon the nature of the gold-cyanide complex solution, various methods can be used for further processing:

For clear solutions:

- In the Merrill-Crowe Process the solution is separated from unsoluble components in a cloth-lined vacuum filter or a suspended filtering candle and is completely deaerated with a vacuum cylinder (otherwise oxidation occurs in subsequent steps which leads to high gold losses). The oxygen concentration is consequently reduced to about 0.5 mg/l. Following the addition of zinc dust and lead nitrate solution (from local elements), the cementation of the gold takes place according to the following reaction:

2 NaAu(CN)2 + 2Zn ® 2 Au + Na2[Zn(CN)4].

Gold and excess zinc are filtered through a filter press (the cyanide solution is re-circulated), and the solid materials are then treated with diluted sulfuric acid in order to wash out the excess zinc. The gold slime is then calcined at approx. 800° C and subsequently melted at 1200° C with borax and silicate fluxing agents.

- A significantly simplified variation, however associated with higher gold losses, is the zinc precipitation method. This is performed using a calotte of nested screens containing loosely-layered fine zinc shavings with large specific surface area The leachate solution is then applied from underneath, flowing upward through the screens. The gold separates out onto the zinc shavings and becomes visible as a black discoloration. When all the shavings are loaded with gold, these are melted and the gold collected (possibly performed by buyers or service organizations).

Recent patent literature also describes the cementation of gold from slightly-turbid cyanide leachate in reaction vessels filled with zinc granules and shaken by means of a vibrator which supposedly leads to faster cementing, higher recovery, lower zinc consumption, and a greatly simplified processing procedure.

- A third possibility is the CIC (Carbon in Column) Process in which clear gold-cyanide- complex solution flows from the bottom upwards through a cylinder filled with activated carbon, whereby the gold adsorbs onto the carbon. Activated carbon which is completely saturated with gold can contain as much as 20 - 30 kg gold/l, marketed either as ashed gold or as gold concentrate.

For slurries:

- In the Carbon-in-Pulp Process, in which granulated activated carbon is added to the slurry, the precious-metal cyanide complex is adsorbed onto the activated carbon. This is then mechanically separated (by screening) and washed out with a strong alkaline sodium-cyanide leaching solution, possibly under conditions of increased pressure and temperature; subsequently the gold is recovered electrolytically by collecting it together with silver and copper on steel wool electrodes. Upon completion of the process, the activated carbon must be regenerated (a costly endeavor). Alternatively, the gold-saturated activated carbon can be incinerated to ash.

- Gold-containing ores that also contain organic substances (which as semi-activated medium can potentially absorb gold from the leachate), are processed using the CIL (Carbon-in-Leach-Process), in which the leachate already contains the activated carbon when it is added to the ore. The more active carbon absorbs, which can then be mechanically separated as described above for the CIP Process. Slurries with a small proportion of suspended material can be filtered in gravel-bed filters; this is the cheapest method, involving the least equipment, for purifying solutions.

For purifying slurries, the CCD method (counter current decantation) is also applied, a process in which several thickeners are charged in counter-current system (opposite direction); the thickened sludge from one is again fed back into the previous thickener, and the overflow is directed into the next thickener.

REMARKS:

The process was developed in South Africa in 1889.

In agitation leaching operations, the leaching can partly begin already in the mill by performing wet grinding in a cyanide leach. This has the advantages in that absolutely fresh (uncontaminated) mineral surfaces come into contact with the solution.

In the ClP-Leaching, it is often the extremely high cost of the activated carbon which renders the procedure uneconomical in developing countries. At the same time, there are good possibilities in many areas in developing countries where activated carbon could be locally produced. Raw materials such as coconut husks are particularly well suited for such purposes. Coconut shell carbon is known particularly for its hardness and fine porosity. However, the raw material, namely the coconut shells, which are usually used as heating fuel, are relatively expensive. Moreover, the quality standards are very high: the shells must be clean and very fresh. For these reasons, imported activated carbon has been employed so far in small-scale mining in developing countries.

High costs occur due to consumption of reagents, particularly the consumption of cyanide through oxidation, release of HCN and reactions with accompanying substances in the ores. In ClP-leaching, abrasion of the loaded activated carbon is problematic (gold losses).

The agitation leaching processes ground products or finely-crushed ores, the vat leaching processes pre-crushed ores, the heap leaching processes coarsely crushed crude ore. Heap leaching is less expensive, but with respect to the comparatively low recovery (approx. 50 %) is less recommended (the process is better suited for low grade ores). Ores which can be leached in the stockpile in a coarsely-crushed form are rare. Gold particles which, for example, are bound within quartz cannot be leached without grinding to liberate them.

Tailings from gold leaching operations must be stockpiled or collected in a sludge pond. Excessive CN-contents decompose over time under the influence of ultra-violet radiation.

In general, agitation leaching and vat leaching, and also heap leaching for easily-leachable ores, appear to be the most suited for small-scale mining; these methods require substantially less equipment for the leaching, adsorption and winning of gold from clear slurries than other methods.

High temperatures tend to cause decomposition of cyanide leaching solutions, whereas low temperatures drastically reduce the speed of reaction. The economical optimum lies at a leaching temperature of about 20 C, which in colder climates is attained through artificial heating. In all cases, leaching tanks and vessels should be covered since UV-radiation leads to decomposition of the leaching solution.

To avoid environmental hazards, leaching tanks and vessels should be covered on top with wire mesh to prevent humans, animals and especially birds from gaining direct access to the toxic solution. Pachuca tanks for compressed-air agitation leaching of the slurry have a height which corresponds to at least three times the diameter of the tank.

Leaching tanks for percolation leaching should not be too deep. Very deep tanks inhibit the penetration of air during the sinking of the leachate level, thereby insufficiently supplying the ore with the necessary oxygen for leaching.

Leached ores can be removed from vat leaching plants and tanks by means of a bottom gate or, even simpler, by flushing with large quantities of water.

Cyanide leaching allows the processing of a very wide spectrum of gold ores, for example, ores with fine-grained free gold (down to sub-microscopic gold occurences such as in vulcanises or carbonates), gold from soluble sulfides, and gold attached to the surface of sulfides. Refractory ores, for example, with gold-containing pyrites are not leachable without further processing (e.g. roasting).

Ores which exhibit varying intergrowth relationships can be selectively comminuted in order to attain liberation without overgrinding. Ores with coarse gold intergrowths in quartz or with finer gold intergrowths in sulfides and their interspaces are frequently encountered. In this case, the sulfides from the primary grinding circuit can be gravimetrically separated (for example in a jig) and selectively finely ground in a second grinding circuit.

Gold-containing cyanide leachates should always be immediately further treated, otherwise there is danger that colioids (mostly aluminum, iron or magnesium hydrates) settle out of the clear solution which hinder the precipitation of gold onto the zinc shavings or zinc dust. Furthermore, the Ca-rich leachates can precipitate calcium carbonate by absorbing CO2 from the air.

Zinc wool for precipitation should have a thickness of approx. 0.02 mm. It then exposes between 10 and 20 m² of specific surface area pro kg and has a volume of approx. 10 lifers. Optimal quantities are approx. 30 lifers of zinc wool for every m³ leachate/24 hours. Solutions which have passed through the zinc wool precipitation are dropped into the supply tank from greater heights so as to enrich it with oxygen as it falls through the air.

High, cylindrical leach tanks, such as pachucas, can be built out of cement rings stacked on top of each other. For leaching in an acidic medium (for example, with thiourea), these cement rings can simply be lined with synthetic resin.

Leaching is especially suitable for ores containing fine-grained gold particles of high specific surface area With feed of coarser grain-size fractions the leaching speed drops. Therefore, these coarser fractions are usually separated in a prior gravity beneficiation, leaving only the tailings and the fine fractions to be leached.

Leaching speed may be increased by leaching under pressure; this method, however, is characterized by enormously high investment costs and is therefore not appropriate for small-scale mining.

EXPERIENCES IN LEACHING IN SMALL-SCALE MINING:

In Brazilian gold mining at its smallest scale, a technique could be observed in which raw ores are mixed with cement via shovelling and thus agglomerated. A leaching process which produces pure solutions is conducted in small vessels (for example, diesel barrels). The adsorption of the gold-cyanide-complex takes place on locally produced Babacu-nut-carbons, which are subsequently incinerated to ashes.

In small-scale gold ore mining in Colombia and Ecuador, percolation leaching plants are in operation in which the tailings from amalgamation plants and gravimetric beneficiation processes are leached. Here the slurry-flow falls in a sedimentation basin, which has the effect of desilting the sands. The sedimented material is then sufficiently permeable to produce a pure solution during leaching. The brick leaching tanks have a capacity of 20 - 100 t and are situated above the precipitation basin in which the gold is precipitated onto the zinc shavings. Subsequently, the solution drains into the leachate supply tank. A small pump, driven by a gasoline-engine, pumps the leachate into the leaching tank once daily. The investment costs for this type of facility are minimal and, depending upon the cost of building materials and wages, total less than 5000 DM.

Electrolytic separation of gold from the cyanide leachate is performed in Philippine mining using locally-produced cells constructed from batteries, where the anodes are made of stainless-steel screen mesh and the cathodes of steel wool The gold-containing leachate continuously flows through these cells in which a 12 V, 60 A electrical current has been applied The gold is later shaken out of the steel wool and collected, and the steel wool reused.

SUITABILITY FOR SMALL-SCALE MINING:

Cyanide leaching yields high recovery particularly in the beneficiation of ores containing fine gold fractions. However, its dependence on large quantities of reagents, some toxic, and the difficulties in controlling the processes are problematic for small-scale mining application. In medium-scale plants where specialized knowledge is readily available, gold leaching is an economic alternative which can even serve, among others, as a substitute for the environmentally detrimental amalgamation processing.


Fig.: A zinc precipitation plant made of wood. Source: Armstrong.

15.12 Gold separation by smelting

Gold Mining
Beneficiation, Gold Beneficiation

germ.:

Schmeiztrennung von Gold

span.:

separacion del oro por fundicion

TECHNICAL DATA:

Dimensions:

oven approx. 1 × 1 × 1 m

Throughput/Capacity:

thermal heating up to about 1200° C

Form of Driving Energy:

gasoline, oil, coal or wood burner; or electric oven

Mode of Operation:

intermittent

Technical Efficiency:

very high recovery

Operating Materials:


Type:

various fluxing agents, coating agent and precious-metal collector (the latter only when fire assay is applied (Dokimasie))

ECONOMIC DATA:

Investment Costs:

refractory (fireclay) crucible, graphite crucible, oxide-ceramic crucible, crucible tongs, agitator, mortar, iron crucible, and heating facility (crucible oven) to 2.000° C, totalling about 5000 DM when of Latin American production

Operating Costs:

cost of energy, labor costs, cost of reagents, cost of crucibles (20 to 35 (max) melts/crucible)

Related Costs:

possibly cost of presses for the manufacture of crucibles and cupels.

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Personnel Requirements:

extensive experience is necessary, especially for the quantitative separation by fire assay

Recovery:

through the use of precious-metal collectors, recovery can be quasi quantitative (100 %)

Replaces other Equipment:

as a beneficiation technique, replaces other methods for winning pure gold from pre-concentrates, e.g. hand picking. As an analytical technique, fire assay is the simplest, fastest and above all the most accurate method of gold analysis.

Regional Distribution:

in gold analysis worldwide, as a beneficiation technique very rare

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high


during use of this process, gases of volatile and possibly toxic components are emitted into the atmosphere; also, depending upon energy source, detrimental exhaust gases.

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

oven cannot be locally produced by non-specialized manufacturing plants; crucibles and cupels can be locally manufactured

Lifespan:

very long |————————| very short


short service life especially of crucibles and cupels

Bibliography, Source: Chemikerausschu� der GDMB

OPERATING PRINCIPLE:

To separate gold from the heavy minerals, the enriched pre-concentrate is placed in a crucible with borax and baking powder or ammonium chloride (NH4CI) and heated to a temperature of 1200° C. This causes the oxidic minerals such as limonite, ilmenite, etc. to melt. In the solid-liquid system which is created, liquid gold concentrates at the bottom of the crucible underneath the slag. The melting temperature of gold is 1063° C.

In the "fire assay" method, the material to be separated, normally a sample for determing precious metal content, is melted together with the excess lead and flux. Through the addition of oxidation or reduction agents, as well as slag-forming agents, the melt separates into the precious-metal containing lead regulus and a slag extensively free of precious metals. The lead regulus is then separated and further processed by the so-called cupellation process. The regulus is heated in a cupel a crucible made of bone ashes - whereby the lead is oxidized in the liquid melt and is either volatized or absorbed by the cupel material (especially the magnesium component therein). What remains is an almost perfectly round preclous-metal grain which allows precise quantitative conclusions to be drawn, either by weighing or by size-comparison with a linear scale, concerning the Initial content of the feed material.

AREAS OF APPLICATION:

Melting to produce pure precious metals from concentrates, employed as a separation technique In small-scale mining.

Fire assay, as the most important method of analysis for gold contents in mined ore, can no longer be ignored; In addition to free gold, other gold occurrences, such as gold contained in pyrite, can also be determined.

REMARKS:

This technique or method is not applicable for platinum group metals due to their significantly higher melting point (platinum 1769° C, rhodium 1966° C, palladium 1550° C, osmium 2700° C, iridium 2454° C).

As an analytical method, fire assay captures and reveals the entire gold content of a sample, including the diadochic contents in the pyrite lattice such as dispersed gold. The recoverable free-gold contents are determined by panning.

Cost of analysis with imported crucibles and cupels is about 4 - 6 US$ per sample, compared to 2 - US$ when locally. manufactured crucibles and cupels are used. Crucibles of clay can be locally formed and fired. It must be taken into consideration, however, that only clay which is completely free of gold should be used, since during melting the crucible material is also melted, and any gold contained in the crucible material could accordingly alter the analytical results. Cupels can also be locally manufactured from a mixture of bone ashes or magnesium and common, commercially-traded cement.

SUITABILITY FOR SMALL-SCALE MINING:

Gold separation by smelting is an inexpensive and very accurate method of achieving marketable products when the concentration of gold is adequate (determined by previous sample melting). Fire assay is the most Important analytical method for determing gold contents in ores.

Cupels made of Bone Ashes

Size

Upper diameter mm

Lead adsorption capacity gr

Height mm

Weight gr

1

22

4

11

4

2

24

7

13

7

4

30

13

14

13

5

33

18

16

18

6

35

24

18

24

7

40

30

19

30

8

50

60

25

60

9

60

100

27

100

10

88

300

33

300

Fig.: Cupels: sizes, lead-adsorption capacity and shape.
Source: Frick-Dausch

Table: The most important sample reagents. Source: Frick-Dausch

Name of Sampler

Composition

Tasks and Characteristics

Quartz

SiO2

scorification, fluxing agent, acidic

Glass

x Na2O y CaO z SiO2

scorification, fluxing agent, acidic (weaker than quartz)

Borax

Na2B4O7 10H2O

scorification, fluxing agent, acidic

Borax glass or molten borax

Na2B4O7

scorification, fluxing agent, acidic

Phosphorus salt

Na(NH4)HPO4 4H2O

scorification, fluxing agent, seldom used

Soda

Na2CO3

scorification fluxing agent, desulfurization

Sodium bicarbonate

NaHCO3

scorification fluxing agent, desulfurization

Potassium carbonate



(Potash)

K2CO3

scorification, fluxing agent, desulfurization

Lead (II) oxide

PbO

scorification, fluxing agent, desulfurization,



oxidizing, collector, basic

Tartaric

KHC4H4O6

reducing agent and basic fluxing agent

Charcoal


reducing agent

Flour


reducing agent

Potassium Cyanide

KCN

reducing agent and neutral fluxing agent

Iron

Fe

reduing agent, desulfurization, basic scorification agent

Salpeter (salts of nitric acid)

KNO3 (NaNO3)

oxidizing agent, desulfurizination, basic fluxing agent

Assay lead

Pb

collector

White lead

2 PbCO3 Pb(OH)2

collector, also desulfurizing, oxidizing basic fluxing agent

Lead acetate

Pb(CH3COO)2 3H2O

collector, sometimes also desulfurizing basic fluxing agent

Sodium chloride

NaCI

coating agent

Fluorite

CaF2

inert neutral fluxing agent

Greenland spar cryolite

Na3AlF6

dissolves Al2O3

Ammonium carbonate

(NH4)2CO3

desulfurizing, volatilizing

1 The earlier common names have been kept


Fig.: Phase diagram of gold-lead melting. Source: Frick-Dausch.


Fig.: Crucible tongs. Source: Frick-Dausch. a) strainght from; b) curved form


Fig.: Mold for fire assay. Source: Frick-Dausch.


Fig.: Standardized reference scale for the determination of gold content from fire assays. Source: Frick-Dausch.

15.13 Gold-coal-agglomeration

Gold Mining
Beneficiation, Gold Beneficiation

engl.:

coal-gold agglomeration, CGA

germ.:

Gold-coal-agglomeration

span.:

aglomeracion oro-carbon

TECHNICAL DATA:

Extent of Mechanization:

fully mechanized

Power:

for agitating and pumping, several kW

Form of Driving Energy:

electric for mixing, agitating

Throughput/Capacity:

not known, since it has not yet been applied in large-scale industrial operations, British Petroleum operates with a 1 t/h pilot plant (see House), 30 min contact time gave optimal results

Technical Efficiency:

loading of the agglomerate in large-scale plant operations to between 1000 and 5000 g/t is possible

Operating Materials:


Type:

oil, activated carbon

ECONOMIC DATA:

Investment Costs:

not known

Operating Costs:

high cost of reagents, conservative cost estimates show that operating costs for CGA are less than those for leaching

Related Costs:

costs of grinding and settling basin, thickener or sludge pond for treating tailings

CONDITIONS OF APPLICATION:

Grain Size of Feed:

0.2 - 200 ym gold particles can be agglomerated

Special Feed Requirements:

gold, electrum (Ag-bearing Au), gold telluride, also for ores with significantly less than 1 g Au/t

Recovery:

over 90 % in pilot plants

Replaces other Equipment:

this technique is used for obtaining meltable gold concentrates and should replace amalgamation, leaching, and other methods.

Regional Distribution:

so far not applied in large scale operations; used in pilot plants in Australia

Operating Experience:

information not yet available

Environmental Impact:

low |————|————| very high


high sludge loading; pollution through discharge and consumption of reagents, which are produced by highly energy-intensive and environmentally detrimental processes (for example the production of activited carbon). Positive effect if it proves successful as a substitute for amalgamation.

Bibliography, Source: F 530793, USA 4, 597, 791, House

OPERATING PRINCIPLE:

In a BP-gold-coal-agglomeration pilot project, the high-grade gold-containing fine-grained slurry is transposed by activated carbon into an oil suspension. The hydrophobia of the gold is being utilized in this process. The gold then agglomerates onto the oil-saturated activated carbon particles. Following agitation of the slurry-reagents-mixture, the gold-oil-activated carbon agglomerate is mechanically separated.


CGA Process Flowsheet:

SUITABILITY FOR SMALL-SCALE MINING:

Suitability for small-scale mining application is not yet assessible due to insufficient operational data.

CLOSE THIS BOOKTools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)
Technical Chapter 16: 0ther Sorting and Separating Techniques
VIEW THE DOCUMENT16.1 Roasting oven, calcining furnace
VIEW THE DOCUMENT16.2 Salt gardens, salt works, salterns
VIEW THE DOCUMENT16.3 Sulfur production in heap smelting or chamber ovens
VIEW THE DOCUMENT16.4 Autoclaves for extracting sulfur
VIEW THE DOCUMENT16.5 Copper sulfate plant
VIEW THE DOCUMENT16.6 Electrostatic sorting
VIEW THE DOCUMENT16.7 Flotation

Tools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)

Technical Chapter 16: 0ther Sorting and Separating Techniques

16.1 Roasting oven, calcining furnace

Metal Mining
Beneficiation, Special Techniques of Separation

germ.:

Abrostofen

span.:

horno de calcinacion

TECHNICAL DATA:

Dimensions:

oven deck plate approx. 2 × 1 × 0.1 m

Weight:

approx. 50 kg

Form of Driving Energy:

thermal energy from heat of combustion

Operating Materials:


Type:

Fuels: oil, coal, gas or wood, possibly NaCI for chloridized roasting

ECONOMIC DATA:

Investment Costs:

when locally produced < 200 DM

Operating Costs:

high energy and fuel costs

Related Costs:

cleaning of exhaust gases

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————————| high

Maintenance Expenditures:

low |————|————| high

Location Requirements:

large quantities of fuel have to be made available or be transported

Special Feed Characteristics:

ores may contain sulfides but no! arsenic, selenium or mercury

Recovery:

after a sufficient retention period the feed oxidizes quantitatively (i.e. nearly 100%)

Regional Distribution:

Bolivia

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high


during roasting of sulphidic ores large quantities of sulfur dioxide are released; additionally there is a high risk of possible release of very volatile and highly toxic metals, such as mercury, arsenic and selenium amongst others, either as elements or oxidized

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

simple metal construction on top a brick oven foundation

Lifespan:

verylong |————|————| very short


depends on the aggressiveness of the roasted products

Bibliography, Source: Ullmann

OPERATING PRINCIPLE:

Roasting is a thermal process for eliminating sulfides, whereby the sulfide and other sulfide-compounds are oxidized, e.g:

2FeS + 3½O2 ® Fe2O3 + 2SO2

This reaction begins at approx. 105° C if there is sufficient oxygen partial pressure. The products to be roasted are spread out on a flat pan-shaped furnace plate and heated to over 105° C.

SPECIAL AREAS OF APPLICATION:

Roasting is performed when it is necessary to free oxidic concentrates of sulfide, for example tin-ore and wolframite concentrates. In addition, sulfide-containing gold ores are roasted prior to being leached with cyanide.

AREAS OF APPLICATION:

For purifying gold concentrates. This involves the roasting of high-grade pre-concentrates, whereby hematite and other iron minerals are broken down and, following a brief grinding, are pulverized into powder. The product is then freed of Fe-mineral fines by means of air (wind) classification or simple manual blowing.

REMARKS:

During the roasting process, large quantities of volatile, gaseous sulfur dioxides are generated. When, besides sulfides, arsenic, selenium or mercury compounds are also present in the products, volatile compounds of these elements also develop. The vapors or gases of these compounds are all highly toxic, and therefore it is not advisable to operate small roasting plants without cleaning of gas emissions.

For special requirements, such as to acquire easily-soluble halide for the leaching process or to eliminate high-metting-point minerals, chlorinated roasting can be performed under addition of common salt (sodium chloride).

SUITABILITY FOR SMALL-SCALE MINING:

The use of roasting ovens is appropriate for small-scale mining needs only in special cases since they are highly detrimental to the environment.

16.2 Salt gardens, salt works, salterns

Salt Mining
Beneficiation, Special Techniques, of Separation

germ.:

Salzgarten, Salinen

span.:

salines

TECHNICAL DATA:

Depositional surface area:

crystallization area: depends on seasonal climate fluctuations; ratio of evaporation to crystallization area = 1: 7

Dimensions:

storage ponds: approx. 1 m in depth; large ground basins, evaporating ponds: approx. 20 cm in depth; crystallisation ponds: approx. 20 cm in depth, thickness of brine layer in crystallisation ponds can be as shallow as a few millimeters

Driving Energy:

seasonally changing solar energy between approx. 5000 and 30.000 kJ/ha/year

Form of Driving Energy:

direct use of solar energy

Throughput/Capacity:

evaporation: approx. 0.2 - 0.5 (1.5) cm/day, approx. 100 - 300 t/ha/year

Technical Efficiency:

approx. 43 m³/t NaCI produced

ECONOMIC DATA:

Operating Costs:

mainly labor and pumping costs

Related Costs:

possibly secondary cleaning facility, rakes and shovels for harvesting salt; possibly tractors, shovel loaders, etc.

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Location Requirements:

location should be characterized by extensive sunshine and low atmospheric humidity (high evaporation potential)

Special Feed Requirements:

ocean saltwater or water (brine) from salt lakes of saltwater composition: NaCI 2.723 %; MgCI2 0.334 %; MgSOA 0.225 %; CaSO4 0.120 %; KCI 0.076 %; NaBr 0.010 %; CaCO3 0.011 %; H2O 96.495 %

Regional Distribution:

technique is distributed worldwide; approx. 30 % of the world production of NaCI is produced by evaporation and crystallization of saltwater.

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————————| very high


space requirements, possibly damage to sea-coast areas

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

simple, but involves very large surface-area excavations, possibly excavation machinery needed

Lifespan:

very long |————|————| very short

Bibliography, Source: Ullmann, Muller

OPERATING PRINCIPLE:

The winning of NaCI in salt gardens is achieved by evaporating saltwater (from oceans, seas, or salt lakes) according to the separation procedure listed below. The crystallization ponds are fed in such a way that carbonates and gypsum are precipitated separately, as the following processing steps indicate:

1. Pumping of saltwater into the initial evaporation ponds.

2. Concentration of the brine in these ponds to a density of approx. 6.5° Be (Baume-Scale: 6.5 mass-% salt solution).

3. Transfer of this pre-concentrated brine to a second evaporation zone, where the evaporation continues up to 17° Be; at this density the bulk of the gypsum precipitates out

4. Transfer to a third evaporation zone, where the brine reaches the saturation point for NaCI. At 20° C the corresponding density is 25.6° Be.

5. Transfer of the saturated brine into crystallization ponds, where density may not exceed an upper limit of 29 - 30° Be. In this way approx. 23 kg NaCI can be won from 1 m of saltwater, while the manganese and potassium salts remain in the mother liquor (spent solution).

6. Removal of the mother liquor from the cristallization pond.

7. Harvesting of the salt.

AREAS OF APPLICATION:

Used for production of common table salt and NaCI for other purposes (e.g. electrolysis) from ocean saltwater and water from saltwater lakes. Bromine and magnesium compounds, as well as potassium salts, could also be separated and won as by-products. Chloridic mother liquors from salt lakes are then further evaporated and subsequently processed in a subsequent flotation facility where sylvinite for use in KCI production is floated out.

REMARKS:

Micro-organisms, plankton, algae and halophillic bacteria have an important influence through their ability to accelerate evaporation due to their radiation-absorbent coloring. The growth of micro-organisms can be enhanced by the addition of nutrients rich in nitrogen or phosphorus.

In situations where the salt is too greatly contaminated by magnesium and gypsum, it can be purified by a washing process in which the salt is washed in a screw conveyor with a saturated counter-current NaCI solution. Gypsum is removed in the float, and Mg-salts dissolve into the solution. The remaining product is dewatered in a hydro-cyclone and then centrifuged.

The average composition of common table salt is:

NaCI:

99.50 % (dry matter)

CaSO4:

0.25 %

MgCI2:

0.15 %

MgSO4:

0.01 %

KCI:

0.02 %

Insoluble residue:

0.02 %

Residual moisture:

3.00 %

Separation sequence of evaporation of ocean saltwater at 27° C:

Remaining saltwater

Initial separation of


100.00

calcite

CaCO3

32.22

gypsum

CaSO4

12.13

halite

NaCl

2.45

astrakanite

Na2SO4 × MgSO4 × 4H2O

2.18

epsomite

MgSO4 × 7H2O

1.96

kainite

MgSO4 × KCl3 H2O

1.63

hexahydrite

MgSO4 × 6 HgO

1.22

kieselite

MgSO4 × H2O

1.18

carnallite

KCl × MgCl2 × 6H2O

0.93

bischofite

MgCl2 × 6 H2O

In the production of potassium salts, it must be taken into account that the demand for agricultural fertilizer is subject to vast seasonal fluctuations, requiring large-capacity covered (weather-tight) storage facilities.

Small amounts of common salt can also be won by collecting precipitated salt crystals developing from salt water sprayed along the sea coast, for example on the cliffs along the shores of the Sinai Peninsula, at Cape Verde, etc.

In polar climates, smaller amounts of salt freeze when water sprays onto pack-ice and freezes, causing salt to crystallize out (Rassol). The freezing procedure is also utilized at an industrial scale for concentrating salt brines in cold climatic regions.

Besides the production of salt from ocean saltwater, production from dry, or former, saltwater lakes in the steppe, desert and high-altitude desert areas of Latin America is of great regional importance. Here, the actual winning of salt occurs by cutting the salt with huge axes into "Quader" or rectangular blocks (panes) weighing approx. 10-15 kg. To remove the most recent, or uppermost, crystallized epsom (bitter) or waste salts, the top layer is split off about 3 cm down. The further processing takes place in small milling plants in which the salts are coarsely crushed and then ground to the desired final grain-size.

Mined salts are, in some cases, heavily contaminated with bituminous substances or other minerals such as gypsum, quartz or a number of others. In order to clean them, the salts are dissolved, possibly boiled, and then enriched into pre-concentrates in cooling towers before being crystallized either under the influence of natural evaporation or by heating.

Rainfall hinders the operation of salterns or salt gardens. The diluting influence of rain water may be countered either by covering the crystallisation basins with plastic film or cement roofs, by diverting the highly-concentrated saltwater into deep, covered rain ditches, or by draining off the lighter (lower specific-density) rain water over an overflow weir.

Salt gardens are always built so that the initial solution, for example sea water, is conveyed by means of a pump into the highest-situated initial evaporation ponds. From here, the saltwater is discharged over weirs without pumps to the lower-lying subsequent evaporation steps and crystallization ponds.

SUITABILITY FOR SMALL-SCALE MINING:

The production of salt in salterns is, in terms of investment requirements, a typical small-scale mining technique which, given a suitable location, yields high specific production quantities and high-quality products.

16.3 Sulfur production in heap smelting or chamber ovens

Mining on Industrial, Minerals and Rocks
Beneficiation, Special Techniques of Separation

germ.:

Schwefelgewinnung im Schmelzmeiler, Kammerofen

span.:

recuperacion de azufre en carboneras de fusion, horno de cameras

ital.:

calcarone, calcarelli

TECHNICAL DATA:

Dimensions:

diameter up to 30 m, height up to 6 m, with inclined bottom (approx. 15° - 20°)

Weight:

brick masonry

Extent of Mechanization:

not mechanized

Form of Driving Energy:

energy of combustion

Mode of Operation:

intermittent

Technical Efficiency:

30 - 60 % recovery, in chamber oven up to 78 %

Operating Materials:


Type:

sulfur as fuel

ECONOMIC DATA:

Investment Costs:

depends on possibilities for purchasing construction material, starting at approx. 1000 DM

Operating Costs:

mainly labor costs

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Location Requirements:

atmospheric partial pressure of oxygen must be sufficient to burn sulfur; for this reason the maximum topographic elevation is limited.

Recovery:

comparably low in heap smelting due to losses caused by capillary forces and burning of sulfur

Replaces other Equipment:

autoclaves

Regional Distribution:

Sicily


chamber oven

Experience of Operators:

very good |————|————| bad


heap


due to the low degree of melting

Environmental Impact:

low |————|————| very high


due to emission of H2SO3 (sulfurous acid)

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

masonry work

Lifespan:

very long |————|————| very short

Bibliography, Source: Ullmann, Buch der Erfindungen "Book of Inventions" (in German) 8 edtn..lV. Bd.

OPERATING PRINCIPLE:

The simple method of winning sulfur by smelting is performed in mounded ore piles, in which sulfur is openly piled against a brick wall (with drainage outlet) where it partially burns and partially melts. The losses of sulfur due to the combustion reaction to sulfur dioxide can exceed 60 %. In order to extract sulfur in a smelting pile, small-lumped feed material is piled into a round brick-walled construction 10 to 30 m in diameter and up to 7 m in height, and covered with spent melt, gypsum and clay. The pile is ignited on the surface, opposite the drain outlet at the deepest point in the pile, in order to generate heat to melt the sulfur. The burning is controlled through the exhaust outlet and openings in the cover. The duration of the smelting process in such a pile lasts about 3 weeks. The sulfur is extracted from the lower end and allowed to crystallize in flat basins or moistened wooden molds, such as is described for autoclaves.

Better smelting results can be obtained with the chamber oven, in which already-melted residues with residual sulfur content are burned, generating hot gases which are then directed through a duct into a second chamber where they serve as the heat source for smelting sulfur out of fresh raw ore. A multi-chamber design avoids the need to re-handle the ore, since the melted ore is burned in a second processing step, thus using the smelting chamber as a combustion chamber.

AREAS OF APPLICATION:

To extract sulfur from raw ore of volcanic or sedimentary deposits containing elementary sulfur.

REMARKS:

The burning of sulfur to produce hot gases for smelting purposes requires high partial pressure of oxygen. At the high altitude of the Andes, where many volcanic deposits of sulfur are being mined at elevations of up to 6000 meters above sea level, the air pressure is not sufficient for burning sulfur. In this situation, the mine operators resort to the autoclave technique which uses steam for smelting.

Chamber ovens can also process feed containing < 15 % S, and are therefore often used for reprocessing residual material from autoclave processing.

Due to its non-dependence on external fuel and its non-mechanized technology devoid of high investment costs, smelting In chamber ovens is very economical.

SUITABILITY FOR SMALL SCALE MINING:

Due to the high environmental Impact associated with the winning of sulfur in smelting-piles, the use of this method is only appropriate in situations where other fuels are not available. At high altitudes the partial pressure of oxygen is not sufficient for combustion, so that the use of chamber ovens or smelting piles is not possible.

16.4 Autoclaves for extracting sulfur

Mining of Industrial Minerals and Rocks
Beneficiation, Special Techniques of Separation

germ.:

Autoklaven zur Schwefelgewinnung

span.:

autoclave pare la recuperacion de azufre, recuperacion de azufre en autoclaves

TECHNICAL DATA:

Dimensions:

horizontal, slightly inclined cylindrical boiler approx. 1 m in diameter, 4.75 m in length; or vertical, of cylindrical dimensions

Form of Driving Energy:

thermal steam-energy from combustion

Alternative Forms:

preheating of water with flat-plate or concentrating solar collectors

Technical Efficiency:

depends on feed content of ore and absorptive capacity of host rock

Operating Materials:


Type:

water fuel, e.g. in Bolivia plant material llareta (Lat. azorella compacta)

Quantity:

approx. 5 m³/t S

ECONOMIC DATA:

Operating Costs:

very high fuel costs

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Location Requirements:

sufficient fuel must be available, or possibilities must exist to transport fuel in large quantities. Grain size of feed: the ore is fed as lumps, but sizes > 20 cm should be avoided due to the low thermal conductivity of sulfur.

Special Feed Requirements:

S content of feed should be as high as possible, which is achievable by selective mining, hand picking of rocks or preliminary flotation.

Output:

In contrast to the extraction of sulfur by heap melting or in chamber ovens, the autoclave process is highly independent of altitude. In Bolivia there are autoclaves in use at altitudes exceeding 4500 m above sea level.

Replaces other Equipment:

heap smelting, chamber oven

Regional Distribution:

in small-scale mining in Latin America, especially in the high-altitude cordillera region

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high


through waste deposition, gas emissions from steam-generating oven, and destruction of vegetation through the use of biogenic fuels

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

local construction companies

Lifespan:

very long |————|————| very short

Bibliography, Source: Ullmann

OPERATING PRINCIPLE:

To smelt sulfur in autoclaves, the lumpy feed is charged into vertical or horizontal cylindrical boilers in layers. The boilers are pressure-sealed following charging, and injected with hot steam at 4 - 5 bar, during which the thermal energy of the steam is transmitted to the ore. At temperatures exceeding 114°C, the surphur begins to melt. It is important that the steam continues to flow through the heaped feed material, since, on the one hand, sulfur is a poor heat conductor, and on the other hand, there is a sharp increase in dynamic viscosity of the melt above 158°C, which has a viscid (semifluid) effect. The melted sulfur flows downward and is discharged periodically through the bottom outlets, from which it then flows into large flat basins where the dark-brown sulfur melt cools down during crystallization and turns into a solid yellow mass. When this mass has reached a thickness of 30 - 50 cm it is manually broken up by means of crowbars and carried off as blocks. The spent melt is removed from the autoclave following depressurization of the melting chamber and discarded as waste. To simplify material transport, the feed material for horizontal autoclaves is brought into the melting chamber in small wagons. Depending upon the composition of the feed, this material still contains significant amounts of sulfur which either could not flow out during melting, or remained in capillary bonds. The recovery from technical-scale plants ranges between 47 % and 55%.

AREAS OF APPLICATION:

Used to extract sulfur from raw ore feed preferably containing > 25 % S. When the S-content is lower, the feed can be pre-concentrated via flotation and then dewatered prior to smelting in autoclaves.

REMARKS:

The energy costs for generating steam are extremely high. In small scale mining in the western cordillera region in Bolivia, a resinous plant is used as fuel. In any event, it should be investigated whether fuel consumption could be reduced by empoying solar energy collectors to preheat the water to just below the boiling point.

Alternatively, the melted sulfur can be poured into moistened wooden boxes, with inclined walls, and then recovered in the form of uniform castings.

SUITABILITY FOR SMALL-SCALE MINING:

Autoclaves are suitable even at high altitudes for the winning of sulfur from high-grade ore feed; however, the high energy consumption creates logistical, economical and ecological problems.

16.5 Copper sulfate plant

Metal Mining
Beneficiation, Special Techniques of Separation

germ.:

Kupfersulfatfabrik

span.:

fabrica de sulfato de cobre

TECHNICAL DATA:

Extent of Mechanization:

not mechanized/semi-mechanized

Operating Materials:


Type:

H2SO4, possibly fuel

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Replaces other Equipment:

production of sulfide copper concentrates

Regional Distribution:

Bolivia

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high


minimal environmental impact due to acidic residues in the tailings. With oven drying, very high impact due to destruction of vegetation and/or gas emissions.

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

masonry construction: tanks, drying basins, crystallization basins

Lifespan:

very long |————|————| very short

Bibliography, Source: Mina Azurita/Bolivia

OPERATING PRINCIPLE:

To produce a copper sulfate, the feed material is placed in a large reaction-tank (basin), soaked with a diluted sulfuric acid solution, and left to react for approx. 2 weeks. The resulting copper sulfate solution is then concentrated either by solar thermal evaporation of the water, or by heating over a fire in drying-calottes made of lead vessels. When the solution reaches the point of saturation, it is pumped into crystallization tanks where copper sulfate crystals form along the bottom and walls, and on iron-wire spirals hung from above.

AREAS OF APPLICATION:

The production of copper sulfate from raw ore, tailings piles, or beneficiation wastes is suitable for feed which is porous, rich in weathered copper minerals, rich in sulfides or sulfates, and of low iron content. During leaching of such material, sulfide is transformed through partial oxidation (supported by bio-catalyzation) into H2SO4 over H2SO3.

REMARKS:

In the vegetation-poor highlands of Bolivia, a three-man copper sulfate operation for processing old tailings piles has proven economical despite high energy and transportation costs.

SUITABILITY FOR SMALL-SCALE MINING:

Suitable technique for the processing of low-grade sulfidic and oxidic copper ores with relatively low investment costs.

16.6 Electrostatic sorting

Ore Mining, Mining of Precious Stones, Gold Mining, Salt Mining
Beneficiation, Special Techniques of Separation

germ.:

Elektrostatische Sortierung

span.:

concentracion electrostatica

TECHNICAL DATA:

Dimensions:

1 - 3 m in height

Weight:

large units are several thousand kg

Power Consumption:

electrical separation efficiency, voltages lie within the range of 5 - 90 kV at field strengths of 3 - 9 kV/cm several 100 W plus roller drive

Form of Driving Energy:

electrical

Alternative Forms:

none

Throughput/Capacity:

up to 5 t/h, in potash up to 25 t/h

Technical Efficiency:

comparatively low degree of separation in one processing step, therefore electrostratic separation always involves a multiple-step procedure

Operating Materials:


Type:

surface-active or chemosorptive substance, tensides for selective separation of various non conductors

ECONOMIC DATA:

Related Costs:

drying, preparation, conditioning

CONDITIONS OF APPLICATION:

Operating Expenditures

low |————|————| high

Personnel Requirements:

working with very high voltages demands strict compliance with safety rules by personnel

Grain Size of Feed:

minimum oF 150 ,um; extremely poor separation when higher proportions of < 40 ym are present due to dust adhesion on larger grains, adhesion on electrodes, etc.; maximum grain size 2 - 6 mm

Special Feed Requirements:

as mentioned above, the dust particles must be removed from the feed; additionally, a narrow-band classification is necessary, since electrostatic separation is characterized by a sharp, precise classification. This is attributable to the comparably high gravitational forces.

Replaces other Equipment:

is employed as an inexpensive sorting process in potash, diamond, and metal mining.

Regional Distribution:

worldwide, but has only seldom been applied as a beneficiation technique in small-scale mining

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high

Suitability for Local Production:

very good |————————| bad

Under What Conditions:

qualified manufacturers experienced in high-voltage technology, capable of working with various materials, might possibly be in a position to build electrostatic separators

Lifespan:

very long |————|————| very short

Bibliography, Source: Schubert, EP 0231441, DE 3035589 C2, DP 2134298, Singewald, Bock, DP 2614146, DP 2125286, DP 2213370, DP 3146295, DP 3216735, DP 2609048, DP 3233780, DP 3233528, DP 3603165, and 166, DP 3825434

OPERATING PRINCIPLE:

Electrostatic separation utilizes the differences in conductibility of the various feed components. The feed material, which has been pretreated or conditioned with surface-activating reagents, is placed in an electrical field which, depending upon the type of construction of the separator, has various effects on the mineral grains:

- in a roller separator, the material is fed onto a roller electrode and directed past a counter-electrode. The non-conductive material is not charged by the counter electrode, but rather only polarised, creating weak adhesive forces which draw this material to the roller electrode. Conducting material transmits its charge to the roller electrode, then becomes recharged and is repelled by the roller electrode and drawn to the counterelectrode. Separating blades divide the sorted material into a conducting and a non-conducting product.

- In a plate separator, the feed must be triboelectrically charged prior to separation. These electrostatically charged particles fall through the gap of a capacitor field between two electrode plates and are differentially deflected by the electric field, depending on the particle material.

- In a high-tension separator, the feed is charged by a corona electrode. Through the rotation of the roller out of the sphere of influence of the corona discharge, the moving conductor material immediately loses its charge; due to the centrifugal force of the roller and the gravitation, these particles are propelled away from the roller, while the nonconductors continue to adhere to the roller and fall off later.

Significant parameters for the separation in electrostatic separators are the inner and surface resistances, the electricity contents, etc. as well as the moisture and grain-size distribution. In order to separate non-conducting materials, the feed must be specially prepared, depending upon the characteristics of the non-conductors, through, for example, the following measures

- thermic pretreatment to dry or alter the surface characteristics of the mineral particles

- triboelectric charging, for example in vibrating screens, rotating drums, fluidized-bed apparatuses

- conditioning with surface-active tensides which affect the surface conductibility of the minerals and their hydration sheaths.

AREAS OF APPLICATION:

- for the separation of heavy-mineral pre-concentrates, for example zircon, monacite, rutile, columbite, tontalite, scheelite, cassiterite, etc.

- for the separation of quartz from hematite concentrates, gold pre-concentrates.

- sorting of phosphate raw materials

- production of pre-concentrates during winning of diamonds

- processing of potassium salts, for example with sylvanite, carnellite, kieserite, etc.


REMARKS:

Specifically for the electrostatic separation of raw potassium (potash) salts, many reagents have been tested and patented which allow a selective separation of potassium-salt mixtures, such as aromatic carboxylic acids such as O-cresotic acid, phthalic acid, cinnamic acid, atropic acid, vanillic acid, salicylic acid, benzoic acid, fatty acids with 6 to 15 C atoms (e.g. hydroxyphenyl butyric acid), etc., which are added in amounts of 50 - 200 g/t, for example supported by auxiliary conditioning agents such as HCI-gas, NH3, acetic acid, silicic acid, etc. These reagents are, for instance, vaporized onto the surface, whereby temperature variations play an important role. Small-scale mining operations can only be advised against employing tints highly sensitive, difficult-to-control technique. All of the other above-mentioned substances can be electrostatically sorted in small-scale operations.

The separation in the electrical field is greatly affected by moisture in both the air and the material. Films of moisture within the molecular density range can already negatively affect the surface conductibility of the feed. The relative air humidity for successful sorting ranges between approx. 2 and 25 %.

SUITABILITY FOR SMALL SCALE MINING:

Electrostatic separation for secondary cleaning of concentrates and winning of by-products in ore-mining operations is an economic technique which is also of interest for small-scale mining purposes. The electrostatic separation of salt to produce potassium (potash) salt concentrates is only suitable for small-scale mining if the mineralogical composition of the feed is not too complex. However, this is not the case for most of the deposits being mined by small-scale mines. Additionally, the unsuitability for local construction generally requires the use of imported equipment.


Fig.: Principle of electrostatic sorting. Source: Otero.

Table: Behavior of minerals in the high-voltage electrical field

Minerals attracted to the rotor

Minerals repelled by the rotor

baryte

cassiterite

beryl

chromite

calcite

galena

quartz

gold

diamond

magnetite

feldspar

graphite

monacite

haematite

scheelite

ilmenite

sillimanite

pyrite

zircon

rutile


wolframite

16.7 Flotation

Mining General (Gold, Ore, Coal,Industrial Minerals)
Beneficiation, Sorting

germ.:

Flotation

span.:

flotacion

Manufacturers:

Aker, Booth, Denver, Galigher Comp., KHD, Krupp, Machinoexport, Minemet Ind., Hoechst (reagents), Outokumpu, Sala, Wemco, Maxwell, INCOMEC, Volcan, Eg. Ind. Astecnia, IAA, COMESA, FAHENA, FINA, Famia, Fund Callao, MAGENSA, MAEPSA, Met. Mec. Soriano, PROPER, IMPROCON, MILAG

TECHNICAL DATA:

Dimensions:

flotation cells approx. 1 × 1 × 0.8 m up to 5 × 5 × 2.5 m and larger

Weight:

approx. 1 - 20 t

Extent of Mechanization:

fully mechanized

Power:

2.2 kW to 100 kW, approx. 1.5 - 5 kW/m³ volume of flotation cells

Form of Driving Energy:

electromechanical

Mode of Operation:

continuous

Operating Materials:


Type:

compressed air reagents bubbles < 2 mm in diameter

Quantity:

0.3 - 2 m³ /min m³ of slurry

ECONOMIC DATA:

Operating Costs:

high grinding costs

Related Costs:

dosing mechanism for reagents, grinding facility, classifying facility, settling pond for tailings

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Personnel Requirements:

for good separation results, precise control of slurry density, alimentary quantities and concentration of reagents is necessary

Grain Size of Feed:

50 · 200 ym

Recovery:

with preliminary flotation and subsequent cleaning of sulfidic ores, considerably higher than with gravimetric methods

Replaces other Equipment:

wet-mechanical sorting processes

Regional Distribution:

worldwide, flotation is the most widely used sorting process for mineral raw materials, partially also used in small~scale mining; approx. 2 billion tons of raw material is floated annually

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very bigh


high environmental impact through discharge of reagents with the tailings. The use of tailing ponds, neutralization basins, etc. and precise dosages of reagents are absolutely necessary.

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

flotation cells can be locally produced, e.g. from wood, iron, ferro-concrete or plastic materials; remaining components from imports

Lifespan:

very long |————|————| very short


when components subject to wear are made of elastomers

Bibliography, Source: Stewart, Priester, Taggert, Schubert, Gerth, Manufacturers information

OPERATING PRINCIPLE:

The flotation process utilizes the differences in surface wettability of various minerals, which can be artifically influenced, to achieve a separation. The completely-liberated feed material is suspended in a slurry containing approx. 30 % solids (by volume) and the valuable mineral selectively hydrophobed through the addition of collector reagents, which are mostly long-chained hydrocarbons of specifically regulated pH-values. This conditioned slurry then flows into the flotation cell' where it is brought into contact with injected, dispersed air bubbles; the electively-hydrophobed valuable-mineral particles adhere to the bubbles and travel upwards as a foam-mineral mixture (possibly stabilized through the addition of foam reagents or 'frothers') to the slurry surface where this "float" is then skimmed off. To suppress the unwanted hydrophobing of accompanying minerals and to enhance their removal with the "non-float", depressant reagents are added to the slurry. In the indirect flotation process, the valuable mineral is concentrated in the hydropilic non-float.

AREAS OF APPLICATION:

For the selective extraction of valuable minerals from raw ore feed:


- sulfide minerals
non-ferrous metal minerals (sometimes following sulfidizing)
precious metals

- fluorite, apatite, phosphorite, sulfur
- wolframite, scheelite, cassiterite, industrial minerals (sand and gravel)
- coal, graphite
- potassium (potash) salts
- quartz, keolin, feldspar, mica

SPECIAL AREAS OF APPLICATION:

To separate impurities and accompanying minerals from mineral-material mixtures

e.g.

reversed iron-ore flotation


reversed magnesite or calcite flotation


cleaning of glass sands

REMARKS:

For small-scale mining needs, flotation cells with external air supply can be recommended. This process requires more equipment and therefore higher investment costs, however permits regulation of the air supply to accommodate fluctuations in feed-quantity, feed contents, slurry density, etc. Self-aspirating cells allow a narrow range of variation only by changing the rpm of agitation.

Of importance for successful flotation is freshly-exposed surfaces. Especially sulfidic ores, which are easily subject to surface corrosion, require wet grinding prior to flotation.

Oil-flotation: W. Haynes/England/1860

Flotation with reagents for the separation of graphite, 1877 by Gebr. (brothers) Bessel/Germany

Foam-flotation: since the mid-twenties, important for very fine feed: agglomeration flotation (not economically significant)

REAGENTS:

Collectors
For sulfide minerals, anionic sulfhydryl collectors such as xanthate and dialkyldithiophosphate (for example, aerofloat, phosokresol) at concentrations of 10 - 200 g/t feed are applied,for non-sulfidic minerals: use of anionic oxhydryl or cationic collector, for example, long-chained, non-saturated (as much as possible) fatty acids or their soaps, which have previously been dissolved in hot oil, in concentrations of between 100 and 1000 g/t feed; by these quantities, the cost of reagents substantially affects operating costs. Silicates, halides and oxidic zinc ores are floated with organic amines as collector. To strengthen natural hydrophobia, for example in sulfur and coal or through the addition of an artificial hydrophobia, saturated hydrocarbons such as petroleum and oils are suitable.

Foaming agents/Frothers
Terpene and cresol or synthetic foaming agents added in quantities of around 5 - 50 g/t during sulfide flotation reduces the size of the bubbles and stabilizes the foam by lowering the surface tension.

Depressing agents/Depressants
Examples: zinc sulfate to depress zinc blende (sphalerite) in Pb-Zn-ores, cyanide to depress gold and silver, copper minerals, etc. by complexing.

Activators
Examples: addition of small quantities (1 - 10 g/t) of cyanide to clean mineral surfaces; sodium sulfide to convert oxide layers in sulfides; copper sulfate to activate zinc blende.

pH-reagents
to establish basic conditions: hydrated (slaked) lime, soda or caustic soda; to establish acidic conditions: sulfuric acids.

For small-scale mining, of special interest are individual components such as stator/impeller units from Aker which can be installed into existing, or possibly locally-manufactured, cells. In addition, these parts, being highly subject to wear, are normally made today of elastomers (for example polyurethane) which are extremely wear-resistant.

In order to assure the quality of the end products of flotation, precise control of the process is crucial. It is essential that the quantities of reagents added during flotation remain constant. Whereas this is performed today in large mechanized plants via dosing pumps, in small-scale mining, bucket-wheel proportioners have proven to be extremely effective. By altering the volume and/or number of buckets, or by modifiying the rpm of the bucket-wheel disk, they can be adjusted to cover a wide range of dosages. Furthermore, they are very sturdy, simple, accurate and suitable for local manufacture.

In addition to the process control, flotation also requires continuous monitoring of product quality. A simple periodic product sampling with the batea or gold pan assists many plants in quickly detecting possible deviations from the standard values. Small pan-shaped or inverted roof-shaped wooden troughs are used for this purpose.

Local products are sometimes used as reagents for the flotation, for example, natural oils, wastes from wood processing and from paper plants, etc. In this way the costs for imported reagents can be decreased substantially.

Tailings from flotation also provide a good aggregate or filler for lean mixed concrete backfill consisting of approx. 10 % cement, 60 % mine waste and 30 % flotation tailings.

EXPERIENCE FROM APPLICATION IN DEVELOPING COUNTRIES:

Representing the simplest forms of foam flotation, pipe flotation, in addition to flotation in sluices and settling basins (buddies see 14.10), is also being used.

The slurry, preconditioned with reagents, is allowed to fall into an open vertical standpipe, whereby air is drawn down along with it (after the principle of the water-jet vacuum pump). The aerated slurry is directed through the pipe into the flotation cell; perforations in the pipe allow the bubbles to escape and the flotation to take place. The float is subsequently scooped or skimmed off.

The quality of the flotation can be assessed simply by visual inspection of the bubbles on the slurry surface. A thick, fine-bubbled, and especially dark-colored foam indicate a correct reagent dosage and good mineral loading on the bubbles.

A foam with big bubbles and a transparent appearance removes only low quantities of "float" minerals and indicates an insufficient addition of reagents or an incorrect pH-value.

SUITABILITY FOR SMALL-SCALE MINING:

Flotation of sulfides is a suitable technique for small-scale mining, particularly if local manufacturers build the flotation cells and are dependent only on a few imported components. The selective sulfide flotation can also be considered appropriate for supplementing gravimetric beneficiation in small-scale processing operations.


Fig.: Designs of standard commercially-sold flotation cells. Source: Young.


Fig.: Types of impellers for standard, commercially-sold flotation cells. Source: Young.


Fig.: Operating principle of a flotation cell. Source: Otero.

CLOSE THIS BOOKTools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)
Technical Chapter 17: Drying
VIEW THE DOCUMENT17.1 Drying oven
VIEW THE DOCUMENT17.2 Solar houses
VIEW THE DOCUMENT17.3 Drying areas, drying surfaces

Tools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)

Technical Chapter 17: Drying

17.1 Drying oven

Mining General
Beneficiation, Drying

germ.:

Trockenofen

span.:

horno de secar, horno secador

TECHNICAL DATA:

Dimensions:

approx. 2 × 1 m hearth area, 10-cm-high rim for oven plate

Weight:

several 100 kg

Form of Driving Energy:

thermal from combustion of wood, peat, diesel, gasoline, oil, gas, coal

Alternative Forms:

mechanical heat generator (by METZLER)

Technical Efficiency:

very low

Operating Materials:


Type:

fuels

Quantity:

very high, approx. 0.05 - 0.1 t coal/t concentrate

ECONOMIC DATA:

Investment Costs:

approx. 200 DM when self made

Operating Costs:

high fuel costs

Related Costs:

fuel transportation costs, which could vastly increase for biogenic fuels due to lumbering requirements

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————————| high

Maintenance Expenditures:

low |————|————| high

Personnel Requirements:

minimal

Grain Size of Feed:

theoretically no restrictions; however, drying of fine grains is lengthy and expensive due to the large proportion of adhesive water which requires high energy input to separate it

Replaces other Equipment:

drying areas

Regional Distribution:

very rare, known from Bolivia, Thailand

Operating Experience:

very good |————————| bad

Environmental Impact:

low |————|————| very high


especially when temperatures exceed 1 05°C and sulfides begin to roast

Suitability for Local Production:

very good |————|————| bad

Lifespan:

very long |————|————| very short

Bibliography, Source: Priester, Gast, Inversin

OPERATING PRINCIPLE:

The drying surface of the oven - the oven plate - is formed like a pan for holding the feed, which is periodically stirred by means of shovels or scrapers. Gast describes an oil-fired oven for drying of wet concentrate: the cylindrical outer wall is perforated and the inner wall (cone shaped) serves as the oven's chimney. The material is fed by shovel and percolates through the oven automatically as the dried concentrate trickles out through the holes and piles up around the oven.

AREAS OF APPLICATION:

For drying of concentrates.

REMARKS:

It is absolutely necessary to ensure that the drying temperature of products containing sulfide minerals remains below 105° C; above this temperature the sulfides begin to roast, releasing sulfide-containing acids, sometimes at very high concentrations.

For preliminary dewatering, the concentrates need to be processed in a raffination barrel following the Schanz-method or in a tossing kieve.

SUITABILITY FOR SMALL-SCALE MINING:

Due to the negative environmental effects of drying in drying ovens, this process should only be employed when alternative methods cannot be used.

17.2 Solar houses

Mining General
Beneficiation, Drying

engl.:

solar tents, solar tunnel dryer

germ.:

Solarhauser, Solarzelte, solare Tunneltrockner

span.:

cases solares, carpas solares, tuner de secado solar

TECHNICAL DATA:

Dimensions:

size depends on drying requirements, specific drying duration and radiation energy

Weight:

e.g. solar tunnel dryer for drying harvested crops: 3 × 20 × 0.1 m

Extent of Mechanization:

not mechanized

Form of Driving Energy:

heat of radiation (solar thermal energy or insolation)

Alternative Forms:

in solar tunnel dryer with small fan: electric or photovoltaic

Mode of Operation:

semi-continuous

Throughput/Capacity:

up to approx. 100 kg/m² drying area

Technical Efficiency:

40° - 70° C drying temperature, drying duration is around half that of simple ground drying

ECONOMIC DATA:

Investment Costs:

dependent on construction material, minimum of approx. 500 DM; also dependent on intensity of solar radiation (insolation), less sun means more collector surface area is required.

Operating Costs:

when fan-operated, low energy costs

Related Costs:

possibly wind protection measures

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Personnel Requirements:

minimal

Location Requirements:

feasibility can only be calculated when solar radiation fluctuations are measured over the entire year

Grain Size of Feed:

all sizes

Special Feed Requirements:

no restrictions

Output:

the drying speed in solar houses and solar tents is notably higher than that of drying areas, especially when the material to be dried is spread out on tables, etc. (see Diderot). This is a result of air circulation through convection.

Replaces other Equipment:

drying areas, drying ovens

Environmental lmpact:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

depends upon the available possibilities using the following building materials: transparent corrugated sheets, glass, black plastic-foil, etc.; imported material (Nicolon) or nationally produced material, UV-stabilized transparent foil, insulation material, sealing material

Lifespan:

very long |————|————| very short

Bibliography, Source: Diderot, Landtechnik Wethenstephan, Bine

OPERATING PRINCIPLE:

Diderot describes southward-facing glass houses for solar drying of beneficiation products where the feed is spread out on tables. A similar effect can be achieved in foil tents made of black cloth foil, whereby the warming principle varies somewhat: with transparent materials, the enclosed space is warmed through the solar irradiation, and with opaque material the covering itself is heated by the solar energy.

Of simpler design, due to their compactness, are solar tunnel dryers. These consist of two flat, parallel tunnel channels, one of which serves as the air collector and the other as the concentrate dryer. Both channels are covered with a transparent foil. The collector is lined on the inside with a black absorbent-foil, black cloth, black stones, or similar heat-asbsorbing material. Towards the bottom, the dryer is thermally-insulated with, for example, plastic foam, rock wool, coconut fiber, straw or other dry organic materials. The walls of the channel are made of wood, brick or metal. The foil covering can be rolled up around a pipe to enable the dryer to be charged. A small fan is used for blowing air into the collector, where it warms up before entering a ventilation duct directing it into the tunnel dryer; the now warm, dry air passes over the thinly-spread layer of feed material and dries It out.

AREAS OF APPLICATION:

Drying of mining products especially in humid or semi-humid locations where open drying in direct sunlight is not possible. In locations at higher elevations, for example in Andean mining where the radiation intensity is particularly high, solar houses and solar tents offer an alternative to oven dryers.

Self-built air collectors are widely used in the agricultural industry for drying of herbs, hay, grains, peanuts, fuel materials, etc, One of the best foil-covering materials has proven to be Nicolon 66530 (from NICOLON B.V., Box 236, 7600 AE Almelo, the Netherlands). This material is a black PE-fabric with monofilament threads in the warp and stretched bands in the woof; It is 0,5 mm thick, 2.4 m or 5 m wide, weighs 182 g/m², has a tensile strength of 227 kg/5 cm in the warp and 104 kg/5 cm In the woof, and is characterized for its high resistance to radiation and long service-life (more than 5 years). Nicolon is air-permeable, thereby allowing air collectors to operate either with blower-fan drive or as gravity dryers. In gravity dryers, the collector unit must be positioned below the drying unit. In windy locations, collectors yield poor results. Air collectors can also possibly be used for ventilation purposes (exhaust of mine air).

SUITABILITY FOR SMALL-SCALE MINING:

This is suitable in locations where drying outside in the open air is not possible for climatic reasons. Simple, reasonably-priced and environmentally compatible constructions are possible.


Fig.: Solar tent made of syntetic fabric, from Landtechnik Weihenstephan (Germany).

17.3 Drying areas, drying surfaces

Mining General
Beneficiation, Drying

germ.:

Trockenflachen

span.:

superficies de secado

TECHNICAL DATA:

Dimensions:

up to 20 × 20 m

Form of Driving Energy:

solar radiation (insolation)

Throughput/Capacity:

several tons per day depending on grain size, climate etc.

ECONOMIC DATA:

Investment Costs:

approx. 10 to 20 DM/m² area

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Location Requirements:

also employable in humid climates, however high radiation intensity necessary

Regional Distribution:

Bolivla, Chile

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high


large space requirements

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

cement foundation

Lifespan:

very long |————|————| very short

Bibliography, Source: Priester, Diderot

OPERATING PRINCIPLE:

The dewatered ore or concentrate is thinly spread over the drying surface and allowed to dry in the sunlight. Wooden rakes are used for turning the feed material over, rubber scrapers for gathering and distributing the material and brooms to sweep together the dried material.

AREAS OF APPLICATION:

Drying of concentrate prior to selling, processing by magnetic separation, etc.

REMARKS:

The drying duration depends greatly on the grain size of the material to be dried. The finer the material, the more water is adhesively bound to the surface, and the longer it takes to dry. Drying time can total 8 hours or more.

SUITABILITY FOR SMALL SCALE MINING:

Drying on drying areas is the simplest method of drying products, and plays an important role particularly in arid and semi-arid climates.

CLOSE THIS BOOKTools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)
Technical Chapter 18: Clarification
VIEW THE DOCUMENT18.1 Thickener
VIEW THE DOCUMENT18.2 Lamella-thickener
VIEW THE DOCUMENT18.3 Continuous (rake) thickener

Tools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)

Technical Chapter 18: Clarification

18.1 Thickener

Mining General
Beneficiation, Clarifying

engl.:

gravity thickener, settling (sedimentation) basin

germ.:

Eindicker, Mehlgerinne, Schwerkrafteindicker, Absetzbecken

span.:

espesador, canaletas pare polvo, espesador por gravedad, estanque de sedimentacion

TECHNICAL DATA:

Dimensions:

up to 40 × 10 m surface area, continuous (Dorr-type) thickeners without rabble arm with approx. 55 inclined walls

Weight:

brick basin

Driving Capacity:

non-driven technique

Form of Driving Energy:

only gravitational influence

Alternative Forms:

mechanized rectangular thickener with scraper for collecting the sludge in the discharge (electric drive), mechanized continuous (Dorr-type) thickener (see technique )

Mode of Operation:

semi-continuous

Operating Materials:


Type:

possibly flocculants

ECONOMIC DATA:

Operating Costs:

only labor cost for removal of sludge

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high


only sludge removal

Personnel Requirements:

only for periodic sludge removal

Location Requirements:

level areas

Grain Size of Feed:

< 1 ,um up to 50 ,um, max. 5 - 10 % solids in the feed

Special Feed Requirements:

suspended slurry, where the density of the solids must clearly lie above 1. The clarifying characteristics of slurries are dependent on the specific surface area of the particles being clarified or sedimented. This increases inversely proportional to the square of the particle-size of separation; for the finest particle separation, flocculants are added to artificially increase the particle size.

Replaces other Equipment:

the construction and employment of thickeners is absolutely necessary to avoid contamination of the receiving stream and natural drainage basin.

Regional Distribution:

worldwide, in small-scale mining however very rare

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high


environmentally beneficial through clarification of tailings, but large space requirement of sludge ponds is destructive to the natural landscape.

Suitability for Local Production:

very good |————|————| bad


discontinuous rectangular thickener

Under What Conditions:

masonry work

Lifespan:

very long |————|————| very short

Bibliography, Source: Schubert

OPERATING PRINCIPLE:

The slurry to be clarified flows into the thickener, whereby the slurry velocity is reduced. Depending upon the residence time In the clarifying basin, the suspended particles settle out and collect on the bottom of the basin, while the clarified water discharges over the overflow. In semi-continuous thickening operations, a second thickener must be available so as to allow alternate clarifying and sludge-removal between the two basins.

AREAS OF APPLICATION:

For clarifying all types of slurries from beneficiation processes. Thickeners (German: Mehlgerinne or "dust sluice") were already used in the beneficiation of lead and silver ores during the 18th and 19th centuries in the Harz mining region in Germany.

SPECIAL AREAS OF APPLICATION:

In locations with strong winds, increased flow velocities, turbulence and short-circuit currents can impair the clarification.

REMARKS:

The space requirements for thickeners are very high.

The design of thickeners is quite simple. These types of thickeners can be locally constructed of simple brickwork for any beneficiation operation.

Sludge ponds are well-suited for clarifying larger quantities of fine-grained slurries; the distribution of the slurry over the larger surface area increases the residence time of the slurry in the basin, providing a chance for even fine grains to settle out. Where the quantity of sedimented fines is very large, the outer rim of the basin is extended in height to prevent the slurry from flowing over the top. The clay fractions in the settled fines act as a sealant on the bottom of the pond.

SUITABILITY FOR SMALL-SCALE MINING:

In small mines, thickeners are the most inexpensive method for the clarification of tailings that are rich In suspended solids, especially since the basins can be built of simple earth or brick-work.

18.2 Lamella-thickener

Mining General
Beneficiation, Clarifying

germ.:

Lamelleneindicker

span.:

espesador de lamelas Manufacturer: Sala

TECHNICAL DATA:

Dimensions:

inclination of lamella 45° - 55°; 15 - 500 m² projected lamellar area, as a combination lamella-continuous (Dorr-type) thickener up to 2500 m² surface area; volume between 3 and 150 m³

Weight:

1 - 30 t

Driving Energy:

applied only if rabble arm or vibrator is used

Form of Driving Energy:

electrical

Alternative Forms:

mechanical or pneumatic drive

Mode of Operation:

continuous

Technical Efficiency:

very good clarification and thickening

Operating Materials:


Type:

possibly flocculants

ECONOMIC DATA:

Related Costs:

sludge ponds or tailings piles for thickened sludge

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Grain Size of Feed:

for clarification of slurries with the finest of solids particles: 0 - 50 ym, maximum 5 - 10 % (by volume) solids in the slurry feed

Special Feed Requirements:

solids must have a significantly heavier specific density than water; the finest sludges are treated with flocculants to increase particle sizes.

Output:

the recovered slurry is separated into clarified water and thickened sludge

Replaces other Equipment:

continuous (Dorr-type) thickener, sedimentation basins

Regional Distribution:

distributed worldwide in large-scale mining

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

manufacturing workshops for large-scale equipment

Lifespan:

very long |————|————| very short

Bibliography, Source: Manufacturer information, DAX

OPERATING PRINCIPLE:

The lamella-thickener consists primarily of two components: the upper tank with 45° to 55 -inclined lamellae-plates, and the lower conical or cylindrical sludge-collecting tank.

The slurry feed entering the lamella-thickener separates into two flows due to the presence of vertical chambers at both sides of the lamella-plates and flows through inlet slots between the lamella-plates. Above each group of lamella-plates there is a continuous overflow-channel which is equipped with outlet openings to create a slight hydraulic counter-pressure against the incoming slurry. This method of feeding the slurry guarantees a homogeneous distribution of slurry into all interstitial spaces betweem lamella with a minimum of turbulence at the points of entry.

The slurry lands in the spaces between the lamella through intake-slots located on the sides in the lower region of the lamella-plates. The clarification occurs above the point of slurry intake to prevent mixing of the clarified fluid with the incoming slurry.

The thickening and consolidation of the sludge in the sludge collecting tank can be enhanced through the use of a vibrator or rabble (raking) unit.

AREAS OF APPLICATION:

For use In mining and beneficiation for clarifying and thickening slurries from classification and sorting processes, washing water and mine water. In addition, it is also employed in the metallurgy industry for purification of domestic water.

SPECIAL AREAS OF APPLICATION:

For clarification of solutions from gold leaching processes which contain coarser solids.

REMARKS:

Due to increasingly stricter environmental regulations, the use of thickeners is gaining in importance also for small-scale mining operations. Lamella-thickeners are suitable for small-scale mining only where available space is limited and the quantity of slurry produced is very large, for example in processing plants which are located in cities.

The very simple driveless design of a lamella-thickener enables it to be locally manufactured. The construction materials are:

Lamella-plates

Lamella tank and sludge-collecting tank

PVC

steel, rubberized as required

fiber-glass reinforced synthetic resin

rustproof, acid-resistant, etc.

other plastics


steel


SUITABILITY FOR SMALL-SCALE MINING:

Lamella-thickeners, as a driveless, continually-operating thickener, are particularly advantageous where space is limited. They can be locally manufactured, and their application for clarification of tailings contributes positively to environmental protection.


Fig.: Lamella-thinckener, 1. slurry intake, 2. slurry distribution chamber, 3. lamella-plates, 4. overflow channels, 5. overflow outlet, 6. sludge collecting tank, 7. underflow outlet. Source: Sala company information.

18.3 Continuous (rake) thickener

Mining General
Beneficiation, Clarifying

engl.:

dorr-type thickener, mechanized thickener

germ.:

Rundeindicker, Mechanisierte Eindicker

span.:

espesador redondo, espesador mecanizado

Manufacturers:

Sala, Dorr-Oliver, Denver, Famia, MAGENSA; MAEPSA, FAMESA, Eq. Ind. Astecnia, Buena Fortuna, COMESA, FAHENA, FIMA

TECHNICAL DATA:

Dimensions:

bottom angle cat 8°; outlet cone 45° - 50°; 0.07 - 0.14 m/s peripheral speed of rabble (raking) arm; approx. 10 - 1500 m² clarification surface area

Weight:

brick construction in the ground

Driving Energy:

electrically-driven rabble arm 0.5 (2.5 m 0) - 2.5 (20 m 0) kW

Alternative Forms:

possibly hydromechanical

Mode of Operation:

continuous

Technical Efficiency:

very good clarification and thickening

Operating Materials:

possibly flocculants

ECONOMIC DATA:

Operating Costs:

energy costs

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Grain Size of Feed:

0 - 50 ym

Special Feed Requirements:

max. 5 - 10 % solids content in the feed, density distribution of components must permit gravity separation, i.e. solids must have comparably high specific density

Replaces other Equipment:

settling basin

Regional Distribution:

worldwide application in residential water works for clarifying domestic as well as industrial sewage; also used in large-scale mining worldwide

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high


positive: minimizes sludge-loading (through fines in effluents) on the natural drainage system; negative: large space requirements

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

smaller units can be manufactured by local machinery and equipment manufacturers, the most complicated elements are the roller bearings and the worm gear for the rabble arm.

Lifespan:

very long |————|————| very short

Bibliography, Source: Ullmann

OPERATING PRINCIPLE:

Continuous (Dorr-type) thickeners are round settling basins for clarifying suspensions and thickening slurries. The most simple non-mechanized form is the 'Dortmund basin' with a funnel-shape cross-section, centralized suspension intake and discharge of the sludge either by means of pumping or a gooseneck hose from the deepest point. To increase the clarification area, larger thickeners of flat-cylindical cross-section and flat hopper bottom are in use in which the sedimented sludge is pushed toward the central discharge cone by means of a scraper on a rabble arm. The rabble arm rotates very slowly around the central thickening channel and serves to thicken the sludge in addition to stirring it. The driving force is extremely low. The clarified water flows over the periphery of the thickener and is collected in the overflow channel.

AREAS OF APPLICATION:

Clarification of mine water and beneficiation slurries containing solids particles smaller than 100 ym, as well as thickening of solids before further drying, for example in filter presses, etc., or prior to deposition in sludge ponds.

REMARKS:

The design of thickeners must take into consideration the slurry quantities and characteristics:

Form of drive:

small thickeners are usually driven by worm gears, larger ones are equipped with a peripheral drive

Rabble arm suspension:

smaller thickeners have rabble arms which are suspended directly at the middle axis, in larger thickeners the arm can be supported by a roller at the periphery of the basin.

Basin construction:

can be of steel-plate or concrete; for agressive slurries, wear resistant materials such as rubber coatings, stainless steel or possibly wood should be employed.

Discharge devices:

pipes in goose-neck form, diaphragm pumps or excentric screw pumps are favorable.

Feeding devices:

These should largely eliminate all kinetic energy of the incoming slurry, e.g. by use of deflecting or baffle plates, or tangential entry of the slurry into the cylinder.


In the event that the slurry feed contains solids that tend toward flotation, possibly due to residuals of flotation reagents from the beneficiation processing, those should be removed with stripping devices installed near the feed intake.

SUITABILITY FOR SMALL-SCALE MINING:

Mechanized continuous (Dorr-type) thickeners are appropriate for use in larger small-scale mines where the high space requirement is not problematic, where large flow volumes of slurry need clarifying and where the necessary energy Infrastructure is available. The complicated technology demands the importation of essential construction components.


Fig.: Continuous (Dorry-type) thinckener with central axis. 1) feed cylinder, 2) overflow channel, 3) sludge discharge outlet, 4) drive-unit bridge, 5) drive unit, 6) hoisting device, 7) rabble arms with scrapers, A slurry feed, K clarified fluid, S thinckened sludge. Source: Schubert.

CLOSE THIS BOOKTools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)
E. Mechanization and energy supply
VIEW THE DOCUMENTE.1. Introduction
VIEW THE DOCUMENTE.2. Energy source
VIEW THE DOCUMENTE.3. Drive unit
VIEW THE DOCUMENTE.4. Energy conversion
VIEW THE DOCUMENTE.5. Distribution of energy
VIEW THE DOCUMENTE.6. Energy systems
VIEW THE DOCUMENTE.7. Aspects of mechanization in mining
VIEW THE DOCUMENTE.8. Environmental and health aspects

Tools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)

E. Mechanization and energy supply

E.1. Introduction

Small-scale mining in developing countries operates at varying technical levels. The simplest level is the artisan or manual small-scale mining in which all tasks are performed by hand and no external energy is employed to ease the workload.

Examples are the gold diggers who win gold or mine tin with shovels, double-pointed picks, sluices and gold pans, in which drilling and blasting is performed by hand, transportation is performed with wheelbarrows and beneficiation with see-saw (rocker-type) crushers, hand jigs and settling basins.

In mining at an intermediary technical level, single work stages in the extraction, hauling and beneficiation processes are mechanized through the application of machines, whereby the control and regulation of the machines are usually performed manually. At this level, the proportion of work performed manually or with physical labor is still very high.

Examples are numerous small mining operations which drill using pneumatic drills on jacklegs, load the ore manually or with simple loading machines, sometimes employ crushers in the comminution process, and employ non-mechanized wet mechanical gravity beneficiation techniques. An additional example is sand-pumping operations in the mining of alluvial tin deposits.

In fully-mechanized mining at the progressive stage, most or all work phases are mechanized through the use, in part, of automated machinery.

Examples are the modern mining operations in industrial countries which are developed using tunnel boring machines.

The majority of the machines described in the previous sections find application in mining at the artisan and intermediary levels. If an external source of energy is necessary, a drive unit (e.g. engine or motor) must be added to the machine:

Energy Source

Drive- unit

Conversion

Energy distribution

Machine

diesel

internal comb. engine

compressor

compressed air line

pneumatic drill mill

water

water wheel

transmission gear

stamp mill


The machines and their intended applications determine the amount and form of energy required. In small-scale mining, the various operational steps should be considered separately.

For underground mining, machines are available for operation by three different basic drive-systems:

- electric
- pneumatic
- internal-combustion devices.

For reasons of mine safety, sturdiness, low maintenance, etc., compressed air tools and equipment have proven to be superior despite the low efficiency of the total system.

The energy requirement for mechanization of underground operations is determined by the size of the operation, surface facilities, geological conditions and particularly the degree of mechanization. There is practically no upper limit. The minimal energy demand is determined by the compressed-air consumption of drills on jacklegs, since drilling is usually the most energy-intensive activity in underground mining, and is accordingly the first area to be mechanized with the help of machines.

Depending upon the characteristics of the deposit, i.e. the hardness of the ore and host rock, drilling of blast holes requires approx. 0,5 kWh drilling work per drilled meter. Hence, mechanization of the drilling can lead to enormous increases in work productivity. A comparison of data from drifting activities in mechanized versus manual operations in solid-rock underground mining clearly demonstrates the differences:

purely manual:

0.02 to 0.243m³ loosened mass/MS

mechanized drilling, manual loading:

0.6 to 1.5 m³ Ioosened mass/MS

mechanized drilling and loading:

2.7 up to 4.6 m³ loosened mass/MS

Compressed-air demand for drilling lies at a minimum of approx. 2 m³/min at 7 bar air pressure and therefore approx. 10-15kW compressor power consumption.

In beneficiation, the comminution of the raw ore is the most energy-intensive processing step. Depending upon the geology of the deposit, the comminution of a ton of raw ore to a flotable fineness (100 % <100 µm) can require up to around 50kWh of crushing and grinding. The minimal power requirement for beneficiation is established by the consumption of a small crusher which lies between 3 - 5 kW.

Branches of mining which have to move bulk materials (for example, sand-pumping operations) need to orient their operations around their planned transport capacities; sulfur mines require, in part, high thermal energy for the operation of autoclaves for smelting.

The total energy requirement can be categorized into individual forms of energy, namely:

- mechanical
- electrical
- thermal

General opinion ascertains - especially from the viewpoint of industrialized countries with their extensive supply of electric power - that mechanization through electrical energy is particularly advantageous. Under closer scrutiny, however, it becomes evident that in the majority of cases, electrical energy is again transformed back into mechanical energy (with corresponding losses in efficiency). This is especially true in small-scale mining in developing countries.

Mechanical Drives for:

- Ventilators

- Jigs

- Pumps

- Vibrating screens

- compressors

- Tables etc.

- Crushers


In small-scale mining, electrical or thermal energy is only necessary in special cases.

Electrical energy for:

- charging lamps


- magnetic separation


- electrostatic beneficiation

Thermal energy for:

- drying


- distillation


- autoclaves

In order to meet the energy demand in terms of the energy form and amount, an energy supply system with the above-mentioned individual components is required. These are:

- energy source
- drive unit (engine or motor)
- energy conversion
- energy distribution

Relevant aspects for planning the energy system and its individual components are briefly systematized and outlined below.

E.2. Energy source

The essential criteria for planning the energy source are the costs and availability.

As energy sources for small-scale mining purposes, the following come into consideration:

- fossil fuels, especially diesel and gasoline
- electrical power originating from a central power supply
- water

The regenerative energy forms - wind, biomass and solar energy - cannot be used for the basic mechanization of mining, but are suitable in some cases for isolated tasks (such as solar charging stations for mining lamps).

When possible, the data collected should not only pertain to the present conditions, but should also, when possible, take into consideration any possible (foreseeable) future changes over the longterm. An important example which indicates the variability of absolute and relative costs for the energy source is the price data for diesel fuel in Bolivian tin mining relative to the price of the raw material produced (in this case tin):

The following table shows a comparison of the price development of tin and diesel in Bolivia:

1984

1 lb mined Sn ca. 6 US$


while 1 lifer diesel 0.03 US$


1987

1 lb mined Sn ca. 3 US$


while 1 lifer diesel 0.30 US$

While a miner could still buy 200 lifers of diesel/lb Sn sold in 1984, in 1987 he could only buy 10 lifers/lb Sn produced. Similarly, the price relation for electric energy from the central power supply (public utility network) reflects a parallel development.

The potential price-fluctuations and supply-shortages (poor infrastructure, strikes, market changes) associated with conventional energy sources suggest that the planning of an energy system which uses regenerative energy should be given priority. A prerequisite for this is the availability of a regenerative energy source on a daily and yearly basis, and comparatively favorable investment costs for the drive system (i.e. engine -possibly through local manufacture).

E.3. Drive unit

The drive systems for supplying energy are discussed in detail in Chapter 19. Decisive planning criteria are obtained by comparing the various systems with regard to the following parameters:

- costs, i.e. operating and investment costs
- repair and maintenance requirements
- adaptability
- suitability for local manufacture

A comparison of investment costs for drive-systems employed in mining is presented in the following table, whereby effort was given to consider machines which can be manufactured locally; these units are not only characterized by lower costs, but also by their comparatively simpler and quicker maintenance and repair requirements.

Table: Investment costs for drive units and energy. supply systems

Internal combustion engine

150 - 300 DM/kW (cif Bolivia)

Diesel generator

500 - 1000 DM/kW (fob)

Water wheels, hydromechanical (local production)

200 - 500 DM/kW (without hydro engineering measures)

Turbine, hydromechanical (local production)

100 - 200 DM/kW (local engineering measures)

Hydroelectric

3000 - 10.000 DM/kW (fob without hydro engineering measures)

Wind, mechanical (local production)

3000 - 5000 DM/kW

Wind, electrical

5000 - 15.000 DM/kW (fob)

Photovoltaic

15.000 - 20.000 DM/kW (fob)

At increasing efficiency or output, prices per installed kW react degressively; an exception is the linear trend in costs for solar electricity. The investment-cost ranges listed above pertain approximately to the maximum and minimum power requirements of small-scale mining.

Regarding investment costs, internal combustion engines are comparatively inexpensive, especially when compared to other drive units manufactured in industrialized countries; the high cost of fuels, however, leads to comparably high operating costs.

E.4. Energy conversion

A number of devices are available for converting one form of energy into another. The most important of these are presented in the Table. It is generally known that every conversion of energy is coupled with a loss in efficiency, which in some cases is very strongly dependent upon location; this is particularly true for conversion of electrical and pneumatic energy, whereby temperature and elevation are the primary influencing parameters.

In converting mechanical into pneumatic energy in two-staged compressors at 8-bar operating pressure, the following elevation-dependent efficiency losses are measured:

Copresor Type

Decrease in % for every 1000 m Elevation increase


Delivery Quantity

Power Consumption

Medium-size, air-cooled compressor

2.1

7.0

Screw compressor with oil injection

0.6

5.0

Larger, water-cooled piston compressor

1.5

6.2

Larger, water-cooled screw compressor

0.3

7.0

The conversion of mechanical into electrical energy in generators is calculated through the use of the following elevation and temperature dependent correction factors:

Elevation of the machine

1000 m

1500 m

2000 m

2500 m

3000 m

factor f1

1

0.96

0.91

0.87

0.83

ambient temperature °C

25

45

50

55

60

factor f2

1.07

0.96

0.93

0.91

0.88

Mechanical energy conversions for the purpose of altering transmission torque and rpm are listed in the following tables (including values for maximum limit and degree of efficiency).

Transmission type

For one transmission step

Capacity N1(PS) up to

RPM n1 (RPM) up to

Periheral speed v (m/sec) up to

Periheral force (wheel) U0(kg) up to

Torque of wheel M0(mkg) up to


Transmission

Total efficiency of efficiency %







usual up to

extreme up to







Spur gear


8

(20)

95...99

25000

100000

200

-

Planetary gear

8

(13)

98...99

10000

40000

-

-

-

Worm gear

60

(100)

97...45

1000

30000

70

50000

25000

Chain drive

6

(10)

97...98

5000

5000

17

28000

-

Flat-belt drive

5

(10)

96...98

2200

18000

90

5000

17500

V-belt drive

8

(15)

94...97

1500

-

26

-

2150

Friction wheel drive

6

(10)

95...98

200

-

20

-

-

E.5. Distribution of energy

Finally, the equipment for bringing the energy from the generator to the machine (drive unit) must be planned. These distribution systems are characterized by different distance ranges and efficiency-losses:

- mechanical drives are limited in range to a few meters but operate a high degrees of efficiency,

- electric drives require power lines and, depending upon the range, high-tension transformers to reduce resistance losses,

- pneumatic drives require expensive compressed-air lines which are characterized by high losses in air pressure (pressure drop) and in the delivered quantity (see Technical Outline 19.1 3).

E.6. Energy systems

In planning a complete energy-supply system for small-scale mining in developing countries, in addition to efficiency, the following parameters are also relevant:

economic factors:

investment costs,


operating costs,

technical factors:

overall efficiency,


worker safety,


environmental aspects


(see below)

A comparison of complete energy-supply systems is presented in the following tables. Generally, installations with a high degree of complexity present greater problems concerning operation, maintenance and repair. The conversion of mechanical into electrical energy and the reconversion for machinery drive-units is not only associated with high efficiency losses and high investment costs, but is also too complex for application in developing countries. Mechanical drives with direct use of torque, for example in internal combustion engines and small turbines, contribute greatly to simplifying mechanized equipment (see also Technical Outline 19.12).

E.7. Aspects of mechanization in mining

The most important aim of mechanization and partial mechanization is to increase efficiency. This goes hand in hand with a reduction in production personnel.

For coal mining at constant production rates, Noetstaller has quantified the number of personnel required as follows:

Finally, the costs accrued due to mechanization must be considered, i.e., the investment costs as well as the operating costs. Mechanization or partial mechanization exerts influence on the following factors, amongst others:

- the extent of investment costs not only for drive units but also for the machines and the associated related investments,

- the energy costs,

- cost of wages, since every mechanization step leads either to increased production or lower personnel requirements as a result of increased efficiency. (A consequence which poses problems in developing countries with their already high rate of unemployment.)



The extent of costs for each respective category listed above vary significantly between industrialized and developing countries. As a rule, the following is true of developing countries:

- investment costs for imported equipment are higher than in industrialized countries

- service costs on capital are higher than in industrialized countries,

- costs of wages are significantly lower than in industrialized countries.

The investment capital requirements for a coal mining operation are described by Noetstaller for the following ranges of mechanization:

A further major consequence of mechanization or partial mechanization is a change in the cost-structure of the operation; this is exemplified by ore beneficiation plants in Bolivia with varying degrees of mechanization:

A problem in the mechanization or semimechanization of plants or processes is the estimation of coupling (indirect) effects. Mechanization usually leads to increased efficiency in the mechanized processing step. However, in order to accommodate the newly-installed machine's operating mode (for example, a continuous mode of operation requiring continuous, homogeneous feed quantities), or the changed economic conditions (for example, higher production capacity), increases in efficiency/production must also be achieved in the preceding and succeeding processing steps. This may be difficult to realize, depending upon the characteristics of the deposit and on the operation's physical and personnel infrastructure. Increased production in th shaft-hoisting system, for instance, can only be attained through major investments or change of the haulage system. In the event that the steps preceding and succeeding a mechanization upgrade cannot be altered, the newly mechanized step cannot be operated economically at full production capacity. Inorder to achieve an improvement in production through mechanization, a prior calculation of the effect on the entire processing procedure is critical.


Fig.:Relative distribution of beneficiation costs in plants with varying degree of mechanization. Source: Priester.

A mechanization or partial mechanization of a plant can then be justified on an economic basis only when the production costs for the final product do not increase as a result of the investment. Aside from the economic aspects, the social, humanitarian, safety, environmental and regional-development aspects in conjuction with mechanization are also important. These are difficult to quantify and hence no concrete suggestions can be offered here in this regard (see Noetstaller).

In providing energy for direct use in mining operations, the welfare of the miners and their families should also be considered. The difficult living conditions in the mining regions located at elevations as high as 5000 m or more above sea level could be alleviated through the provision of warm water, energy for heating, lighting or electricity in general, or energy for cooking. Energy requirements in this area should not be negleted during planning.

E.8. Environmental and health aspects

For economic and especially ecological reasons, it cannot be regarded as reasonable to meet increasing primary-energy demands through the use of fossil fuels, either in the Andean region or worldwide. Unfortunately, ecological considerations in planning in developing countries remain an exception (for instance, mining in the watershed area of drinking-water reservoirs in Potosi, Bolivia). For the long-range and middle. range conservation of the ecological life-support systems, the protection of the atmosphere, water, soil and flora and fauna is imperative. Even small-scale mining in developing countries can and must contribute to protecting the future, without having to suffer economic disadvantages because of it.

In developing countries, the use of renewable energy sources could make a valuable contribution to environmental protection and increase the environmental awareness. This also applies to small-scale mining, where consideration of environmental aspects has so far been lacking.

The diesel-run generators used in conventional decentralized electrical-energy supply, as well as the internal combustion engines used in the operation of machines, burn fossil fuels and, in so doing, emit toxic residues in the form of exhaust fumes. The regenerative energy sources, to the contrary, use water, wind or sunshine as an energy-producing medium, but does so without consuming it and without creating residues. The operation of internal combusion engines not only produces environmental impact through exhaust fumes and noise, but also creates a serious problem concerning waste-oil contamination and disposal. In the remote regions of small-scale mining, environmentally-sound waste-oil disposal is either not possible, or due to inadequate environmental awareness is not available. Usually, waste-oil ends up directly in the soil or in the drainage system, which can have catastrophic effects on the unstable ecosystems of the high-altitude Andes region. Even the rural population in the larger vicinity can be adversely affected since flowing bodies of water (e.g. rivers) are often used for drinking water and for irrigation (possible solution is in Technical Outline 11.3).

CLOSE THIS BOOKTools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)
Technical Chapter 19: Energy Techniques
VIEW THE DOCUMENT(introduction...)
VIEW THE DOCUMENT19.1 Bicycle drive pedal drive
VIEW THE DOCUMENT19.2 Animal-powered whim
VIEW THE DOCUMENT19.3 Water balance
VIEW THE DOCUMENT19.4 Wind generator
VIEW THE DOCUMENT19.5 Savonius rotor
VIEW THE DOCUMENT19.6 Water wheel
VIEW THE DOCUMENT19.7 Horizontal water wheel
VIEW THE DOCUMENT19.8 Rope turbine
VIEW THE DOCUMENT19.9 Solar cells
VIEW THE DOCUMENT19.10 Solar collector (solar thermal)
VIEW THE DOCUMENT19.11 Water turbine
VIEW THE DOCUMENT19.12 Internal combustion engine

Tools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)

Technical Chapter 19: Energy Techniques

ENERGY SUPPLY TECHNIQUES

19.1 Bicycle drive pedal drive

Mining General
Energy, Energy Techniques

germ.:

Fahrradantriebe, Pedalantriebe

span.:

accionamiento a bicicleta, accionamiento a pedal

TECHNICAL DATA:

Dimensions:

starting at approx. 1.2 × 2 × 0.5 m

Weight:

25 kg

Form of Driving Energy:

pedal drive

Mode of Operation:

semi-continuous/intermittent

Throughput/Capacity:

continual output of 80 - 100 W, peak performance up to 500 W

ECONOMIC DATA:

Investment Costs:

for simple pedal lever approx. 20 DM; for bicycle drive starting at approx. 200 DM

Operating Costs:

mainly labor costs

Related Costs:

possibly gear unit

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Machines which can be Driven:



pedal drive:

bicycle drive:


percussion jig, manual diaphragm jig(see photo), Baader's blower (Harzer Wettersatz), air separators (pneumatic dry washer), tire pump, concussion (bumping) table

bumping table, Chinese liberation pump (see fig.) possibly haulage by block and pulley, small ball-mill, small sizing drum, pedal fan, vibrating screen

Replaces other Equipment:

manual and small mechanized drives

Regional Distribution:

based on current knowledge, so far not used in small-scale mining

Environmental Impact:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

metal manufacturing shop using bicycle parts

Lifespan:

very long |————|————| very short

Bibliography, Source: McCullogh

OPERATING PRINCIPLE:

The pedal-lever system transfers the power forces from the leg to the machine using the principle of leverage. In situations where machines have been hand-driven, the use of pedal drive frees the hands for other activities such as control, regulation, feeding, discharge, etc. The bicycle-drive uses the motion of the bicycle chain or rear wheel to drive the particular machine, possibly via a chain gear.

AREAS OF APPLICATION:

Pedal-levers are used for imparting simple pulsating power-impacts in the lower capacity range.

Bicycle drives are applied in all situations where continually rotating low-power movements are needed.

REMARKS:

In small-scale mines of artisan character which have so far been operated primarily manually, there are numerous areas of application where a simple pedal or bicycle drive can substantially ease the work load and increase ouput.

SUITABILITY FOR SMALL-SCALE MINING:

Pedal drive systems are practical for application in traditional small-scale mining in Latin America as low power drive mechanisms (< 100 W). They should, however, not be mistaken as a substitute for mechanization.


Fig.: Pedal drive for a centrifugal water pump. Centrifugal water pump. Source: McCaullagh.

19.2 Animal-powered whim

Mining General
Energy, Energy Techniques

engl.:

animal-driven gear germ.: Gopel

span.:

malacate

TECHNICAL DATA:

Dimensions:

required space: approx. 50 m²

Weight:

150 - 500 kg

Extent of Mechanization:

semi mechanized

Driving Capacity:

0.7 - 3 kW, average of approx. 800 W

Form of Driving Energy:

mechanical via animal power

Mode of Operation:

practically continuous

Throughput/Capacity:

depends on draft animal

Technical Efficiency:

70 - 90 %, for example for shaft haulage: haulage speed 0.3 - 0.65 m/s with haulage bucket volume of 0.3 - 1.2 m³ at a maximum depth of 250 m

Operating Materials:


Type:

draft animals and feed

Quantity:

1 - 2 draft animals (donkeys, oxen, horses)

ECONOMIC DATA:

Investment Costs:

750 to 5000 US$ depending on land of origin and machine

Operating Costs:

low

Related Costs:

for haulinging water, well construction

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————————| high

Maintenance Expenditures:

low |————|————| high

Personnel Requirements:

experience with harnessing and handling animals

Location Requirements:

draft animals and animal feed must be available

Machines which can be Driven:

Harzer Wettersatz (Baader's blower), bucket chain-conveyor, water-bag haulage system, ball mills, roller mills, Chilean (edge) mills, buddies, concussion (bumping) tables, piston pumps

Replaces other Equipment:

small engines, manual drive systems

Regional Distribution:

North Africa, Asia, Latin America, but no longer applied in mining

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

good metal-manufacturing shop; wooden construction also possible

Lifespan:

very long |————|————| very short

Bibliography, Source: Projekt-Consult, Agricola, Calvor, Villefosse, Delius, Lowe, Treptow, Wagenbreth

OPERATING PRINCIPLE:

Animals harnessed to the outer end of a horizontal lever arm continuously walk in a circle, rotating the arm around a central axis, thereby either directly or indirectly (via gear mechanism) driving a machine. Numerous design and construction variations.

AREAS OF APPLICATION:

Driving force for machines of low output for mining and beneficiation. Especially suitable for machines requiring high torque and low rpm.

REMARKS:

Animal-powered whims (gears) are particularly suitable for draining or hauling water. Animal-powered whims were applied historically in beneficiation and for ventilation.

The harnessing of animals for powering machinery was widely used in mining in central Europe during the late Middle Ages up to the 19th century; it was also historically found in agriculture, primarily for pumping purposes, an application which has been transferred to present-day small-scale mining. The output varies substantially depending on the kind of draft animal (e.g. horse 400 - 1000 W, mule 300 - 600 W, donkey 75 - 200 W, ox 300 - 500 W). The camel-type animals typical of the Andes (llamas, alpakas) do not accept being harnessed. In the high altitudes of the Andes, minimum values (output, efficiency, etc.) must be used for planning purposes. The very low rpm of the animal-powered whim prevents a conversion to other forms of energy and limits its application to mechanical uses. Since agriculture and mining activities frequently exist adjacent to one another, and agriculturally-employed draft animals are only needed periodically, use of these animals during idle periods for mining purposes appears practical.

The ability of draft animals to spontaneously produce up to ten times their normal long-term output permits the animal-powered whim, depending on the particular machine, to serve as a replacement for small motors whose output lies around 2-3 times that of the normal output of draft animals.

A special form of animal-powered whim is the Koepe-sheave whim (friction pulley), which was widely used in mining earlier,

SUITABILITY FOR SMALL-SCALE MINING:

Animal-powered whims are suitable for driving machines with low output, especially those with low rpm. The possibility for local production also provides an impetus for technical developments in other economic sectors (e.g. agriculture).


Fig.: Horse-powered whim for shaft haulage. Source: Agricola.


Fig.: Animal-powered whim for deep haulage. Source: Calvor.

19.3 Water balance

General Mining
Energy, Energy techniques

germ.:

Wasseraufzuge

span.:

elevadores de ague

TECHNICAL DATA:

Dimensions:

depends on transport distance

Extent of Mechanization:

not mechanized

Form of Driving Energy:

potential energy of water

Mode of Operation:

semi-continuous

Technical Efficiency:

very high efficiency when constructed with low-friction bearings

Operating Materials:


Type:

water

Quantity:

> weight of material to be conveyed + difference of rope weight

ECONOMIC DATA:

Investment Costs:

substantially cheaper compared to other haulage systems, since rope costs, etc. occur in the latter as well

Operating Costs:

very low

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high


Two persons for filling and emptying the water; these activities could also be partly automated.

Maintenance Expenditures:

low |————|————| high

Location Requirements:

large quantities of water at suitable topographical conditions (vertical elevation difference close to the haulage shaft or drainage gallery)

Equipment which can be Driven:

water and ore transport systems, ore and man-lifts in shafts

Replaces other Equipment:

mechanized haulage machines

Regional Distribution:

no longer in use today; formerly (19th century) distributed throughout Europe

Environmental Impact:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

metal and wood manufacturing shops using industrially-made ropes (cables); car parts can be used for brake systems

Lifespan:

very long |————|————| very short

Bibliography, Source: Various issues of "Zeitschrift fur das Berg- Hutten-, und Salinenwesen im preuss Staate" (Magazine for Mining, Metallurgy and Salt Industry in Prussian States, Germany)

OPERATING PRINCIPLE:

Water balances work according to the counter-weight principle. The bucket to be conveyed is lifted through the lowering of a heavier, water-filled counter-weight. Two conditions are necessary for operation:

- the counter weight has to generate a greater lifting power than the weight to be lifted

- the lifting force of the empty bucket has to be greater than the lifting force of the empty counter- weight (without water) in order to allow both the counter weight and bucket to return to the start position.

In cases where the counter-weJght is guided up a steep ramp, the lifting forces must be corrected by the cosine of the inclination angle. The less steep the ramp is, the higher the empty weight and the filling volume of the counter-weight have to be.

AREAS OF APPLICATION:

Hydromechanical hoisting of raw ore, mine water and possibly personnel transport.

REMARKS:

This method can most successfully be applied where drainage galleries allow the draining of process water, with the counterweight travelling up and down the shaft, without associated difficulties. Historically water balances were in use primarily in English and Upper Silesian coal mines.

The Installation of water balances demands specific conditions:

- mine infrastructure: haulage shafts must be located close to a suitable path for the counter-weight (ramp to the surface or shaft). The fact that drift mining is dominant in Latin America limits the possibilities for small-scale mining application in that region.

- large quantities of water and sufficient elevation potential must be available (topographical and hydrographical prerequisites).

Historically, hydro and pressurized-water motors were in use until the middle of this century.

SUITABILITY FOR SMALL-SCALE MINING:

The possibilities for application of water balances are very limited. Under ideal conditions (hydrographic, topographic and those related to mine-infrastructure) water balances guarantee a simple, stable, and driveless hoisting system.

19.4 Wind generator

Mining General
Energy, Energy Techniques

germ.:

Windgenerator

span.:

generador eolico

Manufacturers:

Elektro, Sudwind, Brummer, Enercon, Electromat and others

TECHNICAL DATA:

Dimensions:

10 m 0, height of tower 14 m with 20 kW generator; weight: 2500 kg

Extent of Mechanization:

fully mechanized

Form of Driving Energy:

wind (aeolian): for high-speed wind generators to produce electrical energy, minimum wind speed of 3.5 m/sec., nominal (rated) speed of 11 m/sec., for low-speed wind-mechanical wind mills, significantly lower wind speeds are sufficient

Mode of Operation:

continuous

Throughput/Capacity:

from 100 W to 50 kW depending on demand

Technical Efficiency:

up to a maximum of 35 % total efficiency as Cp (performance coefficient) × m (mechanical efficiency of the converter) × AM (efficiency of the machine)

Operating Materials:


Type:

wind

Quantity:

for generation of electrical energy, starting at speed of approx. 4 m/sec.

ECONOMIC DATA:

Investment Costs:

8000 to 20.000 DM/kW for facilities of 10 - 30 kW without tower

Operating Costs:

none

Related Costs:

tower, possibly storage batteries

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Location Requirements:

prerequisite for permanent operation is sufficient wind speeds both daily and annually. This must be confirmed by taking wind measurements for a period of several years at the location under consideration.

Machines which can be Driven:

electric motors and other machines with an electrical connection

Replaces other Equipment:

e.g. diesel generator, central electrical power supply, water turbines employing electricity

Regional Distribution:

common in industrialized countries (dependent on location), less frequent in developing countries

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Lifespan:

very long |————————| very short


rotors, gears and generators long-lasting, accumulators limited

Bibliography, Source: Manufacturer information, DVA, von Konig, GATE, STAMPA, Kleemann/Melip

OPERATING PRINCIPLE:

The high-speed wind generator orients itself according to the wind direction, whereby the rotor is set into rotation by the pressure of the wind (wing principle). The rotor axis is coupled, either directly or with a gear, to an asyncronous generator. The electrical energy so generated is drawn off either directly as counter-current electricity and consumed, or rectified for storage in accumulators.

With mechanical utilization of wind - most suitable with low-speed multiple-blade impeller - a connecting rod or drill rods transfer the mechanical energy to the machine (mainly pumps).

AREAS OF APPLICATION:

- decentralized generation of electrical energy as an isolated operation.

- for pumping mine and processing water in mining operations; possibly also for water drainage in shallow mines.

REMARKS:

The high specific investment costs for wind generators can only be Justified when the location exhibits optimal climatic conditions.

The longer the duration of calm periods to be accommodated, the higher the investment costs for the energy-storage unit (batteries with low discharge current). Such batteries are expensive and comparably short-lived, which significantly affects the operating costs and generated energy costs. Experiences from research activities of the DAV and the Frauenhofer Gesellschaft (Society) revealed that wind conditions of the alpine region are very non-constant and are in no way comparable to those of coastal regions, where experiences in using wind to generate energy have been actualized. Storm protection and regulation is still problematic in the alpine region. Unfortunately, it can be feared that this situation also applies to the high mountainous region of the Andes.

In the eastern Mediterranean region and in Persia, indications of early application of wind-energy converters can be traced back to the time of approx. 1000 B.C.

SUITABILITY FOR SMALL-SCALE MINING:

Extreme dependency on location and high investment costs for an imported product make this technology mostly inappropriate for small-scale mining. Furthermore' the storage of wind-generated energy, e.g. in the form of compressed air, is too expensive for the small-scale mining industry.

19.5 Savonius rotor

Mining General
Energy, Energy Techniques

engl.:

cross-flow rotor

germ.:

Savoniusrotor, Durchstromrotor

span.:

rotor savonius, motor de impulsion radial

TECHNICAL DATA:

Dimensions:

7 m × 2.5 m × 5 m (HWL, three-bladed rotor), rotor 0 160 cm

Form of Driving Energy:

aeolian (wind)

Throughput/Output:

up to 200 W

Operating Materials:


Type:

wind

Quantity:

min. 3 m/sec.

ECONOMIC DATA:

Investment Costs:

approx. 2000 DM for smaller units

Operating Costs:

none

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Location Requirements:

sufficient wind conditions (see Technical Outline 19.4 - wind generators), whereby it must be noted that Savonius and cross-flow rotors are more suitable for low wind speeds (around 3 m/sec.).

Machines which can be Driven:

pumps (e.g. small compressors for displacement pumps, tire pumps)

Replaces other Equipment:

fans, ventilators

Reglonal Distribution:

earlier, relatively widely distributed

Operating Experience:

very good |————|————| bad

Environmental Impact:

Iow |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

workshops working with fiberglass-reinforced synthetic resins, metal and wood

Lifespan:

very long |————————| very short

Bibliography, Source: Landtechnik Weinhenstephan (Germany), von Konig

OPERATING PRINCIPLE:

The Savonius rotor, as a machine operated by continual flow, functions similarly to the cross-flow turbines, with the exception that the driving flow-medium is air (wind). Low-pressure (suction) develops on the concave side of the impeller blades, and high-pressure conditions prevail on the convex side. The rotor begins to rotate around its central axis when wind forces are sufficient; this movement is used to power mechanical drive units.

AREAS OF APPLICATION:

Discontinuous drive for low-output machines (e.g. pumps), especially pumps for circulating or hoisting processing water in beneficiation.

SPECIAL AREAS OF APPLICATION:

For generating 12V direct-current electricity with battery storage for illumination or other low-consumption demands for electricity (e.g. recharging of electric mining lamps).

REMARKS:

Due to the unpredictability and nonreliability of wind, making it impossible to plan on, this wind-driven mechanical drive technology is only suitable for machines which can be left to operate periodically without supervision.

The storm protection of Savonius or cross-flow rotors is problematic, since the same surface area of the rotor is exposed to the wind regardless of wind direction, and cannot, as is the usual case, be turned away from too-strong winds. However, the qyrostatic force of the propeller at high rpms has a stabilizing effect. The tower for Savonius or cross-flow rotors can easily be locally constructed of wooden logs at low cost.

The major disadvantages of all wind aggregates are the significantly higher space requirement and the non-planable energy production resulting from the constantly fluctuating wind conditions which determine the output.

SUITABILITY FOR SMALL-SCALE MINING:

Small-scale mining operations in Latin America are seldom located where conditions are suitable for utilization of wind energy; this limits the possibilities for use even of Savonius or cross-flow rotors, which are able to operate at lower wind speeds and are ideal for mechanical-drive purposes.


Fig.: View and cross-section of a Savonius (left and above right) and a cross-flow rotor. Source: Landtechnik Weihenstephan (Germany).

19.6 Water wheel

General Mining
Energy, Energy Techniques

engl.:

water-powered gear

germ.:

Wasserrad, Wassergopel

span.:

rueda de ague, rueda hidraulica, malacate a ague

Manufacturer:

M. Impler, Filou

TECHNICAL DATA:

Dimensions:

water wheels from 80 cm up to more than 7 m in diameter are in use in small-scale mining. E.g. overshot water wheel: with approx. 27 lifer scoop-volume, diameter approx. 4 m, around 40 scoops approx. 70 cm wide, approx. 3 m long axle

Weight:

e.g. 1700 kg for overshot water wheel of 4-m diameter, 950 kg for 2.5 m diameter wheel, 700 - 800 kg for Zuppinger water wheel of 2.5 m diameter

Form of Driving Energy:

hydromechanical

Mode of Operation:

continuous

Throughput/Capacity:

up to approx. 10 kW

Technical Efficiency:

highest with overshot water wheels, approx.70 % middleshot water wheels approx.60 % lowest for undershot water wheels at approx.32 - 38 % Zuppinger water wheel approx.65 - 70 %

Operating Materials:


Type:

water

Quantity:

approx. 100 liters/sec or less for smaller wheels

ECONOMIC DATA:

Investment Costs:

in Germany: overshot water wheel with 4 m diameter: 25.000 DM; overshot water wheel with 2.5 m diameter: 15.000 DM; in developing countries with local production substantially lower costs in some cases, e.g. for overshot wooden water wheel 5 m in diameter made in Colombia 1300 DM

Operating Costs:

practically none

Related Costs:

hydrological engineering measures, flood protection

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Location Requirements:

demand For water and vertical elevation difference as follows: overshot wheels: approx. 1 m plus wheel diameter middleshot wheel: radius of wheel undershot wheel: no elevation-drop necessary at higher flow velocities

Equipment which can be Driven:

Harzer Wettersatz (Baader's blower), Chinese liberation pump, water-bag transport, winch, block and pulley, tire pump, ball mill, stamp mill, Chilean mill, vibrating screen, sizing drum, logwasher, jig, buddle, bumping table

Replaces other Equipment:

generators and all mechanical drive systems, various turbines, combustion engines

Regional Distribution:

historically worldwide, presently in small-scale mining in Colombia and Ecuador

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

wood manufacturer, metal manufacturing shop, shop working with fiberglass-reinforced plastics

Lifespan:

very long |————|————| very short


depends on flood protection

Bibliography, Source: Manufacturer information, Agricola, Delius, v. Koning, Bach, Beyrich, Hartmann, Henne, Mager, Meyer, Muller, Ovens, Redtenbacher, J. Reynolds, T.S. Reynolds, Shaw, Utta, Garrad, Fyfield-Shayler, Hutte, Wagenbreth.

OPERATING PRINCIPLE:

Overshot and middleshot water wheels (wheels with scoops): containers attached at the periphery of the water wheel fill with water from the feeding stream and rotate the wheel under the influence of leverage forces due to the added weight and impact of the water. The scoops empty automatically at the lowest point of revolution.

Undershot water wheels (paddle wheels): Radially-mounted paddles set the wheel into rotation due to the impact forces of the water flow striking the paddles.

AREAS OF APPLICATION:

To win energy for:

- production of electrical energy or
- mechanical drive for machinery by utilizing the torque

REMARKS:

Water wheels were already described by Philon in 230 B.C.

Water wheels represent the simplest utilization of the energy from flowing water. They are basically differentiated as undershot, middleshot and overshot water wheels with horizontal axis; water wheels with vertical axis (e.g. bucket wheel, Ghatta/Nepal); and boat mill or river mill (as special cases of undershot wheels, see Technical Outline 10.8).

Water wheels are generally not susceptible to sediment build-up or ice, but flood-protection measures should be taken regardless. An advantage of well-constructed wheels (with roller bearings) is the high degree of efficiency even with only partially-full buckets or scoops.

Further advantages of water wheels are:

- high moment of inertia, making it particularly suitable for direct drive of slowly-rotating machines and machines with fluctuating resistance (e.g. crushers)

- simple hydraulic design and construction

- suitable for small, highly fluctuating water quantities

- when well-constructed up to 80 % rate of efficiency

- low maintenance expenditures, easy to repair, long lifespan

- simple local production possible

- a storage of water and therefore energy is possible with the help of reservoirs

Disadvantages of water wheels are the heavy weight and large space requiement, as well as the losses with overshot wheels due to height and suspension.

The rotational speed should be as low as possible to avoid premature emptying of the scoops due to the greater centrifugal forces created at higher rotational speeds.

A high initial torque (around 10 rpm) is required. Unlike turbines, water wheels are gravity machines. They are more efficient than turbines (in the category of up to 10 kW) when well constructed. Due to the low rotational operating speed (15 · 20 rpm) the conversion into other forms of energy is quite difficult (electric) or impossible (pneumatic). For low-speed mechanical direct-drive systems (up to 300 rpm), "step-ups" in gearing (reduction in gear ratio) can be realised with force-locking or form-locking belt-drives.

A long-distance transmission of the energy generated by water wheels is not possible. Therefore producer and consumer are both directly bound to the location of the water energy-source. This can require expensive hydrological construction measures, without which the utilization of the hydromechanical energy may not be possible at all. The climatic and geographic conditions in the Andes, characterized by periodic high rainfall and sufficient topographical relief, provide numerous locations which offer an opportunity to utilize the energy of flowing water through water wheels and small turbines. The high demand for processing water in the hydromechanic beneficiation of ores in small-scale mining operations frequently justifies establishing a hydromechanical energy supply.

Types of water wheels: the 'Zuppinger' wheel is the most practical design for undershot water wheels.

Construction material: Wood and iron, fiberglass-reinforced synthetic
resins

Advantages of wooden water wheels:

+ can be disassembled

+ resistent to acidic water

+ no lime deposition

+ can be centered

+ simpler to construct, disassemble and repair


When used in conjuction with moor water, the wooden parts should be impregnated (with Roman salt) since moss disposition promotes rotting.

Water-wheels are seated in bearings of bronze or on bearing-blocks made of soapstone. In the situation where several overshot water wheels are installed on the same level in series, the feeding water is directed through a chute past all of the water wheels; the wheels are filled through opening of bottom gates in the chute.

Ordinary water wheels operate only in one rotational direction. For haulage purposes, reversible bull wheels (overshot) have been developed. They consist, as a unit, of two water wheels with opposite fill directions. By changing the incoming flow from one to the other intake chute, the wheel's rotational direction can be reversed. Bull wheels of up to 15 m or more in diameter were frequently installed underground just above the drainage level.

For shaft haulage with bull wheels, outputs ranging between 7.4 to 11 kW were achieved with haulage speeds of 0.65 to 1.4 m/see and bucket volumes of up to 1.2 m . This system functioned down to depths of 550 m maximum.

SUITABILITY FOR SMALL-SCALE MINING:

Water wheels are very suitable for application in small-scale mining due to the numerous possibilities to use them in direct mechanical drive of various mining and beneficiation machines. Despite the relatively high investment costs, water wheels are simple to manufacture locally using native construction materials; additionally, they are characterized by very low operating, maintenance and repair costs.


Fig.: Undershot water wheel in a mill. Source: Eckholdt.


Fig.: Water wheels for supplying energy in mining: A feeding chute, A' discharge chute (the supports are not shown), R1 bull wheel, S cable drums, SS cable pulleys, B brake mechanism (pulling on 1 releases the brake, pulling on 2 activates the brake). R2 wheel to operate "Frahrunst" or oscillating manlift ladder, SG connecting rods for manlift, KW angular rods for manlift (cast-iron), G shaft rods for manlift.

Source: Wagenbreth.


Fig.: (above): Curve of degree of efficiency of an overshot water wheel (1) compared to a Francis turbine (2) and a Kaplan turbine (3) by partial loading. Source: Konig.


Fig.: Limits of application of various water wheel. Source: Beyrich.

19.7 Horizontal water wheel

General Mining
Energy, Energy Techniques

engl.:

bucket wheel mill

germ.:

Loffelrad

span.:

rueda de cucharas

in Nepal:

ghatta

TECHNICAL DATA:

Dimensions:

diameter 0.7 - 2 m, height of wheel approx. 0.2 - 1 m, 7 - 10 inserted flat or curved wooden paddles (18 max.)

Weight:

from approx. 25 kg

Form of Driving Energy:

hydromechanic

Mode of Operation:

continuous

Throughput/Capacity:

up to approx. 1 kW, 50 - 100 rpm

Technical Efficiency:

approx. 10 - 30 %, in Nepal (with ghatta) 20 - 25 %; much higher (50 - 55 %) with high-quality bearings and paddles as well as sheet-metal guides at the inlet

Operating Materials:


Type:

water

Quantity:

40 - 80 I/sec

ECONOMIC DATA:

Investment Costs:

if locally produced starting at approx. 100 DM

Operating Costs:

very low

Related Costs:

hydro-engineering: weir, drainage channel, inlet chute

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Location Requirements:

Relatively large difference in elevation with relatively low flow quantities necessary, e.g. 20 I/sec and 10 m vertical drop yields 0.5 kW, minimum head approx. 2 m. Paddle wheels must always be erected above the highest water level.


Equipment which can be Driven: examples are gold centrifuge concentrators, possibly vibrating screens, vibrating chutes small Jigs, buddies, small vibrating and concussion tables

Replaces other Equipment:

small electrical motors or internal combustion engines for drive-systems with vertical axes

Regional Distribution:

still in use today, and being promoted, in Nepal for driving grain mills with up to 50 kg milling stones; in Chile on the island of Chil6e, in Bolivia in Dept. Cochabamba as a technique for processing harvested crops, otherwise in the Balkan

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

simple wood manufacturing. The paddle-wheel is technically the simplest and smallest hydromechanical drive-unit; improved wheels are made of iron.

Lifespan:

very long |————|————| very short

Bibliography, Source: Nepal, Hydronet, 1/88, 1/89, 2/89

OPERATING PRINCIPLE:

Paddle wheels are the predecessors of impulse (free-jet) turbines and have a vertical axis. The high-speed water flow strikes the flat or spoon-shaped paddles at an angle tangential to the wheel, which sets it into rotation.

AREAS OF APPLICATION:

Hydromechanical drive for machines with low power output and relatively low rpm.

REMARKS:

Formerly widely distributed in the Balkan, Austria and South Tyrol. As post-harvest technique still applied today in Nepal, Chile and Bolivia

An advantage is the vertical axis, which enables a direct coupling with, for example, milling stones, Chilean mills, etc.

A further advantage is that this low-maintenance drive unit can be placed directly underneath the machine to be driven.

A disadvantage is that rpm of a paddle-wheel drive cannot be controlled or influenced externally.

In Nepal the bearing between the water wheel and milling stone is made of bamboo, which has proven to be much cheaper, longer lasting and very simple to manufacture.

In Nepal, in the meantime, several paddle-wheel drives have been equipped with small counter-current generators for producing electricity for lighting purposes.

SUITABILITY FOR SMALL-SCALE MINING:

Horizontal water wheels are simple and economic power generating devices up to 1 kW, which could be employed to run mineral concentration equipment directly coupled to the turbine shaft.

19.8 Rope turbine

General Mining
Energy, Energy Techniques

germ.:

Seilturbine

span.:

turbine a cable

Manufacturer:

Campo Nuevo

TECHNICAL DATA:

Dimensions:

two pulleys approx. 1.5 m in diameter, approx. 10 m apart

Weight:

approx. 50 kg

Form of Driving Energy:

energy from flowing water with low elevation difference but high flow velocity

Mode of Operation:

continuous

Throughput/Output:

approx. 0.5 kW at very low rpm

Operating Materials:


Type:

water

ECONOMIC DATA:

Investment Costs:

local production: approx. 200 DM

Operating Costs:

low

Realted Costs:

none, possibly minimal hydrological construction measures

CONDITIONS OF APPLICATION:

Operating Expenditures:

Iow |————|————| high

Maintenance Expenditures:

low |————|————| high

Location Requirements:

locations with small elevation differences and small quantities of flowing water, but high flow velocities, are appropriate for rope turbines. The efficiency can be improved by building a channel (e.g. with corrigated sheet-metal or halved PVC-pipes) to control the water flow and to take up the rope of the turbine.

Equipment which can be Driven:

low-speed rotationing devices such as mech. buddies, Harzer Wettersatz (Baader's blower)

Replaces other Equipment:

geared-down electric-motor drive systems

Regional Distribution:

to date not distributed

Environmental Impact:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

simple wood manufacture for pulleys, synthetic rope, rubber parts from car hoses for buckets

Lifespan:

very long |————————| very short

Bibliography, Source: Manufacturer, Hentschel

OPERATING PRINCIPLE:

A rope is suspended longitudinally or diagonally along a flowing stream by means of two pulleys, with the lower rope strand hanging in the water. Flexible rubber buckets are attached to the rope with the open end facing upstream; the buckets fill with water which causes them to be pulled along with the flow due to the ensuing hydraulic pressure head. In the process, several buckets are always under water at any given time. At the lower, downstream pulley the buckets are raised out of the water and emptied. The upper rope strand travels above the water surface back toward the upstream pulley, maintaining a continuous revolving system.

AREAS OF APPLICATION:

To produce slow rotations at high rpm in areas with relatively low energy from flowing water.

REMARKS:

The extremely low rotational speed (< 100 rpm) generated with this rope-turbine is disadvantageous, limiting its application as a drive-unit to just a few machines, such as buddies. There is a need here for further research and development efforts.

SUITABILITY FOR SMALL-SCALE MINING:

Further development of the rope turbine is necessary before it can become suitable for small-scale mining purposes. Furthermore, it remains rather inappropriate for practical application as a drive system.

19.9 Solar cells

General Mining
Energy, Energy Techniques

engl.:

photovoltaic energy

germ.:

Solarzellen, Photovoltaik

span.:

celdas solares, fotovoltaica

TECHNICAL DATA:

Dimensions:

depending on capacity approx. 1 m²/100W

Weight:

2.5 kg/100 W

Form of Driving Energy:

solar

Mode of Operation:

semi-continuous analogous to intensity of daytime radiation

Throughput/Capacity:

unloaded: 0.55 V per cell; loaded up to 0.35 V, nominal voltage 0.45V

Technical Efficiency:

13 - 15 %

ECONOMIC DATA:

Investment Costs:

approx. 20 DM per Watt, tendency falling

Operating Costs:

none

Related Costs:

storage batteries, regulator

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Location Requirements:

sun, global radiation

Equipment which can be Driven:

none, area of application is, for example, charging station for electric lamps; lighting with energy-saving lamps, direct current vibrator

Replaces other Equipment:

smallest generators for electric power production

Regional Distribution:

worldwide, and increasing

Operating Experience:

very good |————|————| bad

Environmental Impact:

low very |————|————| high

Suitability for Local Production:

not possible

Lifespan:

very long |————|————| very short

Bibliography, Source: GTZ, Suntronic, Rau

OPERATING PRINCIPLE:

The solar cell photovoltaically transforms available light energy into electric current. Solar cells consist of mono or semicristalline or amorphous silicon that is doped with boron or posphorus N/P. Electrodes are placed onto the surface and back side. During insolation, free ions as charge-carriers are created which produce voltage in the solar cell by diffusion. Power and voltage can be increased by parallel or serial connection of several individual cells.

AREAS OF APPLICATION:

Solar cells are suitable for generating power in the low-voltage or low-power range, e.g. Iighting, charging of electric mining lamps, charging of booster batteries for lighting purposes.

REMARKS:

Due to technical simplification of the production process, the manufacturing costs of solar cells will be decreasing in the future.

Solar cells are still characterized by very high investment costs because of the technically complicated production process. They can, therefore, only be recommended for the lowest capacity range. Their use in small-scale mining in Latin America can be considered appropriate, since especially in the low-power range up to 200 W, a very definite demand exists for energy generation for:

- lighting, e.g. energy-saving lamps
- mining lamp recharging stations
- audiovisual communication media (TV, radio, etc.)
- The smallest vibrators for beneficiation purposes

The external temperature affects the electrical output of solar cells. As a general rule, the lower the temperature, the higher the capacity (0.3 % per C°). Altogether, solar cells operate in a temperature range from - 50° C to + 120° C (see table below). This fact, combined with the long duration of sunshine and the high quantity of global radiation of the sub-tropical region of the Andes (South Peru, Bolivia) provides ideal natural conditions for the use of solar cells.

Therefore, photovoltaic energy production in the lowest power range is, without question, an ecologically favorable alternative to other generators (internal combustion engines, small hydro-electric generators). In Bolivia, small mining operations have been observed using a gasoline-driven generator for several hours per day only for recharging mining lamps.

SUITABILITY FOR SMALL-SCALE MINING:

Only in the lowest capacity range (up to a maximum of 200 W) are solar cells competitive with other energy sources with regard to investment costs. The independence from operating materials and the very favorable natural climatic conditions support the use of solar cells in small-scale mining in Latin America for the purpose of charging battery-lamps for underground useage.

Table: Typical temperature coefficients for solar cells. Source: Suntronic Company information

Temperature-Range:


- 65°C to + 125°C


Maximum temperature:


+ 250°C for 30 minutes (briefly up to 300°C)



increases


below


VOLTAGE

2 mV°/C



25° C


decreases


above



increases


below


CURRENT


25 µA cm²/°C


25° C


decreases


above



increases


below


EFFICIENCY


0.3 %/°C


25°C


decreases


above


19.10 Solar collector (solar thermal)

General Mining
Energy, Energy Techniques

engl.:

low temperature collectors, flat collectors

germ.:

Sonnenkollektor (solarthermisch), Niedertemperaturkollektoren, Flachkollektoren

span.:

colector solar (termico solar), colectores de baja temperature, colectores pianos

TECHNICAL DATA:

Dimensions:

depends on size and radiation intensity

Driving Energy:

possibly circulating pump to transport the medium

Form of Driving Energy:

intensity of radiation, for circulation electric energy

Alternative Forms:

gravity collector, i.e. utilization of density differences of the various


warm media

Mode of Operation:

continuous

Technical Efficiency:

between 65 % and 85 % (maximum) and losses between 1.5 and 7.5 W/m²K

Operating Materials:


Type:

collector medium, e.g. water, oil

ECONOMIC DATA:

Investment Costs:

in Germany approx. 300 to 800 DM/m² depending on design

Operating Costs:

very minimal

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Location Requirements:

high radiation energy during daylight hours over the entire year is a prerequisite

Equipment which can be Driven:

can be used for heaters, pre-heating of process water, etc.

Replaces other Equipment:

helps to reduce fuel consumption, especially in poorly-vegetated arid zones

Regional Distribution:

in the meantime worldwide

Operating Experience:

very good |————|————| bad


Disregarding large fluctuations in the daily and yearly solar radiation values

Environmental Impact:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

simple workshop for handling metals and synthetic materials

Lifespan:

very long |————|————| very short

Bibliography, Source: Kleemann, Meliss; Patent E. Korber P.2713 810.9 and P 2804999.2

OPERATING PRINCIPLE:

Sun collectors transform incidental sunlight into heat. The flat collectors accomplish this by means of an absorber, a black metal or plastic plate that absorbs light and transforms it into feelable heat. Underneath the absorber are pipes through which a transport medium for the heat (e.g. water, oil, air) flows. This medium conveys the heat from the absorber to the user. In order to minimize heat loss to the surroundings, the collector is lined with a thermal insulation on the back side and is covered over the front with one or more transparent plates. This collector-unit is oriented toward the average direction of radiation in order to transform mostly vertical radiation into as much energy as possible.

FORMS OF APPLICATION:

Heating of process water in the beneficiation processes. Air collectors for drying.

SPECIAL FORMS OF APPLICATION:

Results of technology (warm water for washing, showers, heating, etc.).

REMARKS:

In addition to improving working conditions, the use of warm processing water produced substantially better results from wet mechanical beneficiation by improving the degree of separation achieved in the sorting processes. This effect can be attributed to the lower viscosity of warm water; the warmer the process water, the better the sorting conditions. Moreover, the warming up of processing water provides more confortable working conditions where direct contact is made with the processing water (e.g. manual activities where the hands are under water); examples are hand picking in sluices or hand jigging with screens.

Global radiation values vary significantly depending on the location, ranging between approx. 800 kWh/am² (Iceland) and more than 2200 kWh/am² (in sub-tropical desert regions, e.g. SW-USA/Mexico, highlands of Peru/Bolivia, the Sahara, Arabian Peninsula, the Kalahari and Namib as well as central Australia).

The simple flat collectors also can be equipped to serve as sun-wind generators, whereby the surface of the collector serves as an accumulation area for the wind and thus accelerates the air. This air then used to drive a cylindrically-shaped horizontal Savonius rotor (0.5 m diameter). Through the use of wind sails, this rotatable device can be turned so that the rotar is oriented toward the wind during periods of strong winds.

Materials for the collectors:

Cover:


Corrugated plastic sheets

light, but somewhat opaque

Acrylic tiles

(transmits less sunlight)

Glass

best cover material

Absorber:


Plastic (from 30 DM/m²)

poor heat conduction

Aluminium (approx. 120 DM/m²)

possible corrosion if combined with Cu parts

Steel (approx. 120 DM/m²)


Stainless steel (approx. 12O DM/m²)

very long lasting

Copper (approx. 200 DM/m²)

best heat conduction, very long lasting

Isolation:


Pu-foam


Polystyrene


SUITABILITY FOR SMALL-SCALE MINING:

Sun collectors are particularly suitable for pre-warming of processing water used in small-scale mining equipment in order to lower energy costs and Improve separation results.


Fig.: Operating principle of a flat collector. Source: Klemann.

19.11 Water turbine

General Mining
Energy, Energy techniques

engl.:

water turbine (mechanical and electrical application)

germ.:

Wasserturbinen (mech. und elektrische Nutzung)

span.:

turbine a ague (aprovechamiento mec. y electrico)

Manufacturers:

Campo Nuevo Ossberger, yolk, Voith

TECHNICAL DATA:

Dimensions:

depends on capacity, e.g. for cross-flow (impulse) turbine with 2.5 kW output: turbine wheel 200 mm in diameter, 82 mm in width

Weight:

25 kg for above-mentioned example

Form of Driving Energy:

hydromechanical

Mode of Operation:

continuous

Throughput/Capacity:

practical up to 30 kW

Technical Efficiency:

cross-flow turbine (75 - 82 %), Pelton turbine (75 - 86 %), Kaplan turbine (up to 90 %), Francis turbine (up to 90 %), total degree of efficiency with generator: 50 - 80 %, mechanical utilization (70 - 80 %)

Operating Materials:


Type:

water

Quantity:

depends on fall head of water and size of turbine


N [kW] = n [%] × Q [m³/sec] × h [m] × 9.81 [m/sec²]

ECONOMIC DATA:

Investment Costs:

local production in Bolivia: 200 US$/kW without penstock (pressure pipe)

Operating Costs:

very low

Related Costs:

gearing, hydrological engineering measures, flood protection

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————|————| high

Location Requirements:

requires topographical and hydrographical conditions such as minimum flow and minimum head (approx. 5 m) of water must exist

Equipment which can be Driven:

high-speed beneficiation equipment, e.g. crusher, sizing drum, vibrating screen, pumps, Chiliean or edge mill, jig, heat generator, bumping or concussion table, compressors; can additionally be used to generate electrical energy, e.g. with car generator

Replaces other Equipment:

all other drive units

Regional Distribution:

worldwide, but seldom used for direct drive

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high

Suitability for Local Production:

very good |————|————| bad

Under What Conditions:

qualified metal manufacturing shops: blades can partially be made from stainless steel pipe sections, are also made in developing countries: Bolivia, Colombia, Ecuador, etc.

Lifespan:

very long |————|————| very short

Bibliography, Source: Manufacturer information, T. Hentschel, Meier, Meyer, v. Konig, Elliott, Gate, Inversin, FAKT

OPERATING PRINCIPLE:

Unlike water wheels, which transform only the energy associated with the weight of the water, turbines utilize the flow-energy of water which, upon striking an obstruction (in this case the turbine blades), is partially converted into kinetic energy as pressure. Depending on the water head (height difference) and quantity, different types of turbines (cross-flow turbines, Pelton, Francis and Kaplan turbines) are employed. The operating range of the various types are shown in the figures.

The cross-flow turbine is a radial, partial-admission impulse (free-jet) turbine. It is classified as a slow-speed turbine on account of its low specific rotational speed (low rpm). The water jet stream is formed into a rectangular cross-section by means of a distributor. It flows through the blade ring of the cylindrically-shaped runner first from the outside inwards and then, after passing through the center of the runner, from the inside outwards. The run away speed (off-load) is 1.8 times the on-load speed; the degree of efficiency is good at part load of the turbine.

The Pelton turbine is a tangentially-admitted free jet impulse turbine in which the cup-shaped blades (buckets) are forged, screwed or cast onto a disk. The disk shaft can be set vertically or horizontally, the buckets are loaded tangentially through one or more (maximum of four) jet nozzles; a jet needle valve, operated by a governor, controls the Jet discharge by changing its cross-sectional area. The jet is split into two flows which are discharged from opposite sides to avoid any unbalanced thrust on the shaft. The rotational speed is less than that of Francis turbines. An increase in the diameter of the runner further reduces the rotational speed. Pelton turbines are well suited for smaller flow volumes at higher heads (falling heights). They are characterized by a very flat efficiency curve at partial load of the buckets. Already at 8 % (single-nozzled) and 4 % (double-nozzled) maximum capacity, a high degree of efficiency can be achieved (nearly 90 % at sufficiently high head). The run away (off-load) is approx. 2.0 times the on-load speed. Pelton turbines operate in atmospheric air pressure, requiring that they hang freely and are never submerged under water even when highest water levels are reached.

The Francis turbine is a radially-admitted reaction turbine in which a stay ring with adjustable guide vanes directs the water flow into the runner, which exits along this same axis. Francis turbines are well suited for larger flow quantities at small and intermediate heads, they are characterized by their high-speed operation and have a run away speed (off-load) of revolution 1.8 to 2.1 times the on-load speed.

The Kaplan turbine is constructed as a propeller with 2 - 7 wing-shaped, rotatable blades which are axially loaded with water directed through a stay ring with similarly adjustable gates. It is suitable for handling very large flow quantities at the smallest of water heads (falling height); it has a run away ratio (off-load: on-load) of 2.3 - 2.5 and has a relatively poor efficiency at partial loading.

Another important type of turbine which, depending on its design, can operate more as propeller or Francis turbine, is a pump employed as a turbine. Pumps are produced around the world in great numbers, operate at high efficiency, and can be manufactured at lower cost compared to turbines. By reversing flow direction, pumps can operate as turbines.

USE AND CONVERSION OF ENERGY:

The mechanical utilization of the energy from flowing water as driving power is both possible and practical for the majority of machinery used in small-scale mining. The ideal turbine type for this purpose has proven to be the cross-flow turbine. It is simple to produce locally and operates at a pressure range which allows the investment costs for the penstock (pressure pipe) to remain low. Small useable drops in elevation with large flow quantities lead to lower penstock costs, but generally higher costs for hydraulic engineering measures. High pressure heads (greater elevation drop) increase the penstock costs but require less hydraulic engineering construction work. An economical optimum lies in the pressure-head range which allows the use of locally-produced, reasonably-priced raw materials (for example, PVC up to about 50 m pressure head).

The rotational speed of cross-flow turbines lies in the range of 200 to 1000 rpm, and is thus well suited as a drive-unit for compressors. Modern axial-flow screw compressors operate at a rotational speed between approx. 1000 and 2800 rpm. These rotational values can be reached through the use of chain or V-belt drive systems.

The starting torque of electric drive-units is markedly less favorable than that of hydromechanical drive systems, as revealed during trial testing performed with small crushers common to small-scale mining.

The generation of low voltage electricity (12 V DC) is possible using common commercially-available automobile generators of up to around 500 W capacity. Booster batteries as truck batteries are also locally available. 12 V DC electricity can serve as the energy source for:

- energy-saving lamps
- television
- refrigerators
- vibrator motors
- charging stations for mining lamps, etc.

The generation of alternating-current voltage is similarly possible, however with the following disadvantages for use in small-scale mining in developing countries:

- high investment costs for the generation, transport and re-conversion of the electrical energy source,

- the low degree of efficiency, the larger installation and corresponding hydraulic potential requiret at the turbine location- the greater complexity of the installation, which in developing countries can cause significant maintenance and repair problems for the user,

- the difficulties with regulation - the regulation of frequency and efficiency poses relatively major technical problems. Hydraulic or electronic regulating systems consume the unused electrical power as heat resistance or regulate the inflowing water

- the overload-protection system, which protects the generator from rotating too fast. Reasonably-priced, converted motors serving as generators are capable of withstanding only up to approx. 1.2-times the rated speed without being damaged. Generators which safely operate up to twice the rated speed are very expensive,

- major difficulties with local manufacture and maintenance of this equipment.

Of advantage is the fact that electrical energy is easily transportable via power lines.

COMMENTS REGARDING LOCAL PRODUCTION:

Cross-flow turbines are the easiest to manufacture locally. The runner can be equipped with blades made of either curved sheet-metal or pipe sections sawed in half lengthwise.

Pelton turbines can either be cast (of bronze) in one piece using the wax smelting procedure, or constructed of individual blades (bronze or cast-iron) mounted to a disk with a central shaft. Single blades as models are available on the machinery-parts market, whereby the width of the blade should be approx. 3 times the maximum jet diameter. The greater the number of blades, the better the degree of efficiency. Of primary importance is an exact balancing of the runner.

AREAS OF APPLICATION:

For utilization of water flow energy (hydropower) for low-output requirements in the low-pressure range (5 - 50 m head).

- the direct operation of machines for mining and beneficiation
- the conversion of flow energy into other forms of energy:

* compressors for generating pneumatic energy for use in underground mining (compressed air)
* generators for producing electrical energy, for example through 12 V car generator
* heat generators for producing heat.


REMARKS:

Due to the fact that cross-flow turbines are recommended for use only in the low-pressure range, locally produced plastic pipes can be employed for the penstock, which offer the advantages of being inexpensive and less susceptible to frost. Care should be taken, however, that UV-resistant pipe material is employed to avoid having to cover the penstock. The hydraulic construction measures must include the incorporation of sedimentation chambers (sand traps), since suspended particles can lead to abrasion of the turbine runner.

For direct utilization of torque, the turbine is especially well suited for small-scale mining application in developing countries:

- high starting torque leads to drive-system efficiency (output) which lies as much as 50% below that of electric motors

- the altitude-independent efficiency of turbines compared to electric generators and internal combustion engines (small capacity, more fuel consumption at higher elevation) makes it preferable to use turbines with direct utilization of torque. Numerous small-scale mines in the Andes operate at elevations higher than 4000 m.

A curve of efficiency values for the various types of turbines is presented in the figure. Type BYS is a cross-flow turbine locally manufactured in Nepal of the simplest materials. The curve shows that even handcrafted turbines can achieve a high degree of efficiency (> 70 %).

SUITABILITY FOR SMALL-SCALE MINING:

Small cross flow turbines with direct utilization of torque by means of belt or chain drive systems represent ideal' versatile drive-units which have numerous possibilities for application within the geographical conditions and technical requirements which characterize small-scale mining in Latin America Low-cost local production can also generate technological effects outside the mining sector which provide a stimulus for regional development.

Other types of turbines require more complicated regulation and hydraulic engineering measures' making them more appropriate for medium-scale mining operations.


Fig.: Schematic diagram of a Francis turbine (from Meier) and detailed diagram of a runner (I.Z.E.)


Fig.: Design drawing of cross-flow turbine. Source: Ossberger company information.


Fig.: Pelton turbines: jet needle valve and defection of jet in a blade (above), deflector and jet needle valve for regulating flow (below). Source: Meier: runner from a Pelton turbine. Source: I.Z.E.


Fig.: Schematic diagram of double-nozze Pelton turbine. Source: Meier.


Fig.: Degree-of-efficiency curves for different turbine types. Source: Meier.


Fig.: Range of application for different types of turbines for small-scale hydropower needs. Source: Das Wassertriebwerk 10/82:

1 = A-pipe turbine,
2 = S-pipe turbine,
3 = compact regulated propeller turbine,
4 = special construction, pipe and Kaplan turbine,
5 = spur turbine,
6 = Reiffenstein reaction trubine,
7 = Francis compact spiral turbine,
8 = Francis spiral turbine (horizontal),
9 = special construction Francis spiral turbine,
10 = Mini jet turbine, 4 jets (vertical),
11 = small jet turbine with belt drive,
12 = jet turbine, 1 jet (horizontal),
13 = jet turbine, 2 jet (horizontal),
14 = jet turbine, 3 to 4 jet (vertical),
15 = special construction jet turbine,
16 = Ossberger cross-flow turbine.

19.12 Internal combustion engine

General Mining
Energy, Energy Techniques

germ.:

Verbrennungsmotor

span.:

motor a combustion, motor a gasoline

Manufacturer:

Briggs/Stratton, USA, Liste

TECHNICAL DATA:

Dimensions:

dependent on type and horsepower; internal combustion engines are characterized however by low specific weight (per horsepower) and performance values, e.g. for 20 kW gasoline engine 0.7 × 1 × 1 m

Weight:

starting at approx. 40 kg up to several 100 kg

Form of Driving Energy:

burning of biogenic fuels

Mode of Operation:

continous

Throughput/Capacity:

from 2 kW up to several 100 kW

Technical Efficiency:

25 %(gasoline), 38 %(diesel)

Operating Materials:

gasoline or diesel starting at approx. 21/h; lubricants in nominal quanties

ECONOMIC DATA:

Investment Costs:

for small 5 PS engine approx. 320 US$ (August, 1987)

Operating Costs:

approx. 1 US$/h

Related Costs:

cost of maintenance and repair approx. 50 US$/year

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high

Maintenance Expenditures:

low |————————| high

Equipment which can be Driven:

mainly beneficiation machines and compressors as well as generators

Replaces other Equipment:

e.g. water turbines

Regional Distribution:

worldwide

Operating Experience:

very good |————|————| bad

Environmental Impact:

Iow |————————| very high


used oil, exhaust gases, noise

Suitabllity for Local Production:

unsuitable

Lifespan:

very long |————|————| very short

OPERATING PRINCIPLE:

Engines with one or more cylinders and two or four-stroke cycles, V-belt transmission.

AREAS OF APPLICATION:

Primarily for driving smaller beneficiation machines, compressors and generators.

REMARKS:

Internal combustion engines cover the entire range of energy from 2 kW to more than 100 kW, whereby smaller units are appropriate as direct drive systems which utilize torque. Larger systems, to the contrary, are coupled with generators for producing electric power. Internal combustion engines operate at rotational speeds Iying between 1000 rpm (large diesel engines) and 3000 rpm (small diesel and gasoline engines). The regulation of rpm is very simple, and consequently the conversion into other forms of energy can be accomplished without difficulties; this is significant to small-scale-mining especially for pneumatic drive-systems underground.

Internal combustion engines are generally very independent of location. Problem areas are the supplying of the necessary fuels and the losses in efficiency at higher altitudes; as a general rule, every 100 m increase in altitude results In the following efficiency losses:

for simple internal combustion engines

1.3%

for turbo-charged engines

0.9%

Internal combustion engines are characterized by low investment costs but very high operating costs. In addition, a number of other factors exist which characterize the use of internal combustion engines as an energy source In developing countries as unfavorable:

- difficulty in acquiring spare parts and maintaining imported products. In addition to the direct costs of repair, substantial financial losses can occur from operational disruptions caused by lengthy delivery times for spare parts.

- the poor infrastructure characterizing the majority of small-scale mining regions makes it difficult to maintain a continuous supply of fuel. Especially in the rainy season, remote mining areas are often inaccessible due to damaged roads. Further difficulties can arise due to bottle necks in the supply (e.g. strikes) from the mostly state-owned oil companies.

- high national transport costs as a result of the poor Infrastructure, on the one hand, and drastic increases in energy prices on the other. The fuel costs in Bolivia, for example, in the gold area of Tipuani, approx. 200 km from La Paz, are twice as high as in La Paz.

- the high-altitude topographical loation of many of the mine operations, such as in the Andes of Latin America, is disadvantageous for two reasons for one, the large losses in rated capacity of machines operated at high altitude (up to 50% at 5000 m above sea level) requires large-scale equipment at corresponding high investment costs, secondly' the low degree of efficiency leads to increased fuel consumption and therefore higher operating costs.

- ecological aspects.

SUITABILITY FOR SMALL-SCALE MINING:

Internal combustion engines are suitable for small-scale mining in situations where renewable energy sources are not available. Low Investment costs but relatively high operation costs and a limited lifespan characterize these engines, as well as their technically versatile application.

19.13 Compressed-air supply

General Mining
Energy, Energy Techniques

engl.:

compressor (compressed air tank, compressed-air lines, water separator, lubricator, etc.)

germ.:

Druckluftversorgung (Kompressoren, Drucklumank, Druckluftleitungen, Oler etc.)

span.:

abastecimiento de aire comprimido, compresores, tanque de aire comprimido, tuberia pare aire comprimido, lubricadores etc.

Manufacturers:

Mannesmann Demaq Atlas Copco, Kaeser, Frantz, Ingersoll-Rand

TECHNICAL DATA:



Dimensions:

compressors: ranging from 1 × 1 × 1 m to 2 × 3 × 4 m

pipeline:

50 - 600 mm diameter for pipes, 3/4" or more for hoses

Weight:

e.g. for stationary watercooled axial-flow compressor with 45 kW and 7.2 m³/min (8 bar): 860 kg e.g. for watercooIed piston compressor with 40 kW and 8 m³/min (7 bar): 1650 kg

Material:

pipes: steel, PVC; PE-hoses: rubber, fabric

Driving Capacity:

5 - 6.5 kW per m³ per min

Form of Driving Energy:

mechanical by electric motor, diesel engine

Other Opportunities:

hydromechanical

Mode of Operation:

continuous

Throughput/Capacity:

6 - 10 m/see air speed

Technical Efficiency:

10 - 15 % for total system

Operating Materials:


Type:

oil

cooling water

Quantity:

for axial-flow compressor

approx. 0,5 I/min × kW


for piston compressor


ECONOMIC DATA:

Investment Costs:

new equipment: up to 50.000 DM

Operating Costs:

high due to pressure losses from leakages

Related Costs:

compressed-air dryer, compressed-air lubricator, compressor compressed-air tank, flexible suspension system

CONDITIONS OF APPLICATION:

Operating Expenditures:

low |————|————| high


compressed-air lines

Maintenance Expenditure:

low |————|————| high


compressed-air lines

Personnel Requirements:

training for operation and maintenance is necessary

Location Requirements:

depends on drive-system (possibly hydromechanical) and cooling system (possibly water cooled). Important is the reduction of compressed-air losses due to leakage. In German coal mining these account for 35 % of the total compressed-air volume. These losses can be minimized especially by reducing the number of fittings and employing high-quality material. Besides the volumetric losses, pressure losses (pressure drop) also occur due to friction in the pipeline; the extent depends on pipe diameter, pipe surface conditions and particularly flow geometry.

Machines which can be Driven:

pneumatic drills, slopers (mining hammers), impact drills, pneumatic leg supports, chain saws, lamps, delivery and high-pressure pumps, fans, compressors, winches, drill-steel grinders, ratchet winches, lubrication guns, explosives pumps, loading equipment.

Regional Distribution:

worldwide in mining

Operating Experience:

very good |————|————| bad

Environmental Impact:

low |————|————| very high


depending on drive system, through exhaust fumes, used oil or oil from compressed air

Suitability for Local Production:

not suitable

Lifespan:

very long |————|————| very short


depends upon maintenance

Bibliography, Source: Roschlau, Atlas Copco manual, Fritzeche

OPERATING PRINCIPLE:

Piston, axial-flow and turbo compressors can be used to generate compressed air. Piston compressors compress the drawnin air by reducing the volume in the compression chamber through the stroke of the piston. They operate at 1000 rpm; the operating pressure can be regulated. Axial-flow screw compressors are displacement compressors in which static pressure is created through the rotation of the threaded axis which draws in air, compresses it, and rereleases it. They operate at rpms ranging from 1500 to 2500. Turbo compressors are used to generate large volumes of oli-free compressed air, under conditions of varying air requirements, through acceleration of the drawn-in air and subsequent conversion of the kinetic energy into static pressure.

In present-day mining, both stationary and transportable axial-flow compressors are commonly in use.

Compressed air tanks have three main functions, namely:

1. compressed air storage
2. improving cooling and condensation precipitation
3. equalizing pressure fluctuations in the system caused by tool operation

Compressed air tanks for mining purposes should have a volume equal to about one-tenth the rated output of the compressor (m³n/min). This applies when the compressor can be periodically disconnected (to protect the compressor) from a continuously running drive aggregate. Where the frequent starting of a directly-coupled drive unit must be avoided, a larger tank volume is required. The frequency of start-up operations should not exceed 10 per hour. The difference in pressure during regulation is approximately 1 bar.

The consumption of compressed air at 7 bar equals about:

2,5 - 5 m³ per drilling hammer
7 - 10 m³/min per overhead shovel loader
3 - 5 m³/min per hoist (winch)

The advantages of compressed air as an energy source are evident, according to Roschlau, in the pneumatic equipment itself:

- simple and sturdy construction,
- relatively small mass (low specific weight),
- employable in all operational activities,
- Infinitely variable setting, adjusting and regulating,
- extremely reliable in operation and function, therefore minimal down-time,
- automatic overload protection
- easy to handle maintain and repair,
- no safety problems (exhaust fumes, heating, etc.)
- escaping compressed air improves the climate at the work place (oxygen supply, cooling).

However, these advantages have serious consequences. Among these are following disadvantages:

- the total degree of efficiency of pneumatic equipment, at only around 15 to 20%, is significantly lower than that of other forms of energy,

- compressed air is the most expensive industrial energy source,

- high noise levels during operation of compressed air equipment

- enerqy conveyance requires the installation of an expensive pipeline network, involving substantial costs for maintenance and repair.

Compressed-air Line:

Compressed air pipes/hoses conduct the compressed air to the face where it is needed for driving the equipment. Hence the air line is installed as a large-diameter rigid pipe to a point just short of the working face, where hoses then complete the connections to the pneumatic equipment. The joints between pipeline sections, hoses, to lubricators and to pneumatic equipment are connected with clutch (claw) couplings.

Following the compressed-air tank, and possibly before the pneumatic equipment, a water separator should be installed into the compressed-air network. This device removes the moisture in the air either by having the air flow repeatedly through a screen mesh, or repeatedly deflecting the air so that it strikes the separator walls; both methods result in the moisture condensing and precipitating out. The collected condensate is withdrawn from the collecting container either automatically or by hand. This reduces the risk of occurrence of water-hammer or icing in the equipment.

made of PVC/PE:
For example: 0 50 mm, light, easy to install even around corners; couplings (connections) are difficult to obtain, modern glueable couplings of synthetic material are better and much cheaper - suitable for PE-pipes, also either welding or clamp-couplings with rated pressures up to 16 bar air-tight. 0 up to 1 10 mm: brass couplings, expensive and heavy, otherwise inexpensive, relatively long life-span, very low frictional resistance! Not easy to handle, since delivered in huge rolls.

made of steel
Purely rubber couplings are less expensive than PVC, standardized pipe-section lengths, corrodes easily from contact with condensed water, therefore filtering of the compressed air prior to its use is practical.

In surface facilities, exposed PE/PVC pipes must be covered with earth, straw, etc. in order to prevent adverse effects from UV radiation which lead to accelerated ageing of the plastic material.

Prior to the input of compressed air into the pneumatic equipment, the air must be mixed with oil to lubricate the operating motors. This is achieved through the use of compressed-air lubricators (oilers) which add oil in measured dosages.

REMARKS:

Compressed-air Lines

The pressure available to the consumer is also significantly influenced by the air conveyance system. Couplings and valves as well as smaller-diameter lines greatly reduce the pressure. Consequently, a comparatively larger diameter should always be used. The pressure drop is inversely proportional to the diameter of the line, raised to the fifth power. Even a small increase in diameter from 3/4" to 1" in a 10-m-long line can already reduce the pressure-drop loss to less than half. In general, about 10 - 15 % of the compression work is lost through friction.

The removal of water from the compressed-air line is essential. Condensed moisture collects in the low points of the pipeline and causes not only pressure drop, corrosion, and icing, but also water hammers (water shock) in the operating equipment. In addition to the use of water separators, the compressed air should be pre-cooled on the surface. The climatic conditions at the location play a major role; high temperature and high relative humidity lead to high water condensation in the pipeline.

In the event that the pressure of compressed air drops down under the operating pressure of the machine, an over-proportional decrease in the machine's efficiency results.

The overall efficiency of the compressed-air system is considerably affected by pressure losses through leakages. Such losses have averaged up to 35 % in coal mine in the German Ruhr area!! These losses mostly occur at the joints between pipe sections, which is another point favoring PVC-pipes.

SUITABILITY FOR SMALL-SCALE MINING:

The generation and supply of compressed air is the most important energy-technology installation for mechanized small-scale mining underground. In view of the high investment and fuel costs, the dimensioning of the facility becomes critical in determing the economical success of the operation.


Fig.: Pressure drop per 100 m of line at an average compressed-air pressure of 6.5 bar (5.5 above atmpspheric pressure) and an average temperature of 20°C, relative to compressed-air flow velocity and inner pipe diameter. Source: Hoffmann.


Figures
Fig.: Water separator. Source: Hoffmann
Fig.: Self-regulating (automatic) water separator for main compressed-air pipe. Source: Hoffmann.


Figures
Fig.: Draining of compressed air pipelines. Source: Hoffmann
Fig.: Water separator made from pipe and structural sections. Source: Hoffmann.

CLOSE THIS BOOKTools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)
VIEW THE DOCUMENT(introduction...)
VIEW THE DOCUMENTAcknowledgements
VIEW THE DOCUMENTPreface
VIEW THE DOCUMENTGuide to the user
VIEW THE DOCUMENTIntroduction
A. Analysis
Technical Chapter 1: Analysis
B. Underground mining
Technical Chapter 2: Safety Techniques
Technical Chapter 3: Ventilation
Technical Chapter 4: Water supply and drainage
Technical Chapter 5: Support
Technical Chapter 6: Lighting
Technical Chapter 7: Stoping
Technical Chapter 8: Loading
Technical Chapter 9: Hauling
C. Surface mining
Technical Chapter 10: Surface Mining Equipment
Technical Chapter 11: Other special techniques
D. Beneficiation
Technical Chapter 12: Crushing
Technical Chapter 13: Classification
Technical Chapter 14: Sorting
Technical Chapter 15: Gold Benefication
Technical Chapter 16: 0ther Sorting and Separating Techniques
Technical Chapter 17: Drying
Technical Chapter 18: Clarification
E. Mechanization and energy supply
Technical Chapter 19: Energy Techniques
VIEW THE DOCUMENTBibliography
VIEW THE DOCUMENTList of manufacturers and suppliers
VIEW THE DOCUMENTList of abbreviations

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CLOSE THIS BOOKTools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)
VIEW THE DOCUMENT(introduction...)
VIEW THE DOCUMENTAcknowledgements
VIEW THE DOCUMENTPreface
VIEW THE DOCUMENTGuide to the user
VIEW THE DOCUMENTIntroduction
A. Analysis
Technical Chapter 1: Analysis
B. Underground mining
Technical Chapter 2: Safety Techniques
Technical Chapter 3: Ventilation
Technical Chapter 4: Water supply and drainage
Technical Chapter 5: Support
Technical Chapter 6: Lighting
Technical Chapter 7: Stoping
Technical Chapter 8: Loading
Technical Chapter 9: Hauling
C. Surface mining
Technical Chapter 10: Surface Mining Equipment
Technical Chapter 11: Other special techniques
D. Beneficiation
Technical Chapter 12: Crushing
Technical Chapter 13: Classification
Technical Chapter 14: Sorting
Technical Chapter 15: Gold Benefication
Technical Chapter 16: 0ther Sorting and Separating Techniques
Technical Chapter 17: Drying
Technical Chapter 18: Clarification
E. Mechanization and energy supply
Technical Chapter 19: Energy Techniques
VIEW THE DOCUMENTBibliography
VIEW THE DOCUMENTList of manufacturers and suppliers
VIEW THE DOCUMENTList of abbreviations

List of manufacturers and suppliers

Aceros del Sur S.A. ADESUR
Jacinto ibanez 131, Parque Industrial M-2, Arequipa Peru
(51 ·54) 23 28 55,23 26 40,23 47 05, Fax (51-54) 23 28 55,
Telex 51214 PE ADESUR

AEG
Goldsteinstra�e 238,6000 Frankfurt am Main 71, Germany,
(069) 6699-0, Fax (069) 66 99 205, Telex 413 382

Aker-Minpro
Sandgt 33, Trondheim, Norway
(07) 51 35 22, Telex 55 083 Minpr n

AKW
Posttach 11 69,8452 Hirschau, Germany
(09622) 1 03 30, Fax (09622) 1 83 76, Telex 17 962 282 akwav

Alquexco S.A,
Av.81 N° 69 B-40, Apart.53920, Bogota, Colombia,
223 91 46,251 86 00, Telex 45480

Arcotex
Padre Tadeo No 4920, Casilla 12083, Santiago, Chile
73 55 26, Telex 294 311

ASEA, Perini Hermanos
Cra.19N°,22 B 03, AA.472, Pasto, Colombia
32 449,38 337, Fax 32 449

Atlas Copco,
Ernestinenstra�e 155,4300 Essen 1, Germany
(0201) 247-0, Fax (0201) 21 67 07, Telex 857 467

Barrenas Sandvik Andina S.A.
Fermin Tanguis 160 Urb. Santa Catalina - La Victoria
Apart.6183 Lima 1 do, Lima, Peru,
(51-54) 70 58 85,70 80 30, Fax 70 58 78, Telex 25406 PE

Becorit, siehe KHD
Berry Neu Turbomachines
47 rue Fourier, B.P.327, 59020 Lille, France
(033) 20 09 68 58, Fax (033) 20 92 90 76, Telex 820 257

B�hler
Postfach 80,8605 Kapfenberg, Austria
(03862) 291 85 85, Fax (03862) 33 i 97, Telex 36 529

Bosch
Postfach 10 01 56,7022 Leinfelden-Echterdingen 1, Germany,
(0711) 7 90 31, Telex 72 527 500

Brauer
Goethestra�e 11, 6140 Bensheim 3, Germany
(06251) 7 30 68, Fax (06251) 7 39 55

Campo Nuevo,
Cas.4365 La Paz, Bolivia,
350409

CEAG
Postfach 305.4600 Dortmund 1, Germany
(0231) 5 17 30, Fax (0231) 517 31 89, Telex 8227 575

Compa��a Minera Industrial Buena Fortuna S.R.L
Juan L. Miller 175, Urb. La Chalaca, Callao, Peru
65 72 03,65 99 65, Fax 65 99 65

Consorcio Metalurgico S.A. COMESA
Calle Omega 215, Parque Internacional de la Industria y Comercio
Apart.3528, Callao, Peru,
52 68 43,52 12 29,51 09 20, Fax 51 09 20, Telex 26992 PE HILCO,
30300 CP SMGL

Continental
Konigsworther Platz 1,3000 Hannover 1, Germany
(05 M ) 765-1, Fax (05 M ) 765 27 66, Telex 92 170
Cyphelly & Cie,
Techniques Hydro-mechaniques, 1588 Cudrefin, Switzerland

DeBeSa
Burqplatz 4,5 144 Kreuzau, Germany
(02422) 80 85, Fax (02422) 80 84. Telex 833 944

Denver Equipment Division Joy Manufacturing Company
621 South Sierra Madre, P.O. Box 340, Colorado Springs, CO 80901,
USA,
(303) 471 -3443, TWX 910-920-4999, Telex 45-2442

Desarrollo de Recursos Nacionales DERENA S.A,
Jiron Rodolfo Beltran 929 Lima 1, Peru
2386 12,23 15 18,Fax (51-14) 31 08 48,Telex 25656
Dopke,
Postfach 150,2980 Norden, Germany
(04931) 1 20 36

Dorr-Oliver
Friedrich-Bergius-Stra�e 5,6200 Wiesbaden 12, Germany,
(06121) 70 41, Telex 04 186 756

Dragas HG LtDA
A.A.56650, Medellin, Colombia
277 95 69,255 78 05, Fax 255 77 88, Telex 66 878 Draco,

Dragas HG LtDA
Orfebres del Pacifico, Ed. San Francisco 300, Pisa 19, Of. No.1,
Guayaquil, Ecuador
300671

Eduardo S.A.
Avenida N° 1 Parque Industrial Liviano, Apart..1947, Santa Cruz, Bolivia,
2 28 97,3 76 53, Fax 4 93 44, Telex 4395 Eduardo BV

Equipos Industriales Astecnia Ltd
Carrera 52-A N° 42-A-07 Sur., Apart.19784, Bogota, Colombia,
238 36 19,270 13 94,270 36 68, Telex 42218 ASTEC-CO

Fabrica de Herramientas Nacionales S.A. FAHENA,
Calle Las Fraguas 191, Urbanizacion Ind. El Naranjal, Apart.813 Lima
100,
Lima 31, Peru
81 59 13,81 50 61, Fax 72 08 88, Telex 20250 STEEL IND

Fabricacion Industrial de Maquinarias S.A. FIMA,
Av. Materiales 2632, Apart.3111 Lima 100, Lima, Peru,
52 61 35,52 99 62, Fax 52 91 22, Telex 25389 PE FIALFA

Fabricaciones Mecanicas S.A. FAMESA
Jiron Chavez Tueros 1266 Chacra Rios Sur, Lima Peru,
31 02 16,31 67 41, Fax 3; 67 41, Telex 25582 PE IMEMSA

Fabricaciones Mineras Industriales Comerciales FAMINCO S.A.,
Carlos Villaran 876, Piso 3 Santa Catalina, Apart.5952, Lima 13, Peru
727183,727064,Faxil 1463

FACO Fabrica de Ago Paulista
Ave. Pres. Wilson, 1.716, CEP 0310; Caixa Postal 3190, Sao Paulo,
Brasil
274-6055, Telex 0 M 331 86 FACO BR

Fagersta Secoroc del Peru S.A
Calle Omega 167, Carmen de la Legua, Callao, Peru,
51 7700, 51 7682,Fax 52 4209

Falcon Concentratos,
9807 · 196 · Street, Langley B.C, Canada Y3A 4P8,
(604) 888-55 68, Fax (604) 888-52 82

Famia Industrial S.A.,
Heroes de la Brena 2790, Ate. Lima, Peru
32 99 23,32 99 24,31 22 07, Fax 31 89 14, Telex 25074 PE

FCAP-UMSS,
Casilla 4740, Cochabamba, Bolivia,
2 44 69, Telex 6220 CPBX

Flygt
Bayernstra�e 11,3012 Langenhagen, Germany
(05 11) 7 80 00, Fax (0511) 78 28 93, Telex 924 059

Frantz
Hinschstra�e 45, 6000 Frankfurt am Main 60, Germany
(069) 4089-0 Telex 417 355

Friemann + Wolf,
Meidericher Stra�e 6-8,4100 Duisburg 1, Germany
(0203) 3002-0, Fax (0203) 3002 240, Telex 855 543

FUNDEMIN,
Av. Jimenez No.4-03 OF.1006, AA 20030, Bogota, Colombia,

Fundicion Callao S.A.,
Av. Argentina 3719 Apart.111 Callao, Callao, Peru
51 29 90, Fax 51 59 87, Telex 26003

Fundicion de Hierro Sud America FUNSA
Calle Roberto Hinojosa Esq. Av.31 de Octubre, Apart.1872, Villa San
Antonio, La Paz, Bolivia,
330451,81 0325

Fundacion Ventanilla S.A. FUNVESA,
Av. La Marina 1353 San Miguel Lima, Peru
62 64 92, 62 65 47, 61 91 00 , Telex 25257 PE PB SIS

Gebruder Abt,
8948 Mindelheim/Schwaben, Germany

Goldfield,
P.O.Box 117, Provo, Utah 84603. USA
801 374-66 11, Fax 801 374-66 2

GOLDSPEAR (UK) LTD
Box 203 Beaconsfield, Bucks HP9 2TQ, Great Britain
(0494) 67 84 11, Fax (0494) 67 87 31

Grauvogel
B.P.63 67702 Saverne Cedex, France
(88) 9 i 12 53, Telex 89 0681

H.M. Representaciones S.A.
Av. Contralmirante Mora 590, Apart. 520 - Callao Callao, Peru
65 30 68,65 14 17,65 93 55, Fax 65 i 4 17, Telex 26002 PE PB - CALLAO

Haver + Boecker
Postfach 33 20, Enningerloher Stra�e 64,4740 Oelde
Westfalen, Germany
(02522) 301, Fax (02522) 3 04 04, Telex 89 476 haverd

HBS-Equipment Div.,
3000 Supply Ave., Los Angeles, CA.90040. USA
(213) 726-3033

Hoechst,
Verkauf Chemikalien, Postfach 80 03 20,6230 Frankfurt am Main 80
Germany

Humphrey Mineral Industries, Inc.
2219 Market Street, Denver CO 80205 USA
(303) 296-8000, Telex 45-588
IHGC Sliedrecht BV,
P.O. Box 3,3360 AA, Sliedrecht, Netherland

Impler,
Hummelhausen 3, 8201 Au b. Bad Feilnbach, Germany,

INCOMEC Ltda.,
M. Melgarejo E.1713, Cochabamba, Bolivia
43045

Industria Acero de los Andes S.A. IAA
Av. Eloy Alfaro 939 y Av. Amazonas, Ed. Finandes 1er. piso,
Apart. 235 A, Quito, Ecuador
50 36 00,50 36 01,50 36 02, Fax (59 32) 50 36 33, Telex 2 M 98 IlA ED

Industria Constructora de Maquinaria INCOMAQ
Sambrano s/n · Comite del Pueblo, Apart.706, Quito, Ecuador,

Industrias Metal�rgicas Van Dam C.A.,
2a Av. de Campo Alegre, Torre Credival, Piso 2 of. B., Apart. 1169
Caracas 1010A, Caracas, Venezuela
62 59 94,62 97 10, Telex 21245 VD, 21480 VD

Ingenieria de Proyectos y Construcci�n S.R.L. IMPROCON
Av,20 de octubre 2618, Edificio Kantuta - Mezzanine Of.5, La Paz Bolivia,
Ingersoll-Rand,
Siemensstra�e 16-20,4040 Neuss 21, Germany
(02107) 10 09-0, Telex 8 585 006

Ingersoll -Rand
100 Thanet Circle, Suit 300, Princeton, N.J., 08540 - 3662, USA,
(609) 921 86 88

Inteco
68 Rajendra Market, Tiz Nahir, Dehli 54, India

italvibras
Via Pualia 36,41049 Sassuolo, Italy
(0536) 80 46 34, Telex 5 10 887 itvbra i

John Blake Ltd,
PB 43, Accrington, Lancashire, Great Britain

Jost,
Hammer Stra�e 95,4400 Munster, Germany
(0251) 7797-0, Fax (0251) 77 97 101, Telex 892 7 16

Kaeser
Postfach 21 43,8630 Coburg, Germany
(09561) 640-0, Fax (09561) 64 01 30, Telex 663 264

Keene,
9330 Corbin Ave., Northridge, California 91324, USA,
(818) 933-0411

KHD
Postfach 91 04 57,5000 K�ln 91, Germany
(0221) 82 30, Telex 8812 267

Kleenoil,
30a Robert Street, Harrogate, North Yorkshire HG1 IHP Great Britain
(0432) 52 29 11, Fax (0423) 53 00 43, Telex 57 784 MCCL G

Knelson, Lee-Mar Industries Ltd
R.R. # 11 20313 86th Avenue, Langley, B.C., Canada V3A 6Y3
(604) 888 4000/(604) 421 -3255, Fax (604) 888-4001,
Telex 04-35 12 79 ab

Krantz, Rheinisches Mineralien-Kontor KG,
Fraunhoterstra�e 7,5300 Bonn 1, Germany,
(0228) 66 20 55, Fax (0228) 66 72 66

Krug,
Bornstra�e 291 4600 Dortmund 1, Germany
(0231) 83 80 to Fax (0231) 83 80 727, Telex 822 578

Krupp Widia
Munchener St;aBe 90,4300 Essen 1, Germany
(0201) 725-0,Fax(0201) 725-3035,Telex85718 14

Krupp,
Franz-Schubert-Stra�e 1-3,Postfach 14 19 60, 4100 Duisburg 14,Germany
(02135) 78-0, Fax (02135) 75191, Telex 855 486-0

Las Gaviotas,
calle 18A, No. 1E, Apdo.4976, Ap. Aereo 18261, E;ogot3, Colombia

lenoir et merrier
BP 80,08120 Bogny-sur-Meuse France
2432 1332, Fax 2432 1378, Telex 840 392 lenoir f

MAD (Vorholt & Schega)
Postfach 151,4358Haltern Germany,
(02364) 10 10, Telex 829 888 vasch d

Maestranza General S.A. MAGENSA
Jiron Rodolfo Beltran 631, Apart.1075, Lima 1 Peru
32 36 36,32 37 53, Telex 25820 PE COMETRU, 20141 PE PRUTRAD,

Maestranza Industrial S.A. MAENSA
Av. Las Vegas 845, Zona Industrial San Juan de Miraflores Lima, Peru
67 82 06,67 66 05, Fax (51 · 14) 67 82 07, Telex 21583 PE RGTRADE

Maestranza y Fundicion Quillacollo MAFUQUI
Av. Albina Km.4,5 Quillacollo, Apart.2024, Cochabamba, Bolivia
6 03 02,6 01 71, Cables MAFUOUI

Mannesmann Demag
Solmstra�e 2-26,6000 Frankfurt am Main 90, Germany
(069) 7901-0, Fax (069) 707 24 33, Telex 411 172

Maquinarias y Equipos Peruanos S.A. MAEPSA,
Av. La Marina 1353, San Miguel, Lima, Peru,
62 64 92,61 91 00,62 65 47, Fax 6 i 91 do. Telex 25257 PE PB SIS

Merck,
Frankfurter Stra�e 250,6100 Darmstadt, Germany
(06151) 720,Fax [06151) 72 33 68, Telex 4193 280 em d

Metal Callao E.P.S.,
Av. Los Ferroles 301 Urb. Bocanegra Apart.488 Callao Peru, 29 66 69,29 91 37

Metal Mec�nica Soriano S.A.,
Av. Costanera 708, San Miguel, Lima, Peru,
5245 19

Metalmecanica Milag - Millan
Landaeta 1084, La Paz, Bolivia,
78 54 78,35 78 71

Metalurgica Lacha,
Arawi 243 Cala-Cala, Cochabamba, Bolivia
45067,4 1202

Metalurgica Peruana S.A. MEPSA,
Placido Jimenez 1051 Apart. 5193 Lima 100 Lima 1, Peru,
28 32 85,28 62 97,28 62 98, Fax 32 66 66 Telex 25793

Mineral Deposits,
81 Ashmore Road, Southport, Qld.4215, Australia,
(075) 39 90 55, Fax (075) 39 98 63, Telex AA 40 438

Mineral Equipment, Inc.
Precious Metals Extraction (PMX), 3740 Rocklin Road, Rocklin, CA
95677,
California, USA,
(916) 624-4577

Mogensen
Kronskamp; 26,2000 Wedel/Hamburg, Germany,
(04103) 8042-0, Fax (04103) 80 42 40

Mainzer Stra�e 118,6200 Wiesbaden, Germany
(06121)702891,Fax(06121) 71 3702, Telex 4186220

Mozley,
Cardrew, Redruth, Cornwall TR 15 ISS, Great Britain,
(0209) 21 10 81, Fax (0209) 21 10 68, Telex 45 735 mozley 9

Netter
Hasengartenstra�e 40,6200 Wiesbaden, Germany,
(06121)700051,Fax(06121)71 3858, Telex 4186697

Northern Light,
1 A 3781 Victoria Park Ave., Scarborough,
Ontario M/W 3K5, Canada

Oldorid
Hulsbergstra�e 255,4370 Marl/Westfalen, Germany,
(02365) 8508-9, Fax (02365) 8 28 71, Telex 829 411 olver d

Oliver Manufacturing Company,
P.O. Box 512, Rocky Ford, CO 81067, Colorado. USA,
(303) 254-6371

Ossberger,
Otto Rieder-Stra�e 7,8832 Weissenburg/Bayern, Germany,
(09141) 40 91, Telex 624 672

Outokumpu,
Ritritontuntie 7D, P.O. Box 84.02201 Espoo, Finlandia
04211, Fax 042 i 24 34, Telex 121 461 autosf

Pfister & Langhanss,
Sandstra�e 2-8,8500 Nurnberg, Germany

Pleiger,
Postfach 32 63,5810 Witten 3, Germany
(02324) 398-0, Fax (02324) 39 83 28, Telex 8229 964

Productos Perfilados S.A. PROPER
Enrique Meiggs 262, Parque Int. Industria y Comercio, Callao, Peru,
52 1755,51 5944

Rife Hydraulic Engine Man.,
PB 367, Millburn, New Jersey 07041, USA

Sala,
73300 Sala, Sweden,
(0224) 1 32 20, Telex 7536 sala s

Salzgitter,
Postfach 12 63.4408 Dulmen, Germany,
(02594) 77-0, Fax (02594) 7 72 96, Telex 89 813 epr d

Schauenburg,
Weseler Stra�e 35,4330 Mulheim/Ruhr, Germany,
(0208) 588-0, Telex 0856 787

Schenck,
Postfach 40 18,6100 Darmstadt, Germany,
(06151) 32-0, Fax (06151) 32 32 24, Telex 4196 940 cs d

Schlumpf AG,
Bahnhofstra�e; 5,6312 Steinhausen/Zug, Switzerland,
41 (42) 41 43 43, Fax 41 (42) 41 18 66, Telex 868 968

Sermitec,
Los Platanos 2729, Macul, Santiago, Chile,
2219 597, Fax 2215 783, Telex 346 257 stager ck

Siebtechnik,
Postfach 10 17 51, Platanenallee 46,4330 Mulheim/Ruhr, Germany,
(0208) 587-0. Fax (0208) 58 73 00, Telex 856 825

SIG,
Bereich Bergbau, 8212 Neuhausen am Rheinfall, Switzerland,
(053) 21 61 11, Fax (053) 21 66 06, Telex 896 027 sig ch

SOTEEL S.R.L.
J.A. de Padilla Calle 3 entre Heroes del Chaco, Corretera La Paz km
3,

Oruro, Bolivia,
10801
Postfach i 1 02 09, Fellerstra�e 4,5620 Velbert 11, Germany,
(02052) 605-0, Telex 8516 795

Steve and Duke's Manufacturing Co.,
2500-Z Valley Road, Reno, NV 89512, Nevada, USA,
(702) 322-1629

SVALCOR,
Andrade Duenas, Barrio La Cristiania, Casilla 6070 CCI, Quito,
Ecuador,
473-200,243-731

T. Heintzmann,
Bessemerstra�e 80, Postfach 10 1029,4630Bochum 1,Germany,
(0234) 619-1, Telex 0825 879 heco-d
Taller "Centro del Muchacho Trabajador",

Plaza Marin, Quito, Ecuador
Talleres J.G.,
Casilla 226, Machala, Ecuador,
922-299

Talleres Mejia,
Turuhuayco 270, Apart. 36-A, Cuenca, Ecuador,
800361,800297
P.O.B. 512,33101 Tampere, Finlandia
(0358) 31 32 400, Telex 22 616 tools sf

Telsmith,
Smith engineering works, Milwaukee, Wisconsin, USA

Turmag,
Postfach 13 80,4322 Sprockhover 1, Germany,
(02324) 7003-0, Fax (02324) 70 03 27, Telex 8229 953

Vardax,
3025 Eldridge Ave, Bellingham WA 98225, USA,
(206) 671 -7817, (206) 671 -7820

Vautid-Verschlei�technik,
Postfach 41 10,7302 Stuttgart-Ruit, Germany,
(0711) 44 20 31, Fax (0711) 44 20 39, Telex 722 687

Volcan S.A.,
Av. Chacaltaya 1350, Apart.214, La Paz, Bolivia,
34 03 84,35 50 94, Telex 3460

WAMA,
Th.-Mayr Stra�e 5,8018 Grafing. Germany
(08092) 45 08
Hundersta�e 13,7100 Heilbronn, Germany,
(07131)42561,Fax(07131)4831 65,Telex728 137

Wilfley Mining Machinery Co. Ltd.,
Cambridge Street, Wellingborough, Northamptonshire, NN8 1 DW,
Great Britain
44 (933) 22 63 68, Fax 44 (933) 44 13 77, Telex 31 7220 WILMIN G

Wolff,
Wolfbankring 38.4300 Essen 1, Germany,
(0201) 67 10 11, Fax (0201) 68 10 1 1

Zutta Hermanos,
Calle 13A,No 17-25-59,AA.325,Pasto,Colombia,
322-27

CLOSE THIS BOOKTools for Mining: Techniques and Processes for Small Scale Mining (GTZ, 1993, 538 p.)
VIEW THE DOCUMENT(introduction...)
VIEW THE DOCUMENTAcknowledgements
VIEW THE DOCUMENTPreface
VIEW THE DOCUMENTGuide to the user
VIEW THE DOCUMENTIntroduction
A. Analysis
Technical Chapter 1: Analysis
B. Underground mining
Technical Chapter 2: Safety Techniques
Technical Chapter 3: Ventilation
Technical Chapter 4: Water supply and drainage
Technical Chapter 5: Support
Technical Chapter 6: Lighting
Technical Chapter 7: Stoping
Technical Chapter 8: Loading
Technical Chapter 9: Hauling
C. Surface mining
Technical Chapter 10: Surface Mining Equipment
Technical Chapter 11: Other special techniques
D. Beneficiation
Technical Chapter 12: Crushing
Technical Chapter 13: Classification
Technical Chapter 14: Sorting
Technical Chapter 15: Gold Benefication
Technical Chapter 16: 0ther Sorting and Separating Techniques
Technical Chapter 17: Drying
Technical Chapter 18: Clarification
E. Mechanization and energy supply
Technical Chapter 19: Energy Techniques
VIEW THE DOCUMENTBibliography
VIEW THE DOCUMENTList of manufacturers and suppliers
VIEW THE DOCUMENTList of abbreviations

List of abbreviations

A.D.

Anno Domini

AGID

Association of Geoscientists for International Development

AKW

Amberger Kaolinwerke

approx.

Aproximate

B.C.

Before Christ

BGR

German Federal Institute for Geosciences and Raw

Material


cif

Cost insurance freight

COMIBOL

Coorporacion Minera de Bolivia

Coop.

Cooperative

Cord.

Cordillera

CSMRI

Colorado School of Mines

DAV

German Alpine Club

DBM

German Mines Museum

DDR

German Democrate Republic

DE

German Patent

Dept.

Departamento

DM

Deutsch Mark

e.g.

Exempli grati (lat. = for instance)

E/MJ

Engineering Mining Journal

Ed.

Edition

EP

European Patente

etc.

Etcetera

Fig.

Figure(s)

fob.

Free on board

FONEM

Fondo Nacional de Exploracion Minera, La Paz

GATE

German Appropiate Technology Exchange

GFK

Glasfaserverstarkter Kunststoff (glass fibre-reinforced synthetic)

GTZ

Gesellschaft fur Technische Zusammenarbeit (German Technical Cooperation)

KfW

Kreditanstalt fur Wiederaufbau

KHD

Klockner Humboldt Deutz

LA

Latin-America

M.S.L.

Mean Sea Level

MAK

Maximale Arbeitsplatzkonzentration (maximum concentration at work place)

max.

Maximum

min.

Minimum

MWSt

Mehrwertsteuer (value added taxes)

NE

Nichteisen (non-ferrous)

No.

Number

P,

Page

PAAC

Programa de Asistencia Agrobioenergetica al Campesino

PE

Polyethylene

PGM

Platin Group Metals

PVC

Polyviniychlorid

R+D

Research and Development

RFA

X-rayfluorescentanalyses

SKAT

Schweizerische Kontaktstelle fur Angepa�te Technik (Swiss Contact Agency for Appropriate Technology)

SM

Schwermineral (heavy mineral)

TMM

Taller Metal Mecanico

TZ

Technische Zusammenarbeit (Technical Cooperation)

US $

American Dollar

UV

Ultra-violet

VDI

Verein Deutscher Ingenieure (Association of German Engineers)

VITA

Volunteers in Technical Assistance

WHO

World Heath Organisation

PHYSICAL QUANTITIES, SIMBOLS OF FORMULAE AND UNITS

Inch, approx. 2.5 cm

%

Per-cen

Foot, approx. 30 cm

<

Smaller then

>

Bigger then


Difference

A

Ampere

a

Year

W

Width

bar

Bar-pressure

Be

Beaume

C

Degree Celsius

cd

Candela, measurement for degree of luminosity

cm

Centimetre

cm³

Cubic centimetre

d

Diameter, density

D

Diameter, Depth

die

Diameter

En

Electrons' potential

F

Force

f (...)

Function of

ft.

Foot

g

Earth acceleration, 9.81 m/sec²

g

Gramne

G

Weight

h

Hour

H

Height

HP

Horse-Power

in

Inch

kg

Kilogramme

km

Kilometre

KW

Kilowatts

I

Litre

L

Length

lb.

Libra = pound

m

Metre

M

Man

Cubic metre

min-1 Per minute


min.

Minute

mm

Milimetre

MP

Intermediary (middle) product

MS

Man Shift

Mstat

Statistical moment

µ

Micro

µm

Micro meter

n

Amount

N

Newton

oz

Ounze

p

Pressure

pH

Negative decadic log of hydrogen ions or proton concentration

ppb

Parts per billion

ppm

Parts per million

q

Constant factor

R, r

Radius

rpm

Revolutions per minute

sec.

Second

t

Metric ton

TMF

Tonelade metrica fina

v

Speed

V

Voltage

W

Watt

E

Sum

0

Diameter

°

Degree

°C

Degree Celsius

CHEMICAL SYMBOLS

Ag

Silver

Al

Aluminium

Au

Gold

Bi

Bismuth

C

Carbon

Ca

Calcium

Cd

Cadmium

Cu

Copper

Fe

Iron

H

Hydrogen

Hg

Mercury

M²+

Metalion with double valence

N

Nitrogen

O

Oxygen

Pb

Lead

S

Sulphur

Sb

Antimony

Si

Silicon

Sn

Tin

W

Tungsten

Zn

Zin

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