Electrolyte purification in energy-saving monovalent copper electrowinning processes

被引:39
作者
Alam, M. S.
Tanaka, M.
Koyama, K.
Oishi, T.
Lee, J.-C.
机构
[1] Natl Inst AIST, Res Inst Environm Management Technol, Tsukuba, Ibaraki 3058569, Japan
[2] Mem Univ Newfoundland, Fac Engn & Appl Sci, St John, NF A1B 3X5, Canada
[3] KIGAM, Minerals & Mat Proc Div, Taejon 305350, South Korea
基金
日本学术振兴会;
关键词
copper; nickel; cobalt; zinc; ammonia; LIX; 26; electrolyte purification; cementation; solvent extraction; alkaline solution; monovalent copper electrowinning;
D O I
10.1016/j.hydromet.2006.12.001
中图分类号
TF [冶金工业];
学科分类号
0806 ;
摘要
A suitable method has been proposed to purify a copper electrolyte within the framework of an energy-saving cuprous electrowinning process. In this method, the impurities are selectively removed from the electrolyte that contains a large amount of cuprous ion in an ammoniacal alkaline solution at pH 9-11. Among these impurities, precious metals such as silver are removed by cementation with copper powder. Other metals such as cobalt, nickel, zinc, aluminum, manganese, lead etc. are removed selectively by solvent extraction using an oxine-type chelating extractant (LIX 26). Equilibrium and kinetic studies for the extraction of cobalt, nickel, and zinc were performed under different experimental conditions with or without synergistic agents. Loading tests of LIX 26 were carried out, and McCabe-Thiele diagrams were constructed for stage calculations for these metals. The metals are extracted with LIX 26 via a cation exchange mechanism, and slope analysis suggested that the nickel and zinc chelates, extracted by LIX 26, were 1:2 metal:reagent species. The loaded organic is regenerated by stripping the metals completely using dilute sulfuric acid. Copper loss in the purification stages is about 10% because monovalent copper is not extracted with LIX 26 from the ammoniacal alkaline solution. (C) 2007 Elsevier B.V. All rights reserved.
引用
收藏
页码:36 / 44
页数:9
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