New Approaches for Extracting and Recovering Metals from Mine Tailings ⇑ Carmen Falagán , Barry M
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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. -
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. -
Back Ground of Gold Leaching Reagent ---Florrea Goldix
SHENYANG FLORREA CHEMICALS CO., LTD 1719, BLD B,Hai‐li‐de Mansion,NO.135,ChangJiang Street, Huanggu District, Shenyang, Liaoning Province, P. R . China Tel: 0086 24 31515191 Mobile: 0086 136 0982 1616 Fax: 0086 24 31513277 Skype: yang(florrea) ISO 9001 Certified NO. : 086911Q E‐mail: [email protected] www.florrea.com MSN: [email protected] ‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐ BACK GROUND OF GOLD LEACHING REAGENT -----FLORREA GOLDIX 567 (Excellent Cyanide Replacement , Environmentally friendly) Florrea Gold Lixiviant GOLDIX 567‐‐‐ Environmentally friendly Gold Leaching without cyanide. The various oxidized gold ore were leached with various lixiviants and Florrea Goldix 567 is the best lixiviant substitute for cyanide as gold lixiviant at present, meanwhile gole leaching speeds with organic chlorine C was 8 times of that with cyanide Gold cyanidation, also called cyanide leaching, is a metallurgical technique for extracting gold from low‐grade ore by converting the gold to a water soluble coordination complex. It is the most commonly used process for gold extraction. Due to the highly poisonous nature of cyanide, the process is controversial and its usage is banned in a number of countries and territories. It uses cyanide to dissolve the gold within the rock, which, itself, is not soluble in cyanide. The gold is then drawn out in a liquid form that can be treated to remove the cyanide. Almost 90% of all gold extracted commercially is done so by cyanidation. The process has been controversial since its inception due to the poisonous nature of cyanide and the threat it poses to the environment and the people working in the extraction facilities. -
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. -
Background for Nepa Reviewers: Non-Coal Mining Operations
EPA/530//R-95/043 NTIS/PB96/109/103 TECHNICAL DOCUMENT BACKGROUND FOR NEPA REVIEWERS: NON-COAL MINING OPERATIONS December 1994 U.S. Environmental Protection Agency Office of Solid Waste Special Waste Branch 401 M Street, SW Washington, DC 20460 Disclaimer and Acknowledgements This document was prepared by the U.S. Environmental Protection Agency (EPA). The mention of company or product names is not to be considered an endorsement by the U.S. Government or by the EPA. This Technical Document consists of nine sections. The first is EPA's overview of mining and the statutory and regulatory background. That is followed by a description of mining activities and their potential environmental impacts. The remaining sections cover specific environmental concerns, environmental monitoring, and pollution prevention. Also provided are a list of contacts, glossary, and references. This report was distributed for review to the U.S. Department of the Interior's Bureau of Mines, Bureau of Land Management, and National Park Service; the U.S. Department of Agriculture's Forest Service; Western Governors Association; and other industry and public interest groups. The use of the terms "extraction," "beneficiation," and "mineral processing" is not intended to classify any waste stream for the purposes of regulatory interpretation or application. Rather, these terms are used in the context of common industry terminology. Background for NEPA Reviewers TABLE OF CONTENTS Page INTRODUCTION ..................................................................1-1 -
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 -
Recovery of Gold and Iron from Cyanide Tailings with a Combined Direct Reduction Roasting and Leaching Process
metals Article Recovery of Gold and Iron from Cyanide Tailings with a Combined Direct Reduction Roasting and Leaching Process Pingfeng Fu 1,2,* ID , Zhenyu Li 1, Jie Feng 1 and Zhenzhong Bian 1 1 School of Civil and Resources Engineering, University of Science and Technology Beijing, Beijing 100083, China; [email protected] (Z.L.); [email protected] (J.F.); [email protected] (Z.B.) 2 Key Laboratory of High-Efficient Mining and Safety of Metal Mines, Ministry of Education, Beijing 100083, China * Correspondence: [email protected]; Tel.: +86-10-6233-2902 Received: 25 June 2018; Accepted: 19 July 2018; Published: 21 July 2018 Abstract: Cyanide tailings are the hazardous waste discharged after gold cyanidation leaching. The recovery of gold and iron from cyanide tailings was investigated with a combined direct reduction roasting and leaching process. The effects of reduction temperature, coal dosage and CaO dosage on gold enrichment into Au-Fe alloy (FexAu1−x) were studied in direct reduction roasting. Gold containing iron powders, i.e., Au-Fe alloy, had the gold grade of 8.23 g/t with a recovery of 97.46%. After separating gold and iron in iron powders with sulfuric acid leaching, ferrous sulfate in the leachate was crystallized to prepare FeSO4·7H2O with a yield of 222.42% to cyanide tailings. Gold enriched in acid-leaching residue with gold grade of 216.58 g/t was extracted into pregnant solution. The total gold recovery of the whole process reached as high as 94.23%. The tailings generated in the magnetic separation of roasted products, with a yield of 51.33% to cyanide tailings, had no toxic cyanide any more. -
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 ............................................................................................................... -
Addressing the Information Gaps on Prices of Minerals Sold in an Intermediate Form
The Platform for Cooperation on Tax DISCUSSION DRAFT: Addressing the Information Gaps on Prices of Minerals Sold in an Intermediate Form Feedback Period 24 January 2017 – 21 February 2017 Organisation for Economic Co-operation and Development (OECD) World Bank Group (WBG) International Monetary Fund (IMF) United Nations (UN) 1 This discussion draft has been prepared in the framework of the Platform for Collaboration on Tax by the OECD, under the responsibility of the Secretariats and Staff of the four mandated organisations. The draft reflects a broad consensus among these staff, but should not be regarded as the officially endorsed views of those organisations or of their member countries. 1 Table of Contents Introduction................................................................................................................................................................ 6 Domestic Resource Mobilisation from Mining......................................................................................... 6 Report Structure ................................................................................................................................................... 9 Building An Understanding of the Mining Sector – A Methodology ................................................ 10 Introduction ........................................................................................................................................................ 10 Steps in the Methodology ........................................................................................................................... -
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. -
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.