Processing Tests, Adjusted Cost Models and the Economies of Reprocessing Copper Mine Tailings in Chile
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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. -
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 -
Treatment and Microscopy of Gold
TREATMENT AND MICROSCOPY OF GOLD AND BASE METAL ORES. (Script with Sketches & Tables) Short Course by R. W. Lehne April 2006 www.isogyre.com Geneva University, Department of Mineralogy CONTENTS (Script) page 1. Gold ores and their metallurgical treatment 2 1.1 Gravity processes 2 1.2 Amalgamation 2 1.3 Flotation and subsequent processes 2 1.4 Leaching processes 3 1.5 Gold extraction processes 4 1.6 Cyanide leaching vs. thio-compound leaching 5 2. Microscopy of gold ores and treatment products 5 2.1 Tasks and problems of microscopical investigations 5 2.2 Microscopy of selected gold ores and products 6 (practical exercises) 3. Base metal ores and their beneficiation 7 3.1 Flotation 7 3.2 Development of the flotation process 7 3.3 Principles and mechanisms of flotation 7 3.4 Column flotation 9 3.5 Hydrometallurgy 10 4. Microscopy of base metal ores and milling products 10 4.1 Specific tasks of microscopical investigations 11 4.2 Microscopy of selected base metal ores and milling products 13 (practical exercises) 5. Selected bibliography 14 (Sketches & Tables) Different ways of gold concentration 15 Gravity concentration of gold (Agricola) 16 Gravity concentration of gold (“Long Tom”) 17 Shaking table 18 Humphreys spiral concentrator 19 Amalgamating mills (Mexican “arrastra”, Chilean “trapiche”) 20 Pressure oxidation flowsheet 21 Chemical reactions of gold leaching and cementation 22 Cyanide solubilities of selected minerals 23 Heap leaching flowsheet 24 Carbon in pulp process 25 Complexing of gold by thio-compounds 26 Relation gold content / amount of particles in polished section 27 www.isogyre.com Economically important copper minerals 28 Common zinc minerals 29 Selection of flotation reagents 30 Design and function of a flotation cell 31 Column cell flotation 32 Flowsheet of a simple flotation process 33 Flowsheet of a selective Pb-Zn flotation 34 Locking textures 35 2 1. -
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 ........................................................................................................................... -
Xstrata Technology Update Edition 13 – April 2012 Building Plants That Work
xstrata technology update Edition 13 – April 2012 Building plants that work You have to get a lot of things it takes another operator to get them right to build a plant that works. right. Someone who has lived through the problems, had to do the maintenance, operated during a midnight power Of course the big picture must be right – doing the right project, in the right place, failure, cleaned up the spill. Someone at the right time. who has “closed the loop” on previous designs; lived with previous decisions After that, the devil is in the detail. You and improved them, over and over. need a sound design, good execution, good commissioning, and ongoing This is why Xstrata Technology provides support after commissioning. You need a technology “package”. Just as a car to operate and maintain your plant in is more than an engine, technology is the long run, long after the construction more than a single piece of equipment. company has left. That’s when all the Technology is a system. All the elements “little” details become important – how of the system have to work with each easy is it to operate, how good is the other and with the people in the plant. maintenance access, what happens in We want our cars designed by people a power failure, where are the spillage who love cars and driving. So should points and how do we clean them our plants be designed by people with up? Are the instruments reliable and experience and passion to make each is the process control strategy robust one work better than the last. -
Copper Recovery Using Leach/Solvent Extraction/Electrowinning Technology
Copper recovery using leach/solvent extraction/electrowinning technology: Forty years of innovation, 2.2 million tonnes of copper annually by G.A. Kordosky* small scale in analytical chemistry3 and on a large scale for the recovery of uranium from Synopsis sulphuric acid leach solutions4. Generally Mills had already developed and commercialized The concept of selectively extracting copper from a low-grade dump Alamine® 336 as an SX reagent for the leach solution followed by stripping the copper into an acid recovery of uranium from sulphuric acid leach solution from which electrowon copper cathodes could be produced liquors5 and believed that a similar technology occurred to the Minerals Group of General Mills in the early 1960s. for copper recovery would be welcome. This simple, elegant idea has resulted in a technology by which However, an extensive market survey showed about 2.2 million tonnes of high quality copper cathode was produced in year 2000. The growth of this technology is traced over that the industry reception for copper recovery time with a discussion of the key plants, the key people and the by L/SX/EW technology was almost hostile. important advances in leaching, plant design, reagents and The R&D director of a large copper producer electrowinning that have contributed to the growth of this predicted at an AIME annual meeting that technology. Some thoughts on potential further advances in the there would never be a pound of copper technology are also given. recovered using solvent extraction and his comment prompted -
Pretreatment of Copper Ore Prior to Heap Leaching Includes Crushing and Agglomeration Processes Which Were Studied in This Thesis Research
PRETREATMENT OF COPPER ORE PRIOR TO HEAP LEACHING by Phanindra Kodali A thesis submitted to the faculty of The University of Utah in partial fulfillment of the requirements for the degree of Master of Science Department of Metallurgical Engineering The University of Utah August 2010 Copyright Phanindra Kodali 2010 All Rights Reserved The University of Utah Graduate School STATEMENT OF THESIS APPROVAL The thesis of Phanindra Kodali has been approved by the following supervisory committee members: Jan D. Miller , Chair 11113/2009 Chen-Luh Lin , Member 11113/2009 Xuming Wang , Member 11113/2009 Michael S. Moats . Member 11113/2009 and by Jan D. Miller , Chair of the Department of Metallurgical Engineering and by Charles A. Wight, Dean of The Graduate School. ABSTRACT Pretreatment of copper ore prior to heap leaching includes crushing and agglomeration processes which were studied in this thesis research. Crushing is a high energy consuming process. In mining operations generally jaw and gyratory crushers are used for primary crushing and cone crushers are used for secondary crushing. During the past couple of decades High Pressure Grinding Roll (HPGR) crushers are being considered by mining companies due to lower energy consumption. In the present research copper ores (copper oxide and copper sulfide ores) were crushed by a jaw crusher and by HPGR and the products evaluated for particle damage, as well as by column leaching to determine the rate and extent of copper recovery. X-ray computed tomography analysis and laboratory column leaching experiments on copper oxide samples revealed that products from HPGR crushing have more particle damage and higher copper recoveries when compared with products from jaw crusher crushing. -
In-Situ Chromium and Vanadium Recovery of Landfilled Ferrochromium
Chemical Engineering Journal 303 (2016) 359–368 Contents lists available at ScienceDirect Chemical Engineering Journal journal homepage: www.elsevier.com/locate/cej In-situ chromium and vanadium recovery of landfilled ferrochromium and stainless steel slags ⇑ Jeroen Spooren a, , Eunyoung Kim a,b, Liesbeth Horckmans a, Kris Broos a, Peter Nielsen a, Mieke Quaghebeur a a VITO – Flemish Institute for Technological Research, Boeretang 200, B-2400 Mol, Belgium b Department of Bioengineering, University of Antwerp, Groenenborgerlaan 171, B-2020 Antwerp, Belgium highlights NaOCl assisted alkaline heap leaching of Cr and V from slags was investigated. The matrix material of stainless steel slag and ferrochromium slag remains intact. 11–19% Cr and 7.0–7.5% V were leached selectively after 64 days. A model shows that Cr will leach for 4–5 years at chosen heap leaching conditions. Cr and V extraction potentially improves the slags’ environmental quality. article info abstract Article history: A novel heap leaching method was investigated for selective removal of chromium (Cr) and vanadium (V) Received 26 March 2016 from ferrochromium (FeCr) and stainless steel (SS) slags. In particular, alkaline oxidative heap leaching Received in revised form 25 May 2016 was simulated on lab-scale by batch and column leaching tests. The results show a selective leaching Accepted 26 May 2016 of Cr (11–19%) and V (7.0–7.5%) after 64 days of column leaching, with a very low dissolution (<2.2% Available online 27 May 2016 (FeCr slag) and <0.15% (SS slag)) of matrix elements (e.g. Al, Fe, Si, Mg, Ca), when NaOCl is applied as oxi- dation agent and NaOH as alkaline agent. -
Biooxidation of a Gold Bearing Arsenopyrite/Pyrite Cencentrate
.... r BIOOXIDATION OF A GOLD BEARING ARSENOPYRITE/PYRITE CONCENTRATE by D.M. MILLER B. Sc. Eng (UNIVERSITY OF THE WI1WATERSRAND).1984 University of Cape Town Submitted to the University of Cape Town in fulfilment of the requirements for the degree of Masters of Science in Engineering February 1990 The University of Cape Town has been given the right to reproduce this ti.esi3 in whole or In part. Copyright is he!(! Ly the author. The copyright of this thesis vests in the author. No quotation from it or information derived from it is to be published without full acknowledgement of the source. The thesis is to be used for private study or non- commercial research purposes only. Published by the University of Cape Town (UCT) in terms of the non-exclusive license granted to UCT by the author. University of Cape Town i ABSTRACT Biooxidation of gold bearing refractory sulphide concentrates is emerging as a viable alternative to roasting and pressure oxidation as the procedure where by gold liberation is achieved. Agitated, aerated bioreactors are required for rapid oxidation; hence the need for the development of a kinetic model where by results obtained by batch and small scale testwork are interpreted and the performance of biooxidation reactors can be predicted and which facilitates reactor design and scale-up Many models have been proposed to describe biooxidation, predicting either bacterial growth in the system, or the rate of sulphide mineral oxidation. Of these, only one, incorporating the empirical logistic equation to describe the rate of sulphide oxidation, (Pinches et al., 1987), was found to include rate parameters useful for design and scale-up purposes. -
Principles of Extractive Metallurgy
Principles of Extractive Metallurgy by Professor Nosa O. Egiebor Environmental Engineering Program Department of Chemical Engineering Tuskegee University Tuskegee, AL 36088 USA Course Reference Texts Materials for the course were taken from multiple textbook. The main texts include: Principles of Extractive Metallurgy by Terkel Rosenquist; Tapir Academic Press, Trondheim, Norway, 2004. The Chemistry of Gold Extraction (2nd Ed) by John O. Marsden and C. Lain House, SME Littleton, Colorado, USA (2006) Process Selection in Extractive Metallurgy by Peter Hayes, Hayes Publishing Co., Brisbane, Australia (1985) Instructor’s Lecture Notes, Prof. Nosa O. Egiebor (2011) Introduction - Definitions Metallurgy is the science of extracting and refining metals from ores and the compounding of metals to form alloys. Extractive metallurgy is the branch of metallurgical science & engineering which deals with the extraction and refining of metals from ores. An ore is a rock that contains commercially viable amounts of metallic/non-metallic solid minerals. Ores are complex associations of mineral grains A mineral is a chemical compound that constitute a component of an ore, and with its own characteristic chemical composition. Introduction – Types of Ores & Minerals Most metals are combined with other elements to form minerals. Few exist as pure metals. The table below provides examples of the common types of ores with minerals, their chemical formula and Common Names: Native Metals (Can occur as Pure Metals) Silver-(Ag), Gold-(Au), Bismuth-(Bi), -
Study of the Calcination Process of Two Limonitic Iron Ores Between 250 °C and 950 °C
Lisbeth Longa-Avello - Cristina Pereyra-Zerpa - Julio Andrés Casal-Ramos - Pedro Delvasto Study of the calcination process of two limonitic iron ores between 250 °C and 950 °C Estudio del proceso de calcinación en dos minerales de hierro limoníticos entre 250 °C y 950 °C Estudo do processo de calcinação em dois minerais de ferro limoníticos entre 250 °C e 950 °C Lisbeth Longa-Avello* Cristina Pereyra-Zerpa** Fecha de recepción: 20 de septiembre de 2016 Julio Andrés Casal-Ramos*** Fecha de aprobación: 20 de marzo de 2017 Pedro Delvasto**** Abstract The dehydration process of two limonitic ores from Venezuela was studied between 250 °C and 950 °C by means of thermogravimetry, infrared spectroscopy, and x-ray diffraction. These techniques indicated for both minerals that the goethite-to-hematite transformation occurred in the range of 250-350 °C. In addition, the x-ray diffraction showed a structural re-arrangement within the orebody above 350 °C, temperature above which only the hematite structure is recognizable. Finally, infrared spectroscopy revealed that such transformation implies the loss of structural OH- functional groups, characteristic of the limonite. Keywords: Iron Ore; Limonite; Thermal Modification of Minerals. Resumen Se estudió el proceso de deshidratación de dos minerales limoníticos de Venezuela entre 250 °C y 950 °C, usando termogravimetría, espectroscopia infrarroja y difracción de rayos x. Para ambos materiales, estas técnicas indicaron que la transformación de goethita a hematita ocurrió en el rango de 250 °C a 350 °C. Adicionalmente, la difracción de rayos X mostró un rearreglo estructural dentro de la mena a una temperatura por encima de 350 °C; a temperaturas mayores, solo se reconoce la estructura de la hematita.