Selective extractions of Zn and Cd from Zn-Cd-Co-Ni sulphate solution using di-2-ethylhexyl phosphoric acid extractant

被引:85
作者
Owusu, G [1 ]
机构
[1] Hudson Bay Min & Smelting Co, Flin Flon, MB R8A 1N9, Canada
关键词
D O I
10.1016/S0304-386X(97)00044-3
中图分类号
TF [冶金工业];
学科分类号
0806 ;
摘要
A bench scale solvent extraction study has been carried out on mixed electrolyte solutions containing zinc, cadmium and cobalt as sulphates. Very high separation factors or Delta pH(0.05) were obtained. These values indicate the ease of separation of these metals under appropriate conditions. In batch countercurrent experiments using a plant solution containing 83.2 g/l Zn, 52.8 g/l Cd, 2 g/l Co and 0.10 g/l Ni and 30 v/o di-2-ethylhexyl phosphoric acid (DEHPA) plus 4 v/o TBP in SX-1, stepwise (selective) extractions of zinc and cadmium from the mixed electrolyte solution were achieved, leaving cobalt and nickel in the raffinate. Zinc was extracted at pH 2.0 followed by cadmium extraction at pH 3.7. The Zn-loaded organic was scrubbed with ZnSO4 solution to remove any co-extracted cadmium and cobalt contaminants at equilibrium pH 2-2.2. Similarly, the Cd-rich organic phase was scrubbed with CdSO4 solution to remove any co-extracted cobalt and nickel species at pH 3.6-3.7. Under the experimental conditions, overall cobalt and nickel extractions were negligible. (C) 1998 Elsevier Science B.V.
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收藏
页码:205 / 215
页数:11
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