Recovery of Gold and Iron from Cyanide Tailings with a Combined Direct Reduction Roasting and Leaching Process
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From Base Metals and Back – Isamills and Their Advantages in African Base Metal Operations
The Southern African Institute of Mining and Metallurgy Base Metals Conference 2013 H. de Waal, K. Barns, and J. Monama From base metals and back – IsaMills and their advantages in African base metal operations H. de Waal, K. Barns, and J. Monama Xstrata IsaMill™ technology was developed from Netzsch Feinmahltechnik GmbH stirred milling technology in the early 1990s to bring about a step change in grinding efficiency that was required to make Xstrata’s fine-grained lead/zinc orebodies economic to process. From small-scale machines suited to ultrafine grinding, the IsaMill™ has developed into technology that is able to treat much larger tonnages, in coarser applications, while still achieving high energy efficiency, suited for coarser more standard regrind and mainstream grinding applications. The unique design of the IsaMillTM, combining high power intensity and effective internal classification, achieves high energy efficiency and tight product distribution which can be effectively scaled from laboratory scale to full-sized models. The use of fine ceramic media also leads to significant benefits in downstream flotation and leaching operations. These benefits are key drivers for the adoption of the technology into processing a diverse range of minerals worldwide, and offer major opportunities for power reduction and improved metallurgy for the African base metal operations. Keywords: IsaMill, regrind, energy efficiency, inert grinding. Introduction The development of the IsaMillTM, by MIM (now GlencoreXstrata) and Netzsch Feinmahltechnik GmbH, was initiated to enable the development of the fine-grained ore deposits at Mt Isa and McArthur River in Northern Australia. To liberate the valuable minerals and so produce a saleable concentrate this ultrafine-grained ore needed to be ground to a P80 of 7 μm. -
Significance of Mineralogy in the Development of Flowsheets for Processing Uranium Ores
JfipwK LEACHING TIME REAGENTS TEMPERATURE FLOCCULANT CLARITY AREA COUNTER CURRENT DECANTATION It 21 21 J^^LJt TECHNICAL REPORTS SERIES No.19 6 Significance of Mineralogy in the Development of Flowsheets for Processing Uranium Ores \W# INTERNATIONAL ATOMIC ENERGY AGENCY, VIENNA, 1980 SIGNIFICANCE OF MINERALOGY IN THE DEVELOPMENT OF FLOWSHEETS FOR PROCESSING URANIUM ORES The following States are Members of the International Atomic Energy Agency: AFGHANISTAN HOLY SEE PHILIPPINES ALBANIA HUNGARY POLAND ALGERIA ICELAND PORTUGAL ARGENTINA INDIA QATAR AUSTRALIA INDONESIA ROMANIA AUSTRIA IRAN SAUDI ARABIA BANGLADESH IRAQ SENEGAL BELGIUM IRELAND SIERRA LEONE BOLIVIA ISRAEL SINGAPORE BRAZIL ITALY SOUTH AFRICA BULGARIA IVORY COAST SPAIN BURMA JAMAICA SRI LANKA BYELORUSSIAN SOVIET JAPAN SUDAN SOCIALIST REPUBLIC JORDAN SWEDEN CANADA KENYA SWITZERLAND CHILE KOREA, REPUBLIC OF SYRIAN ARAB REPUBLIC COLOMBIA KUWAIT THAILAND COSTA RICA LEBANON TUNISIA CUBA LIBERIA TURKEY CYPRUS LIBYAN ARAB JAMAHIRIYA UGANDA CZECHOSLOVAKIA LIECHTENSTEIN UKRAINIAN SOVIET SOCIALIST DEMOCRATIC KAMPUCHEA LUXEMBOURG REPUBLIC DEMOCRATIC PEOPLE'S MADAGASCAR UNION OF SOVIET SOCIALIST REPUBLIC OF KOREA MALAYSIA REPUBLICS DENMARK MALI UNITED ARAB EMIRATES DOMINICAN REPUBLIC MAURITIUS UNITED KINGDOM OF GREAT ECUADOR MEXICO BRITAIN AND NORTHERN EGYPT MONACO IRELAND EL SALVADOR MONGOLIA UNITED REPUBLIC OF ETHIOPIA MOROCCO CAMEROON FINLAND NETHERLANDS UNITED REPUBLIC OF FRANCE NEW ZEALAND TANZANIA GABON NICARAGUA UNITED STATES OF AMERICA GERMAN DEMOCRATIC REPUBLIC NIGER URUGUAY GERMANY, FEDERAL REPUBLIC OF NIGERIA VENEZUELA GHANA NORWAY VIET NAM GREECE PAKISTAN YUGOSLAVIA GUATEMALA PANAMA ZAIRE HAITI PARAGUAY ZAMBIA PERU The Agency's Statute was approved on 23 October 1956 by the Conference on the Statute of the IAEA held at United Nations Headquarters, New York; it entered into force on 29 July 1957. -
Some Problems and Potentials of the Study of Cupellation
Some problems and potentials of the study of cupellation remains: the case of post-medieval Montbéliard, France Marcos Martinon-Torres, Nicolas Thomas, Thilo Rehren, Aude Mongiatti To cite this version: Marcos Martinon-Torres, Nicolas Thomas, Thilo Rehren, Aude Mongiatti. Some problems and po- tentials of the study of cupellation remains: the case of post-medieval Montbéliard, France. Archeo- sciences, revue d’Archéométrie, G.M.P.C.A./Presses universitaires de Rennes, 2008, pp.59-70. halshs- 00599974 HAL Id: halshs-00599974 https://halshs.archives-ouvertes.fr/halshs-00599974 Submitted on 19 Jun 2011 HAL is a multi-disciplinary open access L’archive ouverte pluridisciplinaire HAL, est archive for the deposit and dissemination of sci- destinée au dépôt et à la diffusion de documents entific research documents, whether they are pub- scientifiques de niveau recherche, publiés ou non, lished or not. The documents may come from émanant des établissements d’enseignement et de teaching and research institutions in France or recherche français ou étrangers, des laboratoires abroad, or from public or private research centers. publics ou privés. Some problems and potentials of the study of cupellation remains: the case of early modern Montbéliard, France Problèmes et perspectives à partir de l’étude des vestiges archéologiques issus de la coupellation : l’exemple du site de Montbéliard (France) Marcos Martinón-Torres*, Nicolas Thomas**, Thilo Rehren*, and Aude Mongiatti* Abstract: Bone-ash cupels are increasingly identified in medieval and later archaeological contexts related to the refining of noble metals in alchemy, assaying, jewellery or coin minting. These small finds may provide information on metal refining activities, the technical knowledge of different craftspeople, and the versatility of laboratory practices, which often differed from the standard protocols recorded in metallurgical treatises. -
Curbing Illicit Mercury and Gold Flows in West Africa: Options for a Regional Approach
Curbing Illicit Mercury and Gold Flows in West Africa: Options for a Regional Approach i INCLUSIVE AND SUSTAINABLE INDUSTRIAL DEVELOPMENT ii Curbing Illicit Mercury and Gold Flows in West Africa: Options for a Regional Approach iii November 2018 iv © UNIDO 2018. All rights reserved. This document has been produced without formal United Nations editing. The designations employed and the presentation of the material in this document do not imply the expression of any opinion whatsoever on the part of the Secretariat of the United Nations Industrial Development Organization (UNIDO) concerning the legal status of any country, territory, city or area or of its authorities, or concerning the delimitation of its frontiers or boundaries, or its economic system or degree of development. Designations such as ‘developed’, ‘industrialized’ or ‘developing’ are intended for statistical convenience and do not necessarily express a judgement about the stage reached by a particular country or area in the development process. Mention of firm names or commercial products does not constitute an endorsement by UNIDO. Unless otherwise men- tioned, all references to sums of money are given in United States dollars. References to ‘tons’ are to metric tons, unless otherwise stated. All photos © UNIDO unless otherwise stated. Cover photo by Sadibou Sylla Acknowledgements This report was authored by Marcena Hunter of the Global Initiative Against Transnational Organized Crime. The report is part of the United Nations Industrial Development Organization (UNIDO) project, funded by the Government of Switzerland, to assist the Economic Community of West African States (ECOWAS) in its early implementation of the Minamata Convention. More information about the Minamata Convention and UNIDO’s work can be found on UNIDO’s website <https://www.unido.org/mercury> or by emailing Gabriela Eigenmann at [email protected]. -
S Ndlovu (PDF)
Extraction of Gold Then, Now and the Future Prof Sehliselo Ndlovu DST/NRF SARChI: Hydrometallurgy and Sustainable Development University of the Witwatersrand, Johannesburg Building a Robust Minerals Industry 3 – 4 July 2017, Cresta Lodge, Harare University of the Witwatersrand Johannesburg Founded Oct. 1896: School of Mines Approx. 37 000 Students 5 Faculties, 33 Schools, 3610 Courses >160 000 Degrees Conferred since 1922 55% Female Students 10 National Centres of Excellence Home to the Bidvest Football Club( Current PSL league Champions) Evolution in Gold Processing Past Technologies • Amalgamation • Panning Current Technologies • Cyanide leaching • Processing of Emerging and Future refractory ores Technologies • Bio-oxidation • Ionic liquids • Alternative leaching • Ultrasonic leaching reagents • Corn starch?? Past Technologies Used in Ancient Times History of gold extends back at least 6,000 years. Egypt and Mesopotamia around 4000 BC. Gravity Separation: Gold Panning Gold concentrated by washing lighter river sands with water Leaves dense gold particles Alternative- wash gold-bearing sand and gravel over a woollen fleece Traps heavier gold dust that would sink into the wool fibres. Advantages • Simplicity Disadvantages • Labour intensive Gravity Separation: Sluicing • Water is channelled to flow through a sluice-box. • Sluice-box is essentially a man-made channel with riffles (barriers) at the bottom. • Riffles create dead-zones in the water current which allows gold to drop out of suspension. Sluicing and panning results in the direct recovery of small gold nuggets and flakes. Gold Parting: Salt Cementation Process • Invented to remove Ag from Au-Ag mixtures around 6th century BC. Mix: argentiferous gold foil, common salt, brick dust or burnt clay and urine in a sealed container. -
Principles of Extractive Metallurgy Lectures Note
PRINCIPLES OF EXTRACTIVE METALLURGY B.TECH, 3RD SEMESTER LECTURES NOTE BY SAGAR NAYAK DR. KALI CHARAN SABAT DEPARTMENT OF METALLURGICAL AND MATERIALS ENGINEERING PARALA MAHARAJA ENGINEERING COLLEGE, BERHAMPUR DISCLAIMER This document does not claim any originality and cannot be used as a substitute for prescribed textbooks. The information presented here is merely a collection by the author for their respective teaching assignments as an additional tool for the teaching-learning process. Various sources as mentioned at the reference of the document as well as freely available material from internet were consulted for preparing this document. The ownership of the information lies with the respective author or institutions. Further, this document is not intended to be used for commercial purpose and the faculty is not accountable for any issues, legal or otherwise, arising out of use of this document. The committee faculty members make no representations or warranties with respect to the accuracy or completeness of the contents of this document and specifically disclaim any implied warranties of merchantability or fitness for a particular purpose. BPUT SYLLABUS PRINCIPLES OF EXTRACTIVE METALLURGY (3-1-0) MODULE I (14 HOURS) Unit processes in Pyro metallurgy: Calcination and roasting, sintering, smelting, converting, reduction, smelting-reduction, Metallothermic and hydrogen reduction; distillation and other physical and chemical refining methods: Fire refining, Zone refining, Liquation and Cupellation. Small problems related to pyro metallurgy. MODULE II (14 HOURS) Unit processes in Hydrometallurgy: Leaching practice: In situ leaching, Dump and heap leaching, Percolation leaching, Agitation leaching, Purification of leach liquor, Kinetics of Leaching; Bio- leaching: Recovery of metals from Leach liquor by Solvent Extraction, Ion exchange , Precipitation and Cementation process. -
Table of Contents
Table of Contents Preface ........................................... xi Chapter 1. Physical Extraction Operations .................... 1 1.1. Solid-solid and solid-fluid separation operations .............. 1 1.1.1. Flotation ................................... 1 1.1.2. Settling under gravity ........................... 3 1.1.3. Centrifugation ................................ 3 1.1.4. Filtration ................................... 4 1.2. Separation operations of the components of a fluid phase ........ 5 1.2.1. Condensation ................................ 5 1.2.2. Vacuum distillation ............................. 5 1.2.3. Liquation ................................... 6 1.2.4. Distillation .................................. 8 1.2.5. Extractive distillation ........................... 11 1.3. Bibliography ................................... 12 Chapter 2. Hydrometallurgical Operations .................... 15 2.1. Leaching and precipitation operations .................... 15 2.1.1. Leaching and precipitation reactors ................... 15 2.1.2. Continuous stirred tank reactor (CSTR) ................ 18 2.1.3. Models of leaching and precipitation operations ........... 20 2.1.4. Particle-size distribution (PSD) functions ............... 21 2.2. Reactor models based on particle residence time distribution functions ........................................ 24 2.2.1. Performance equations for a single CSTR ............... 24 2.2.2. Performance equations for multistage CSTRs ............. 28 2.3. Reactor models based on the population balance -
Metal Leaching in Mine-Waste Materials and Two Schemes for Classification of Potential Environmental Effects of Mine-Waste Piles
Metal Leaching in Mine-Waste Materials and Two Schemes for Classification of Potential Environmental Effects of Mine-Waste Piles By David L. Fey and George A. Desborough Chapter D4 of Integrated Investigations of Environmental Effects of Historical Mining in the Basin and Boulder Mining Districts, Boulder River Watershed, Jefferson County, Montana Edited by David A. Nimick, Stanley E. Church, and Susan E. Finger Professional Paper 1652–D4 U.S. Department of the Interior U.S. Geological Survey ffrontChD4new.inddrontChD4new.indd ccxxxviixxxvii 33/14/2005/14/2005 66:07:29:07:29 PPMM Contents Abstract ...................................................................................................................................................... 139 Introduction ............................................................................................................................................... 139 Purpose and Scope ......................................................................................................................... 140 Sample Collection and Preparation ....................................................................................................... 140 Bulk Surface Samples ..................................................................................................................... 140 Two-Inch Diameter Vertical Core .................................................................................................. 140 Location of Mine-Waste Sites ............................................................................................................... -
Simulation Study of the Optimal Distribution of Cyanide in a Gold Leaching Circuit
Minerals Engineering 19 (2006) 1319–1327 This article is also available online at: www.elsevier.com/locate/mineng Simulation study of the optimal distribution of cyanide in a gold leaching circuit L.R.P. de Andrade Lima a,b,*, D. Hodouin a a Department of Mining, Metallurgical, and Materials Engineering, Laval University, Quebec City, Canada G1K 7P4 b Department of Materials Science and Technology, Federal University of Bahia, C.P. 6974, Salvador, BA 40810-971, Brazil Received 25 September 2005; accepted 1 December 2005 Available online 19 January 2006 Abstract The mineral industry has been using cyanidation to recover gold from ores for more than a century; however, a systematic study of the best reactant addition strategy in a cascade of agitated leaching tanks is not available in the open literature. A phenomenological math- ematical model of the gold cyanidation process, calibrated with a set of industrial data from an Australian plant, together with an eco- nomic performance index is used to analyze this problem. The simulated results show that the best compromise between the two antagonistic effects, cyanide consumption and gold recovery, which are both function of cyanide concentrations, leads to a reagent dis- tribution that depends on the leaching and cyanide consumption kinetics, pulp feed characteristics, and economic factors such as the gold market value. For the specific studied plant, in the operating range of low cyanide consumption and fast gold dissolution, all the cyanide must be added in the first tank; however, in the operating conditions of high cyanide consumption, cyanide has to be distributed in the first, second and third tanks. -
Metallurgical Leaching
METALLURGICAL LEACHING Metallurgical leaching is a mining technology that involves the treatment of mineralmaterials, mainly oxidized containing desirable metals and which are reduced in size to be subjected to a wet process with acidic or basic solutions to dissolve soluble elements and concentrate in an enriched solution, so it is considered a “hydrometallurgical” process. This process allows to work “mineral deposits” ranked as low concentration provided that the mining operation occurs to a large scale to reduce costs per ton of mineral extraction and ensure profitability in the process. Compared to pyrometallurgical operations, leaching is a much simpler and much less harmful because gaseous pollution never occurs, and because its energy consumption is very low, mostly depending on gravity’s action and pumping solutions to the heap. The control points in the leaching process are to monitor the potential of acid generation of waste rocks to avoid toxicity, the efficiency of the operation and the temperature of the reactions are essential to ensure the profitability of the chemical operation of the reactants. There are various kinds of Metallurgical leaching processes. To choose the most appropriate will generally depend on the type of “reagents” used for the operation, which are selected according to the type of mineral or material being processed and that will generally can be identified as “oxides “or” sulfide” In the case of the leaching of a zinc oxide, a simple leaching reaction can be illustrated in the following formula: ZnO (zinc oxide) + H2SO4 (sulfuric acid) -> ZnSO4 (soluble zinc sulphate) + H20 (water) In the case of aluminum oxide, the leaching can occur with “alkali” solutions, for example, under the following formula: Al2O2 (1 molecule of aluminum oxide) + 3H2O (3 molecules of water) + 2NaOH (2 molecules hydroxide sodium) -> 2NaAl (OH) 4 (hydrated sodium aluminate) The leaching of precious metals like gold and silver can be done very easily with cyanide or ozone under ambient conditions. -
Tungsten and Gold Recovery from Alaskan Scheelite-Bearing Ores
¿I ri 9251 REPORT OF INVESTIGATIONS/1989 LIBRARY SPOKANE RESEARCH CENTER RECEIVED SEP5 1983 U.S. BUREAU OF MINES E 315 MONTGOMERY AVE SPOKANE, W A 99207 Tungsten and Gold Recovery From Alaskan Scheelite-Bearing Ores By J. N. Greaves, W. R. McDonald, and J. H. Maysilles M ission: As the Nation's principal conservation agency, the Department of the Interior has respon sibility for most of our nationally-owned public lands and natural and cultural resources. This includes fostering wise use of our land and water resources, protecting our fish and wildlife, pre serving the environmental and cultural values of our national parks and historical places, and pro viding for the enjoyment of life through outdoor recreation. The Department assesses our energy and mineral resources and works to assure that their development is in the best interests of all our people. The Department also promotes the goals of the Take Pride in America campaign by encouraging stewardship and citizen responsibil- ityforthe public lands and promoting citizen par ticipation in their care. The Department also has a major responsibility for American Indian reser vation communities and for people who live in Island Territories under U.S. Administration. Report of Investigations 9251 Tungsten and Gold Recovery From Alaskan Scheelite-Bearing Ores By J. N. Greaves, W. R. McDonald, and J. H. Maysilles UNITED STATES DEPARTMENT OF THE INTERIOR Manuel Lujan, Jr., Secretary BUREAU OF MINES T S Ary, Director Library of Congress Cataloging in Publication Data: Greaves, J. N. Tungsten and gold recovery from Alaskan scheelite-bearing ores. (Report of investigations / United States Department of the Interior, Bureau of Mines; 9251) Bibliography: p. -
Isamill™ Uses Horizontal Milling to Secure Better Energy Efficiency
IsaMill™ uses horizontal milling to secure better energy effi ciency, product size and availability with a 25% capital-back performance guarantee. IsaMill’s horizontal configuration means it’s completely different from other mills. IsaMill™ gives me an increased recovery that outweighs the cost. I never have to worry about the mill.” – Amandelbult Operation, Anglo American Flowsheet improvements for the real world IsaMill™ at a glance > Real-world success in 130 metalliferous installations across 21 countries since launching in 1994 > World’s only horizontal fine grinding mill, it avoids short-circuits and gives the highest availability > Most efficient fine grinding mill in the world > Strongest performance guarantee in the world > Most consistent product size > Delivers better results to downstream flotation and leaching For more: [email protected] Tel +61 7 3833 8500 IsaMill™ 1 IsaMill™ is the most effi cient and reliable grinding mill available and with 130 metalliferous installations in 21 countries it has a proven record in the real world. The IsaMill™ reduces the energy, media and capital costs of grinding. It’s incredibly effi cient and intense. It focuses only on the particles that need grinding. The IsaMill™ produces greater power vertical mill. It’s easy to operate and it The IsaMill™ is currently available in the intensity than ball or tower mills. maximises availability. following models, named for their net grinding volume: Today’s IsaMill™ is also light. A modest The IsaMill™ gives an accurate and volume of concrete and structural steel rapid scale up, so it’s predictable • M1000 (355–500kW)* are used, and the entire unit sits on a and reliable.