Simultaneous electrogenerative leaching of chalcopyrite concentrate and MnO2

Shao-fen Wang , Zheng Fang , Ya-fei Tan

Journal of Central South University ›› 2006, Vol. 13 ›› Issue (1) : 49 -52.

PDF
Journal of Central South University ›› 2006, Vol. 13 ›› Issue (1) : 49 -52. DOI: 10.1007/s11771-006-0105-6
Article

Simultaneous electrogenerative leaching of chalcopyrite concentrate and MnO2

Author information +
History +
PDF

Abstract

In order to enhance the electrogenerative leaching rate of chalcopyrite concentrate reasonably, the principle of generative process was applied to simultaneous leaching of chalcopyrite concentrate and MnO2. The results show that Cu2+ and Mn2+ in addition to electrical energy could be acquired in the simultaneous electrogenerative leaching process. The leaching cell has the open circuit potential of about 1.0 V and gains quantity of electricity of about 700 C. The optimum leaching rates of Cu2+ and Mn2+ are 23.1% and 22.1%, respectively after electrogenerative leaching for about 10 h under the present conditions.

Keywords

chalcopyrite concentrate / electrogenerative leaching / MnO2

Cite this article

Download citation ▾
Shao-fen Wang, Zheng Fang, Ya-fei Tan. Simultaneous electrogenerative leaching of chalcopyrite concentrate and MnO2. Journal of Central South University, 2006, 13(1): 49-52 DOI:10.1007/s11771-006-0105-6

登录浏览全文

4963

注册一个新账户 忘记密码

References

[1]

WangShao-fen, FangZheng, WangYun-yan. Application of carbon paste electrode on the electrogenerative-leaching process of sulfide minerals[J]. Electrochemistry, 2005, 11(1): 77-82(in Chinese)

[2]

WangShao-fen, FangZheng, WangYun-yan, et al.. Electrogenerative leaching of nickel concentrate with ferric chloride[J]. Journal of Central South University of Technology, 2004, 11(4): 405-409

[3]

WangShao-fen, FangZheng. Study on the intensifying and catalyzing action of the electrogenerative leaching process of sulfide minerals [J]. Journal of Changsha University of Science and Technology (Natural Science), 2004, 1(3): 87-91(in Chinese)

[4]

WangShao-fen, FangZheng, WangYun-yan, et al.. Electrogenerative leaching of galena with ferric chloride[J]. Minerals Engineering, 2003, 16(9): 869-872

[5]

WangShao-fen, FangZheng, ChenYang-guo, et al.. Application of mechanical activation on the electrogenerative leaching process of galena[J]. The Chinese Journal of Hydrometallurgy, 2003, 22(2): 93-96(in Chinese)

[6]

WangShao-fen, FangZheng, ChenYang-guo, et al.. Exploration of electrogenerative leaching of PbS with FeCl3 [J]. The Chinese Journal of Process Engineering, 2002, 2(3): 235-240(in Chinese)

[7]

WangShao-fen, FangZheng, ChenYang-guo. An investigation on electrogenerative leaching of galena with FeCl3 [J]. Journal of the Chinese Rare Earth Society, 2002, 20(S): 234-236(in Chinese)

[8]

DeviN B, MadhuchhandaM, RathP C, et al.. Simultaneous leaching of a deep-sea manganese nodule and chalcopyrite in hydrochloric acid[J]. Metallurgical and Materials Transactions B: Process Metallurgy and Materials Processing Science, 2001, 32(5): 777-784

[9]

DeviN B, MadhuchhandaM, RaoK S, et al.. Oxidation of chalcopyrite in the presence of manganese dioxide in hydrochloric acid medium[J]. Hydrometallurgy, 2000, 57(1): 57-76

[10]

ChenHsiao-hong, FuChong-yue. Leaching of manganese nodule in dilute acid solutions in presence of zinc sulfide concentrate[J]. Mineral Processing and Extractive Metallurgy Review, 1994, 15(1–4): 95-100

[11]

TakamiK, Yo-ichS, AtsukoM, et al.. Kinetic model for simultaneous leaching of zinc sulfide and manganese dioxide in the presence of iron-oxidizing bacteria [J]. Canadian Journal of Chemical Engineering, 1996, 74(3): 353-362

[12]

ChenHsiao-hong, FuChong-yue. Kinetics of leaching manganese nodules in the presence of zinc sulfide[J]. Mineral Processing and Extractive Metallurgy Review, 1994, 15(1–4): 101-114

[13]

NayakB B, MishraK G, ParamguruR K. Kinetics and mechanism of MnO2 dissolution in H2SO4 in the presence of pyrite[J]. Journal of Applied Electrochemistry, 1999, 29(2): 191-200

[14]

ParamguruR K, KanungoS B. Electrochemical phenomena in MnO2-FeS2 leaching in dilute HCl. Part 1: Theoretical derivation of rate equations under various limiting conditions[J]. Canadian Metallurgical Quarterly, 1998, 37(5): 389-393

[15]

ParamguruR K, KanungoS B. Electrochemical phenomena in MnO2-FeS2 leaching in dilute HCl. Part 3: Manganese dissolution from indian ocean nodules [J]. Canadian Metallurgical Quarterly, 1998, 37(5): 405-417

[16]

DutrizacJ E. Dissolution of chalcopyrite in ferric sulfate and ferric chloride media [J]. Metallurgical Transactions B, 1981, 12B(2): 371-378

[17]

HiroshiM, YasuhiroA, TetsujiH, et al.. Leaching of chalcopyrite in ferric chloride and ferric sulfate solutions[J]. Canadian Metallurgical Quarterly, 1985, 24(4): 283-291

[18]

SaxenaN N, MandreN R. Mixed control kinetics of copper dissolution for copper ore use ferric chloride [J]. Hydrometallurgy, 1992, 28(1): 111-117

[19]

LuZ Y, JeffreyM I, LawsonF. Effect of chloride ions on the dissolution of chalcopyrite in acidic solutions[J]. Hydrometallurgy, 2000, 56(2): 189-202

[20]

PalmerB R, NeboC O, RauM F, et al.. Rate phenmena involved in the dissolution of chalcopyrite in chloride-bearing lixivants[J]. Metallurgical Transactions B, 1981, 12B(3): 595-601

AI Summary AI Mindmap
PDF

95

Accesses

0

Citation

Detail

Sections
Recommended

AI思维导图

/