Feasibility Study on Physical Beneficiation of Low-Grade PGM Flotation Tailings Using Spiral Classifiers and Enhanced Gravity Separators

Total Page:16

File Type:pdf, Size:1020Kb

Feasibility Study on Physical Beneficiation of Low-Grade PGM Flotation Tailings Using Spiral Classifiers and Enhanced Gravity Separators 2nd International Conference on Trends in Industrial and Mechanical Engineering (ICTIME'2013) Sept 17-18, 2013 Hong Kong Feasibility Study on Physical Beneficiation of Low-Grade PGM Flotation Tailings using Spiral Classifiers and Enhanced Gravity Separators J. Siame, and H. Kasaini and chemical processes are used to extract the desired product Abstract— A study on physical beneficiation of platinum group from the run of the mine ore and produce a waste stream metals (PGMs) flotation tailings was carried out by means of spiral known as tailings. This process of product extraction is never classifiers and a gravity separator (Knelson Concentrator – KC-CVD 100% efficient, nor is it possible to reclaim all reusable and 6 unit). The economic mineral reserves for PGMs are found in the expended processing reagents and chemicals. The Busheveld Complex geological formation of South Africa unrecoverable and uneconomic metals, minerals, chemicals, particularly in the narrow strata of Merensky Reef, (Platreef) and the organics and process water are discharged, normally as slurry, UG2 chromitite layer. In addition, there are about 450 million tonnes to a final storage area commonly known as a Tailings of mine waste material (tailings and smelter slags) across the platinum industry which contains sufficient PGMs for economic Management Facility (TMF). exploitation. The major minerals in UG2 flotation tailings are Tailings are generally stored on the surface either within chromite {FeCr2O4, S.G = 4.5 – 4.8}, orthopyroxene {(Mg, retaining structures or in the form of piles (dry stacks) but can Fe)2Si2O6, S.G = 3.2 – 3.9} and plagioclase {Na0.5Ca0.5Si3AlO8, also be stored underground in mined out voids by a process S.G = 2.6 – 2.8} with small amounts of talc {Mg3Si4O10(OH)2, S.G commonly referred to as backfill [1]. = 2.7 – 2.8} and clay minerals (chlorites/phlogopite, S.G = 2.2 – The challenges associated with tailings storage are ever 2.75). PGMs in flotation tailings are either associated with silicates increasing. Advances in technology allow lower grade ores to (60%) or are free PGMs particles (10%) while 30% of them are be exploited, generating higher volumes of waste that require associated with sulphide minerals (pentlandite, chalcopyrite, safe storage. Environmental regulations are also advancing, pyrrhotite pyrite and millerite). On the basis of mineralogical data, about 70% of total PGMs associated with silicates and native alloys placing more stringent requirements on the mining industry, can be separated from oxide and sulphide minerals using gravity particularly with regard to tailings storage practices. This separators. This was confirmed by results from the spiral classifier ultimately places added pressure on the operators of a tailings and Knelson Concentrator where 71% of total PGMs were recovered facility who carry out the day to day roles of tailings discharge to the tailings (lighter fraction) and the overall grade of PGMs and water management [2]. increased from 0.75 g/t to 1.07 g/t. The highest amount of palladium The economic benefits of physical beneficiation of ores to be transferred from the feed solids (10 kg) to tailings (5 kg) was include the reduction of the impact on the environment, capital about 84%. The optimum conditions for operating a Knelson and operational expenditures which are often associated with Concentrator (KC-CVD 6) and spiral with regards to PGMs extractive metallurgical operations (concentrators, roasting, beneficiation are discussed further in this study. Even though the feed solids to the KC-CVD 6 gravity separator were deslimed, its capacity smelting, leaching and purification of solutions). Furthermore, to upgrade PGMs from 0.7 g/t to 1.11 g/t at an average recovery of physical beneficiation can be applied to reduce the carbon 71% compared well with the results from a spiral classifier where the print of a mining firm by scaling down its dependence on fines remained part of the feed. The recovery of PGMs by gravity chemicals, energy and water for extracting minerals. In separation was about 75% at an upgrade ratio of 1.8. general, physical pre-treatment of low grade ores is necessary for reducing the total mass of reagent-consuming minerals and Keywords— Beneficiation, Classifier, Gravity Separation, other gangue minerals in order to improve metallurgical plant Knelson Concentrator, Platinum, Spiral Classifier, UG2 Tailings. efficiency and productivity. There are over 450 million tonnes of flotation tailings and I. INTRODUCTION smelter slags containing appreciable amounts of PGMs in AILINGS consist of ground rock and process effluents South Africa. This is a huge resource for secondary PGMs. that are generated in a mine processing plant. Mechanical Several researchers have carried out feasibility studies of T recovering PGMs (often associated with gold) by recycling the tailings back to the flotation banks or by lixiviation with J. Siame is with the Copperbelt University, School of Mines and Mineral Sciences, Department of Chemical Engineering, P.O. Box 21692, Kitwe, HCl/H2SO4 acid [3]. The average grade of total PGMs in Zambia. (Phone: +260 969 206022; Fax: +260 212 228212; tailings vary from one mining firm to another. The average E-mail: [email protected]). PGM recoveries on concentrator feed solids vary between 80 H. Kasaini is with Rare Element Resources Corporation, Denver, USA. and 88% across the industry and depending on the feed grade (E-mail: [email protected]). 46 2nd International Conference on Trends in Industrial and Mechanical Engineering (ICTIME'2013) Sept 17-18, 2013 Hong Kong (4–8 g/t); the final flotation tailings may contain significant Table II illustrates the mineralogical profile of UG2 amounts of PGMs (0.7–1.6 g/t). In the past three decades, flotation tailings which contain about 0.7 g/t, total PGMs PGM losses to flotation tailings were very high mainly (Northam Platinum Ltd.). The most floated PGMs are because there were no reliable analytical tools to verify the associated with metal oxides and sulphides while PGMs PGM assays in concentrator tailings until the mini enclosed or attached to silicates are lost to the tailings together laparoscopy-assisted (MLA) technique was introduced to the with significant amount of free PGM particles [7]. platinum industry. Therefore, stockpiles of flotation tailings On the basis of mineralogical data shown in Table II, about constitute an important secondary resource of PGMs for the 57% of total PGMs in flotation tailings are attached or global market. But, beneficiation of PGM tailings by further enclosed in silicates while 13% of total PGMs are associated flotation has limited benefits since only about 30% of PGMs with native minerals. Both silicates and native minerals are are associated with base-metal sulphides and the rest are either lighter minerals compared to metal oxides and sulphides and inclusions or attached to clay minerals, with a small fraction therefore physical separation of these minerals is possible being free or native minerals of PGMs. Fine grinding is under optimized granulometric conditions. Therefore, about required to liberate the PGMs which are locked in either 70% of total PGMs can be transferred to lighter minerals chromite matrix or silicates [4]. Owing to the mineral hardness resulting in PGMs upgrade. The extent of the upgrade ratio of silicates and chromite (5–6 Mohs scale) energy depends on the partition coefficient of solids. consumption in the milling process is expected to be high. Further milling of the heavier minerals from the gravity The mineralogical profile of PGM feed solids to the separators may be necessary to liberate 30% of PGMs which concentrators is illustrated in Table I along with PGMs which are associated or attached to metal sulphides or the heavy are associated with or attached / enclosed in 25% oxide, 12% minerals (almost silica or clay free minerals) may be subjected silicate, 36% sulphide or 27% native minerals. Mineralogical to froth flotation in order to recover PGMs [8], [9]. data on UG2 samples was generated by means of MLA technique. The UG2 samples are flotation tailings from the TABLE II Northam Platinum Limited plant operations in South Africa. MINERALOGICAL DATA ON UG2 TAILINGS. Complete recovery of PGMs which are locked in silicates, Minerals PGM Distribution Oxides Enclosed 2% native minerals and chromite matrix is difficult. Therefore, Silicates Association 25% most of the PGMs in flotation tailings are attached or enclosed Attached 21% in silicates [5], [6]. Enclosed 11% Sulphides Association 26% Attached 2% TABLE I Enclosed 2% MINERALOGICAL DATA ON UG2 FEED SOLIDS TO THE CONCENTRATOR. Free or Native Minerals Free 13% Chemical Formula S.G PGMs Oxide Chromite FeO.Cr2O3 4.7 Attached/Enclosed In this study, the KC-CVD was used to treat rougher Minerals (25%) flotation tailings that were pretreated by desliming (removal of Silicate Orthopyroxene (Mg, Fe) 2Si 2O6 3.5 Attached/Enclosed –45 µm fractions) using a spiral classifier. The final tailings Minerals (12%) from the spiral classifier (less heavy minerals) were transferred to the pilot enhanced gravity separator at a flow Plagioclase Na 0.5Ca0.5 Si 3AlO 8 2.7 rate of 1.69 m3/hr. Talc Mg3Si 4O10 (OH)2 2.7 The rationale of the concept of upgrading PGMs in flotation tailings lies in the fact that a decrease in chromite Chlorites X4-6Y4O10(OH,O)8 2.4 minerals (heavier and abundant) will almost invariably lead to an upgrade of PGMs. Chromites are almost not physically or phlogopite KMg AlSi O F(OH) 2.8 3 3 10 chemically associated with PGMs in tailings. Sulphide Pentlandite (Fe, Ni)9S8 4.8 Association In industry, gravity separation units are classified Minerals (3%) according to the average particle size of the feed; fine solids Chalcopyrite CuFeS 2 4.2 Attached/Enclosed (40 - 75 µm) require units that permit settling of particles in a (33%) fluid media under a centrifugal force (Knelson Concentrator, Pyrrhotite Fe(1 - x)S; 4.5 Kelsey, Falcon).
Recommended publications
  • Contents 2009
    INNEHÅLLSFÖRTECKNING/CONTENTS Page Forssberg, Eric, Luleå University of Technology Energy in mineral beneficiation 1 Acarkan N., Kangal O., Bulut G., Önal G. Istanbul Technical University The comparison of gravity separation and flotation of gold and silver bearing ore 3 Ellefmo, Steinar & Ludvigsen, Erik, Norwegian University of Science and Technology Geological Modelling in a Mineral Resources Management Perspective 15 Hansson, Johan, Sundkvist, Jan-Eric, Bolin, Nils Johan, Boliden Mineral AB A study of a two stage removal process 25 Hulthén, Erik & Evertsson, Magnus, Chalmers University of Technology Optimization of crushing stage using on-line speed control on a cone crusher 37 Hooey1, P.L., Spiller2, D.E, Arvidson3, B.R., Marsden4, P., Olsson5, E., 1MEFOS, 2Eric Spiller Consultants LLC, 3Bo Arvidson Consulting LLC, 4, 5Northland Resources Inc. Metallurgical development of Northland Resources' IOCG resources 47 Ikumapayi, Fatai K., Luleå University of Technology, Sundkvist, Jan-Eric & Bolin, Nils-Johan, Boliden Mineral AB Treatment of process water from molybdenum flotation 65 Johansson, Björn, Boliden Mineral AB Limitations in the flotation process 79 Kongas, Matti & Saloheimo, Kari, Outotec Minerals Oy New innovations in on-stream analysis for flotation circuit management and control 89 Kuyumcu, Halit Z. & Rosenkranz, Jan, TU Berlin Investigation of Fluff Separation from Granulated Waste Plastics to be Used in 99 Blast Furnace Operation Mickelsson1, K-O, Östling2 J, Adolfsson3, G., 1LKAB Malmberget, 2Optimation AB Luleå, 3LKAB Kiruna
    [Show full text]
  • National Instrument 43-101 Technical Report
    ASANKO GOLD MINE – PHASE 1 DEFINITIVE PROJECT PLAN National Instrument 43-101 Technical Report Prepared by DRA Projects (Pty) Limited on behalf of ASANKO GOLD INC. Original Effective Date: December 17, 2014 Amended and Restated Effective January 26, 2015 Qualified Person: G. Bezuidenhout National Diploma (Extractive Metallurgy), FSIAMM Qualified Person: D. Heher B.Sc Eng (Mechanical), PrEng Qualified Person: T. Obiri-Yeboah, B.Sc Eng (Mining) PrEng Qualified Person: J. Stanbury, B Sc Eng (Industrial), Pr Eng Qualified Person: C. Muller B.Sc (Geology), B.Sc Hons (Geology), Pr. Sci. Nat. Qualified Person: D.Morgan M.Sc Eng (Civil), CPEng Asanko Gold Inc Asanko Gold Mine Phase 1 Definitive Project Plan Reference: C8478-TRPT-28 Rev 5 Our Ref: C8478 Page 2 of 581 Date and Signature Page This report titled “Asanko Gold Mine Phase 1 Definitive Project Plan, Ashanti Region, Ghana, National Instrument 43-101 Technical Report” with an effective date of 26 January 2015 was prepared on behalf of Asanko Gold Inc. by Glenn Bezuidenhout, Douglas Heher, Thomas Obiri-Yeboah, Charles Muller, John Stanbury, David Morgan and signed: Date at Gauteng, South Africa on this 26 day of January 2015 (signed) “Glenn Bezuidenhout” G. Bezuidenhout, National Diploma (Extractive Metallurgy), FSIAMM Date at Gauteng, South Africa on this 26 day of January 2015 (signed) “Douglas Heher” D. Heher, B.Sc Eng (Mechanical), PrEng Date at Gauteng, South Africa on this 26 day of January 2015 (signed) “Thomas Obiri-Yeboah” T. Obiri-Yeboah, B.Sc Eng (Mining) PrEng Date at Gauteng, South Africa on this 26 day of January 2015 (signed) “Charles Muller” C.
    [Show full text]
  • Stillwater Mine, 45°23'N, 109°53'W East Boulder Mine, 45°30'N, 109°05'W
    STILLWATER MINING COMPANY TECHNICAL REPORT FOR THE MINING OPERATIONS AT STILLWATER MINING COMPANY STILLWATER MINE, 45°23'N, 109°53'W EAST BOULDER MINE, 45°30'N, 109°05'W (BEHRE DOLBEAR PROJECT 11-030) MARCH 2011 PREPARED BY: MR. DAVID M. ABBOTT, JR., CPG DR. RICHARD L. BULLOCK, P.E. MS. BETTY GIBBS MR. RICHARD S. KUNTER BEHRE DOLBEAR & COMPANY, LTD. 999 Eighteenth Street, Suite 1500 Denver, Colorado 80202 (303) 620-0020 A Member of the Behre Dolbear Group Inc. © 2011, Behre Dolbear Group Inc. All Rights Reserved. www.dolbear.com Technical Report for the Mining Operations at Stillwater Mining Company March 2011 TABLE OF CONTENTS 3.0 SUMMARY ..................................................................................................................................... 1 3.1 INTRODUCTION .............................................................................................................. 1 3.2 EXPLORATION ................................................................................................................ 1 3.3 GEOLOGY AND MINERALIZATION ............................................................................ 2 3.4 DRILLING, SAMPLING METHOD, AND ANALYSES ................................................. 3 3.5 RESOURCES AND RESERVES ....................................................................................... 3 3.6 DEVELOPMENT AND OPERATIONS ........................................................................... 5 3.6.1 Mining Operation ..................................................................................................
    [Show full text]
  • Gravity Concentration in Artisanal Gold Mining
    minerals Review Gravity Concentration in Artisanal Gold Mining Marcello M. Veiga * and Aaron J. Gunson Norman B. Keevil Institute of Mining Engineering, University of British Columbia, Vancouver, BC V6T 1Z4, Canada; [email protected] * Correspondence: [email protected] Received: 21 September 2020; Accepted: 13 November 2020; Published: 18 November 2020 Abstract: Worldwide there are over 43 million artisanal miners in virtually all developing countries extracting at least 30 different minerals. Gold, due to its increasing value, is the main mineral extracted by at least half of these miners. The large majority use amalgamation either as the final process to extract gold from gravity concentrates or from the whole ore. This latter method has been causing large losses of mercury to the environment and the most relevant world’s mercury pollution. For years, international agencies and researchers have been promoting gravity concentration methods as a way to eventually avoid the use of mercury or to reduce the mass of material to be amalgamated. This article reviews typical gravity concentration methods used by artisanal miners in developing countries, based on numerous field trips of the authors to more than 35 countries where artisanal gold mining is common. Keywords: artisanal mining; gold; gravity concentration 1. Introduction Worldwide, there are more than 43 million micro, small, medium, and large artisanal miners extracting at least 30 different minerals in rural regions of developing countries (IGF, 2017) [1]. Approximately 20 million people in more than 70 countries are directly involved in artisanal gold mining (AGM), with an estimated gold production between 380 and 450 tonnes per annum (tpa) (Seccatore et al., 2014 [2], Thomas et al., 2019 [3], Stocklin-Weinberg et al., 2019 [4], UNEP, 2020 [5]).
    [Show full text]
  • On the Association of Palladium-Bearing Gold, Hematite and Gypsum in an Ouro Preto Nugget
    473 The Canadian Mineralogist Vol. 41, pp. 473-478 (2003) ON THE ASSOCIATION OF PALLADIUM-BEARING GOLD, HEMATITE AND GYPSUM IN AN OURO PRETO NUGGET ALEXANDRE RAPHAEL CABRAL§ AND BERND LEHMANN Institut für Mineralogie und Mineralische Rohstoffe, Technische Universität Clausthal, Adolph-Roemer-Str. 2A, D-38678 Clausthal-Zellerfeld, Germany ROGERIO KWITKO-RIBEIRO§ Centro de Desenvolvimento Mineral, Companhia Vale do Rio Doce, Rodovia BR 262/km 296, Caixa Postal 09, 33030-970 Santa Luzia – MG, Brazil RICHARD D. JONES 1636 East Skyline Drive, Tucson, Arizona 85178, U.S.A. ORLANDO G. ROCHA FILHO Mina do Gongo Soco, Companhia Vale do Rio Doce, Fazenda Gongo Soco, Caixa Postal 22, 35970-000 Barão de Cocais – MG, Brazil ABSTRACT An ouro preto (black gold) nugget from Gongo Soco, Minas Gerais, Brazil, has a mineral assemblage of hematite and gypsum hosted by Pd-bearing gold. The hematite inclusion is microfractured and stretched. Scattered on the surface of the gold is a dark- colored material that consists partially of Pd–O with relics of palladium arsenide-antimonides, compositionally close to isomertieite and mertieite-II. The Pd–O coating has considerable amounts of Cu, Fe and Hg, and a variable metal:oxygen ratio, from O-deficient to oxide-like compounds. The existence of a hydrated Pd–O compound is suggested, and its dehydration or deoxygenation at low temperatures may account for the O-deficient Pd-rich species, interpreted as a transient phase toward native palladium. Although gypsum is a common mineral in the oxidized (supergene) zones of gold deposits, the hematite–gypsum- bearing palladian gold nugget was tectonically deformed under brittle conditions and appears to be of low-temperature hydrother- mal origin.
    [Show full text]
  • The Geological Occurrence, Mineralogy, and Processing by Flotation of Platinum Group Minerals (Pgms) in South Africa and Russia
    minerals Review The Geological Occurrence, Mineralogy, and Processing by Flotation of Platinum Group Minerals (PGMs) in South Africa and Russia Cyril O’Connor 1,* and Tatiana Alexandrova 2 1 Department of Chemical Engineering, Centre for Minerals Research, University of Cape Town, Cape Town 7701, South Africa 2 Department of Minerals Processing, St Petersburg Mining University, St Petersburg 199106, Russia; [email protected] * Correspondence: [email protected] Abstract: Russia and South Africa are the world’s leading producers of platinum group elements (PGEs). This places them in a unique position regarding the supply of these two key industrial commodities. The purpose of this paper is to provide a comparative high-level overview of aspects of the geological occurrence, mineralogy, and processing by flotation of the platinum group minerals (PGMs) found in each country. A summary of some of the major challenges faced in each country in terms of the concentration of the ores by flotation is presented alongside the opportunities that exist to increase the production of the respective metals. These include the more efficient recovery of minerals such as arsenides and tellurides, the management of siliceous gangue and chromite in the processing of these ores, and, especially in Russia, the development of novel processing routes to recover PGEs from relatively low grade ores occurring in dunites, black shale ores and in vanadium-iron-titanium-sulphide oxide formations. Keywords: Russia; South Africa; PGMs; geology; mineralogy; flotation Citation: O’Connor, C.; Alexandrova, T. The Geological Occurrence, Mineralogy, and Processing by Flotation of Platinum Group Minerals (PGMs) in South 1. Introduction Africa and Russia.
    [Show full text]
  • NI 43-101 Report Template
    Report to: Technical Report on the Magino Property, Wawa, Ontario Document No. 1295890100-REP-R0001-02 1295890100-REP-R0001-02 Report to: TECHNICAL REPORT ON THE MAGINO PROPERTY,WAWA,ONTARIO EFFECTIVE DATE:OCTOBER 4, 2012 Prepared by Patrick Huxtable, MAIG (RPGeo) Todd McCracken, P.Geo. Todd Kanhai, P.Eng. PT/JW/jc 1295890100-REP-R0001-02 Report to: TECHNICAL REPORT ON THE MAGINO PROPERTY,WAWA,ONTARIO EFFECTIVE DATE:OCTOBER 4, 2012 “Original document signed by Prepared by Patrick Huxtable, MAIG (RPGeo)” Date October 4, 2012 Patrick Huxtable, MAIG (RPGeo) “Original document signed by Prepared by Todd McCracken, P.Geo.” Date October 4, 2012 Todd McCracken, P.Geo. “Original document signed by Prepared by Todd Kanhai, P.Eng.” Date October 4, 2012 Todd Kanhai, P.Eng. “Original document signed by Reviewed by Jeff Wilson, Ph.D., P.Geo.” Date October 4, 2012 Jeff Wilson, Ph.D., P.Geo. “Original document signed by Authorized by Jeff Wilson, Ph.D., P.Geo.” Date October 4, 2012 Jeff Wilson, Ph.D., P.Geo. PT/JW/jc Suite 900, 330 Bay Street, Toronto, Ontario M5H 2S8 Phone: 416-368-9080 Fax: 416-368-1963 1295890100-REP-R0001-02 REVISION HISTORY REV. PREPARED BY REVIEWED BY APPROVED BY NO ISSUE DATE AND DATE AND DATE AND DATE DESCRIPTION OF REVISION 00 2012/09/20 Patrick Huxtable Jeff Wilson Jeff Wilson Draft to Client for review. Todd McCracken 01 2012/09/27 Patrick Huxtable Jeff Wilson Jeff Wilson Draft to Client for review. Todd McCracken 02 2012/10/04 Patrick Huxtable Jeff Wilson Jeff Wilson Final to Client.
    [Show full text]
  • Scavenging Flotation Tailings Using a Continuous Centrifugal Gravity Concentrator
    Scavenging Flotation Tailings using a Continuous Centrifugal Gravity Concentrator by Hassan Ghaffari B.A.Sc. & M.A.Sc. Department of Mining Engineering, Technical Faculty Tehran University, Iran, 1990 A THESIS SUBMITTED IN PARTIAL FULFILMENT OF THE REQUIREMENTS FOR THE DEGREE OF Master of Applied Science in THE FACULTY OF GRADUATE STUDIES DEPARTMENT OF MINING ENGINEERIG THE UNIVERSITY OF BRITISH COLUMBIA We accepted this thesis as conforming to the required standard THE UNIVERSITY OF BRITISH COLUMBIA August 2004 © Hassan Ghaffari, 2004 THE UNIVERSITY OF BRITISH COLUMBIA FACULTY OF GRADUATE STUDIES Library Authorization In presenting this thesis in partial fulfillment of the requirements for an advanced degree at the University of British Columbia, I agree that the Library shall make it freely available for reference and study. I further agree that permission for extensive copying of this thesis for scholarly purposes may be granted by the head of my department or by his or her representatives. It is understood that copying or publication of this thesis for financial gain shall not be allowed without my written permission. H ASS A A/ GrMFFAR I 31 ,o%2t>4 Name of Author (please print) Date (dd/mm/yyyy) Title of Thesis: Degree: /l/l-A S C Year: Department of The University of British Columbiumbia ^ u c/ Vancouver, BC Canada grad.ubc.ca/forms/?formlD=THS page 1 of 1 last updated: 31-Aug-04 11 Summary A study was conducted to evaluate the Knelson Continuous Variable Discharge (CVD) concentrator as a scavenger for coarse middling particles from flotation tailings. The goal was to recover a product of suitable grade for recycling to the grinding circuit to improve liberation and aid subsequent recovery in flotation.
    [Show full text]
  • Knelson Concentrator
    UPGRADING OF GOLD GRAVITY CONCENTRATES A STUDY OF THE KNELSON CONCENTRATOR Liming Huang A thesis subrnitted to the Faculty of Graduate Studies and Research in partial fuifiiiment of the requirements for the Degree of Philosophy Department of Mining and Metaliurgical Engineering, McGill University Montreal, Canada National Library Bibliothèque nationale 1*1 of Canada du Canada Acquisitions and Acquisitions et Bibliographie Services services bibliographiques 395 Wellington Street 395. nie Wellington ûîtawaON K1AON4 OttawaON K1AOW Canada Canada The author has granted a non- L'auteur a accordé une licence non exclusive licence dowing the exclusive permettant à la National Library of Canada to Bibliothèque nationale du Canada de reproduce, loan, distribute or sell reproduire, prêter, distribuer ou copies of ths thesis in microfom, vendre des copies de cette thèse sous paper or electronic formats. la forme de microfiche/£ïlm, de reproduction sur papier ou sur format électronique. The author retains ownership of the L'auteur conserve la propriété du copyright in this thesis. Neither the droit d'auteur qui protège cette thèse. thesis nor substantid extracts from it Ni la thèse ni des extraits substantiels may be printed or otherwise de celle-ci ne doivent être imprimés reproduced without the author's ou autrement reproduits sans son permission. autorisation. ABSTRACT In recent years. the Knelson Concentrator has become the predominant unit used for primary goid recovery by gravity . However. its application potential as a cleaner in the final gravity concentration stage and its separation mechanisms have not been well studied. In most Canadian gold mills. rougher gravity concentrates produced by the Knelson (operating at 60 gravity acceleration or 'g') are further upgraded with shaking tables.
    [Show full text]
  • Flotation and Gravity Separation
    'r 1 TECHNICAL, REPORT December 1,1994 through February 28, 1995 Project Title: A FINE COAL CIRCUITRY STUDY USING COLUMN FLOTATION AND GRAVITY SEPARATION DOE Cooperative Agreement Number: DE-FC22-92PC92521 (Year 3) ICCI Project Number: 94-l/l.lA-lP Principal Investigator: Ricky Q. Honaker Department of Mining Engineering Southern Illinois University Other Investigators: Stephen Reed Kerr-McGee Coal Corporation Project Manager: Ken Ho, Illinois Clean Coal Institute ABSTRACT Column flotation provides excellent recovery of ultrafine coal while producing low ash content concentrates. However, column flotation is not efficient for treating fine coal containing sigtllficant amounts of mixed-phase particles. Fortunately, enhanced gravity separation has proved to have the ability to treat the mixed-phased particles more effectively. A disadvantage of gravity separation is that ultrafine clay particles are not easily rejected. Thus, a combination of these two technologies may provide a circuit that maximizes both the ash and sulfur rejection that can be achieved by physical coal cleaning while maintaining a high energy recovery. This project is studying the potential of using different combinations of gravity separators, i.e., a Floatex hydrosizer and a Falcon Concentrator, and a proven flotation column, which will be selected based on previous studies by the principle investigator. During this reporting period, an in-plant Box-Behnken test program of the Floatex hydrosizer has been conducted at Kerr-McGee's Galatia preparation plant. The results have shown that the Floatex hydrosizer can be successfblly used to reject most of coarser (+lo0 mesh) pyrite and mineral matter in the coal stream to the plant.
    [Show full text]
  • British Geological Survey
    BRITISH GEOLOGICAL SURVEY Mineralogy and Petrology Short Report Series Short Report No. MPSR/99/24 RECOVERING THE LOST GOLD OF THE DEVELOPING WORLD: BIBLIOGRAPHIC DATABASE E J Evans & C J Mitchell Date 31/03/99 Classification Open Geographical Index World-wide Subject index Gold, mercury, mineral processing, gravity, sluice, Bibliographic reference E J Evans & C J Mitchell Recovering the lost gold of the developing world: bibliographic database Mineralogy and Petrology Group Short Report MPSR/99/24 ©NERC 1999 British Geological Survey, Keyworth, Nottingham. NG12 5GG. UK. MPSR/99/24 31103/99 BRITISH GEOLOGICAL SURVEY Mineralogy and Petrology Group Short Report No. MPSR/99/24 Recovering the lost gold of the developing world: bibliographic database E J Evans & C J Mitchell INTRODUCTION This report contains a library of 181 references, including abstracts, prepared for Project R 7120 "Recovering the lost gold of the developing world" funded by the UK' s Department for International Development (DFID) under the Knowledge and Research (KAR) programme. As part of an initial desk study, a literature review of gold processing methods used by small-scale miners was carried out using the following sources; the lSI Science Citation Index accessed via Bath Information and Data Services (BIDS), a licensed GEOREF CD-ROM database held at the BGS's Library in Keyworth and IMMage a CD-ROM database produced by the Institution of Mining and Metallurgy held by the Minerals group ofBGS. Information on the search terms used is available from the author. Results of this literature review were compiled in digital form as an Endnote® bibliographic library containing 181 individual references.
    [Show full text]
  • Towards the Recovery of Rare Earth Elements from End-Of-Life Products: Hydrometallurgical Routes and Mathematical Modelling of Extraction Systems
    Chemical Engineering Department PhD Program: Chemical Processes Engineering TOWARDS THE RECOVERY OF RARE EARTH ELEMENTS FROM END-OF-LIFE PRODUCTS: HYDROMETALLURGICAL ROUTES AND MATHEMATICAL MODELLING OF EXTRACTION SYSTEMS Author: Eleonora Obón Estrada Director: Dr. Ana Maria Sastre Requena Codiretor: Dr. Agustín Fortuny Sanromà Escola Tècnica Superior d’Enginyeria Industrial de Barcelona (ETSEIB) Universitat Politècnica de Catalunya, Barcelona, July 2019 Thesis presented to obtain the qualification of Doctor awarded by the Universitat Politècnica de Catalunya II Abstract The rare earth elements (REEs) are essential ingredients for the development of modern industry and the transition to a more sustainable economy model. The unique physicochemical features of these elements, such as their magnetism and optical properties, are greatly expanding their application. They have become key elements for the manufacture of many ordinary consumer goods like hybrid cars, fluorescent lamps or electronic devices like mobile phones or tablets. The growing popularity of the rare earth elements derivatives is leading to an increase in the global demand and the price of these elements. Unfortunately, the current availability of these resources is limited due to three main factors: their heterogeneous geological location, their low concentration in the ores, and the environmental issues related with their mining. All these disadvantages concerning the supply of the rare earth elements have led to the study of new techniques to obtain them, such as the recycling of end- of-life products. Recycling of REEs arises as a new secondary source of supply of REEs, especially in Europe where large amounts of technological waste are generated every year. Currently, the recycling of rare earth elements represents less than 1% of the global supply.
    [Show full text]