Electrochemical simulation of redox potential development in bioleaching of a pyritic chalcopyrite concentrate

被引:26
作者
Khoshkhoo, Mohammad [1 ]
Dopson, Mark [2 ]
Shchukarev, Andrey [3 ]
Sandstrom, Ake [1 ]
机构
[1] Lulea Univ Technol, Div Sustainable Proc Engn, SE-97187 Lulea, Sweden
[2] Linnaeus Univ, Ctr Ecol & Evolut Microbial Model Syst, S-39182 Kalmar, Sweden
[3] Umea Univ, Dept Chem, S-90187 Umea, Sweden
基金
瑞典研究理事会;
关键词
Chalcopyrite; Bioleaching; Electrochemical cell; Redox potential; XPS; THIOBACILLUS-FERROOXIDANS; FERROUS-IONS; DISSOLUTION; OXIDATION; MECHANISM; BACTERIA; SULFIDE; SULFUR; XPS;
D O I
10.1016/j.hydromet.2013.12.003
中图分类号
TF [冶金工业];
学科分类号
080601 [冶金物理化学];
摘要
The majority of the world's copper reserves are bound in the sulphide mineral chalcopyrite (CuFeS2), but supply of the copper is hindered by the recalcitrance of chalcopyrite to (bio)leaching. The main reason for the slow rate of chalcopyrite dissolution is the formation of a layer on the surface of the mineral that hinders dissolution, termed "passivation". The nature of this layer and the role of microorganisms in chalcopyrite leaching behaviour are still under debate. Moderately thermophilic bioleaching of a pyritic chalcopyrite concentrate was mimicked in an electrochemical vessel to investigate the effect of the absence and presence of microorganisms in copper dissolution efficiency. Data from the redox potential development during bioleaching was used to program a redox potential controller in an electrochemical vessel to accurately reproduce the same leaching conditions in the absence of microorganisms. Two electrochemical experiments were carried out with slightly different methods of redox potential control. Despite massive precipitation of iron as jarosite in one of the electrochemically controlled experiments and formation of elemental sulphur in both electrochemical experiments, the efficiencies of copper dissolution were similar in the electrochemical tests as well as in the bioleaching experiment. No passivation was observed and copper recoveries exhibited a linear behaviour versus the leaching time possibly due to the galvanic effect between chalcopyrite and pyrite. The data suggest that the main role of microorganisms in bioleaching of a pyritic chalcopyrite concentrate was regeneration of ferric iron. It was also shown that the X-ray photoelectron spectroscopy measurements on the residues containing bulk precipitates cannot be employed for a successful surface characterisation. (C) 2014 Elsevier B.V. All rights reserved.
引用
收藏
页码:7 / 14
页数:8
相关论文
共 27 条
[1]
Synchrotron scanning photoemission microscopy of homogeneous and heterogeneous metal sulfide minerals [J].
Acres, Robert George ;
Harmer, Sarah Louise ;
Shui, Hung Wei ;
Chen, Chia-Hao ;
Beattie, David Allan .
JOURNAL OF SYNCHROTRON RADIATION, 2011, 18 :649-657
[2]
Use and limitations of electron flood gun control of surface potential during XPS: two non homogeneous sample types [J].
Baer, DR ;
Engelhard, MH ;
Gaspar, DJ ;
Lea, AS ;
Windisch, CF .
SURFACE AND INTERFACE ANALYSIS, 2002, 33 (10-11) :781-790
[3]
Leaching of chalcopyrite with ferric ion.: Part II:: Effect of redox potential [J].
Cordoba, E. M. ;
Munoz, J. A. ;
Blazquez, M. L. ;
Gonzalez, F. ;
Ballester, A. .
HYDROMETALLURGY, 2008, 93 (3-4) :88-96
[4]
How do bacteria interact with minerals? [J].
Crundwell, FK .
HYDROMETALLURGY, 2003, 71 (1-2) :75-81
[5]
CHEMICAL-ELECTROCHEMICAL APPROACHES TO THE STUDY PASSIVATION OF CHALCOPYRITE [J].
Debernardi, Gianfranco ;
Carlesi, Carlos .
MINERAL PROCESSING AND EXTRACTIVE METALLURGY REVIEW, 2013, 34 (01) :10-41
[6]
Dixon DG, 2008, CAN METALL QUART, V47, P327, DOI 10.1179/000844308794408317
[7]
Analysis of community composition during moderately thermophilic bioleaching of pyrite, arsenical pyrite, and chalcopyrite [J].
Dopson, M ;
Lindström, EB .
MICROBIAL ECOLOGY, 2004, 48 (01) :19-28
[8]
Fowler TA, 1999, APPL ENVIRON MICROB, V65, P5285
[9]
Fowler TA, 1999, APPL ENVIRON MICROB, V65, P2987
[10]
Electrochemistry of chalcopyrite [J].
Gomez, C ;
Figueroa, M ;
Munoz, J ;
Blazquez, ML ;
Ballester, A .
HYDROMETALLURGY, 1996, 43 (1-3) :331-344