High Purity Nickel Recovery from an Industrial Sidestream Using Concentration and Liquid-Liquid Extraction Techniques

被引:2
作者
Hu, Fang [1 ,3 ]
Wilson, Benjamin P. [1 ]
Han, Bing [2 ]
Zhang, Jianxin [2 ]
Louhi-Kultanen, Marjatta [2 ]
Lundstrom, Mari [1 ]
机构
[1] Aalto Univ, Sch Chem Engn, Dept Chem & Met Engn CMET, Hydromet & Corros, POB 12200, Aalto 00076, Finland
[2] Aalto Univ, Sch Chem Engn, Dept Chem & Met Engn CMET, Chem Engn Aqueous Syst, POB 16100, Aalto 00076, Finland
[3] Cent South Univ, Coll Chem & Chem Engn, Changsha 410083, Hunan, Peoples R China
关键词
DIRECT SOLVENT-EXTRACTION; SODIUM-SALTS; SULFATE; PURIFICATION; COBALT; SEPARATION;
D O I
10.1007/s11837-019-03928-4
中图分类号
T [工业技术];
学科分类号
08 ;
摘要
This article outlines an alternative flowsheet for the purification of a multi-metal industrial sidestream (16.3 g/l Ni, 0.7 g/l Co, 0.6 g/l Ca and 1.6 g/l Mg) to allow high-purity nickel recovery. The methodology comprises an initial evaporation step to achieve Ca removal followed by impurity (Ca, Mg) and valuable (Co, Ni) element separation via two-step solvent extraction with organophosphorus extractants. Results indicate that > 80% of Ca is selectively removed as CaSO4 center dot 2H(2)O by evaporation with a concentration degree > 6. In the following treatment, 90% of residual Ca (0.6 g/l) can be selectively extracted with Na-D(2)EHPA. The subsequent solvent extraction step with Na-Cyanex 272 separates Co (> 99%) and Mg (> 95%). The resultant nickel sulfate solution (61.7 g/l Ni, 0.3 g/l Mg and Co 0.007 g/l) of > 99.5% purity can be directly integrated into state-of-the-art nickel recovery processes.
引用
收藏
页码:831 / 838
页数:8
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