Principles of Mineral Processing
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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 -
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. -
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 .................................................................................................. -
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]). -
A Study of a Carbonaceous Gold Ore James S
Montana Tech Library Digital Commons @ Montana Tech Bachelors Theses and Reports, 1928 - 1970 Student Scholarship 1941 A Study of a Carbonaceous Gold Ore James S. Huckaba Follow this and additional works at: http://digitalcommons.mtech.edu/bach_theses Part of the Ceramic Materials Commons, Environmental Engineering Commons, Geology Commons, Geophysics and Seismology Commons, Metallurgy Commons, Other Engineering Commons, and the Other Materials Science and Engineering Commons Recommended Citation Huckaba, James S., "A Study of a Carbonaceous Gold Ore" (1941). Bachelors Theses and Reports, 1928 - 1970. 147. http://digitalcommons.mtech.edu/bach_theses/147 This Bachelors Thesis is brought to you for free and open access by the Student Scholarship at Digital Commons @ Montana Tech. It has been accepted for inclusion in Bachelors Theses and Reports, 1928 - 1970 by an authorized administrator of Digital Commons @ Montana Tech. For more information, please contact [email protected]. ! -.. '_ _. r' ...: ,.... ,/'" f • . A STUJ.)Y C.u.RBON.u.CiiOUS GOLD By James S. Huckaba A Thesis ubmitted to the Departmen~ of etallurgy in }artial Fulf11~ent of the Requirouents fer the Degree of 2cchelor of ~cience in Jetallurgical ~n0ineering MONTAI~ SCI! OL OF r.mreB LIBRARY BUTTE " A S'J]UDY OF CARB ADEOUS GOLD ORE By ~mnes S. Huckaba I -4 D 70 s: Thesis Submi tted to the Dep artment of etallurgy in Partial Fulfillment of the Requirements for the Degree of Bachelor of Science in ~etallurgical Engineering MONTANA SCHOOL OF MINES LIBRARY, I - TABLE OF CONrENI'S -
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. -
The Separation of Galena and Blende from Their Gangue As Practised at the Mines of Sentein, Ariege, France
3% LUEIS ON THE SEPARATION OF GALENA AND BLENDE. [Selected (Paper No. 1942.) The Separation of Galena and Blende fiom their gangue as practised at the Mines of Sentein, Arihge, France.” By ERNESTDU BOISLUKIS, Assoc. M. Inst. C.E. THISis a record of detailed observations made whilst preparing formarket galena and blende, at the mines of Sentein in the Pyrenees. The oreswere intimately mixed in the proportion of 8 to 10 per cent. of galena, 15 to 20 percent. of blende, and gangue consisting of hard quartz, quartzose rock, schist, &c. The market lead-ore obtained included from 16 to 20 oz. of silver per ton.The blende did not contain sufficient silver for valuation. By experiments in the laboratory, it was found that the galena lost very little silver byfine crushing and washing. The machinery, supplied by Mr. George Green, of Aberystwyth, was erected in existing buildings; but these were so scattered that it is not thoughtnecessary to givea plan of them. Instead of this, a method of arranging the whole of the required plant under one roof, with slight modifications, that would render such proposed dressing-floors more efficient, is given in Plate 7, Figs. 1, the sub- stantialstructure indicated being necessary on account of the climate of the Pyrenees, where protection from frost and snow is indispensable. Water-power was used, being abundant, but the motors are not shown in Figs. 1, for, depending on the position of such proposed floors, steamor water wouldbe used asmight be found most advantageous. Mention is, however, made later on of the power required. -
FIG. 1 I Crush And/Or Grind to Free the Iron Oxide
Aug. 22, 1967 J‘ E. LAWVER 3,337,328 IRON ORE BENEFICIATION PROCESS Filed June 19, 1964 6 Sheets-Sheet l Heavy Media Tailings Tailing Pond Fines or Semitaconite 25 to 50% Iron FIG. 1 I Crush and/or Grind to Free the Iron Oxide Partial Concentration to Separate Iron Mineral from Waste Product by one of Following Processes or or A B C High Intensity Wet Froth Gravity Magnetic Separation Flotation Separation l l I I Partial Waste Partial Waste Partial Waste Concentrate Product Concentrate Product Concentrate Product L I I . Gravity Gravity Concentrates or Separation of Partial‘ Concentrates Low-grade Hematitic Ore From "An or “all or "ch 40 to 58%‘.Iron Crush and Grind to Liberate Silica Coarse Fraction Minus O. 010" plus 0.003" Fine Fraction‘ Less than 0.003" G to 75% Weight @ 25 to 100% Weight Electrodynamic Process to Separate Froth Flotation Process to Separate Iron Oxides and Silica Iron Oxides and Silica Silica Product to Waste Silica Product to Waste Iron Oxide Concentrate 62 to 65% Iron 5% Silica ' INVENTOR J9me; E. L’ AWl/ER 14 T TORNE Y! Aug. 22, 1967 J. e. LAWVER 3,337,328 IRON ORE BENEFICIATION PROCESS Filed ‘June 19, 1964 6 Sheets-Sheet 2 Crude Ore %Wt. 100. O0 FIG.' 2 %Fe%Insol.4l.l9 39 . 35 4" Screen -4" Ore +4" Ore %wt.84.45 %Wt. 15.39 %E‘e 4O. 19 %E'e 34. 75 %Inso]l . 48. 57 Crush 8 Screen %Fe Rec.l3.59 _ -___.______ +14 Mesh ~~14 Mesh Heavy Media Sands Slimes Separation '7‘Wt- 9-58 Spirals %E‘e 11.78 Sinks Floats ' Concentrate r(‘ailing %Wt. -
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. -
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. -
Control of Comminution Circuit for Efficient Froth Flotation D
FROTH FLOTATION : RECENT TRENDS @IIME, JAMSHEDPUR, 1998; pp. 10-17 Control of Comminution Circuit for Efficient Froth Flotation D. D. IVIIISRA ilndian School of Mines, :Marked] - 626004 ABSTRACT Efficiency of separation in the froth flotation circuit is rely much dependant on the efficiency of size reduction and size separation in the preceeding comminution and classification circuit. A coarser grinding product than desired causes loss of grade or recovery due to inadequate liberation where as with over grinding there is an increase in slime loss. This paper ennumerates the factors that affect the performance of the grinding circuit and the steps that should be taken for its efficient operation. Once the grinding circuit is commisioned its performance is dependant mainly on the operation and control of the classifier. In case of the mechanical classifiers very effective control can be obtained by suitably varying the wash water flow rate and the weir height. In case of the cyclone classifiers the control is some what difficult. Key Words : Comminution circuit, Control froth flotation, Operating parameters, Efficiency. INTRODUCTION The froth flotation process is extremely sensitive to the particle size. Ideally the particles should be just small enough to ensure liberation of the ore from the gangue and no smaller. In some rare cases of relatively high grade ore deposits some what acceptable liberation may take place at a size too large (+1 mm) to float in thd froth flotation, process. In such cases the ore should be ground to about -0.3 mm to ensure flotation as the flotation rate is observed to decrease rapidly with the increase in particle size. -
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.