4.7 Article

Extraction and separation of indium and copper from zinc residue leach liquor by solvent extraction

期刊

SEPARATION AND PURIFICATION TECHNOLOGY
卷 156, 期 -, 页码 348-355

出版社

ELSEVIER SCIENCE BV
DOI: 10.1016/j.seppur.2015.10.021

关键词

Solvent extraction; Separation; Indium recovery; Reductive leach solution

资金

  1. National Basic Research Program of China [2014CB643404]
  2. National Natural Science Foundation of China [51304093, 51564030, 51174104, 51474117]
  3. Ph.D. Programs Foundation of Ministry of Education of China [20115314110001]

向作者/读者索取更多资源

Solvent extraction and separation of indium and copper from zinc residue reductive leach liquor containing a high concentration of zinc (ca. 85 g/L) and iron (ca. 35 g/L) was studied. Di-(2-ethylhexyl) phosphoric acid (D2EHPA) and Acorga M5640 were used as extractants for indium and copper, respectively. Indium was preferentially extracted by 15%(v/v) D2EHPA with three-stage extraction using an aqueous/organic (A/O) phase ratio of 6/1. Indium was effectively stripped from the D2EHPA organic phase by 4 M HCl. Copper was subsequently extracted selectively from the indium-extracted solution using 15%(v/v) Acorga M5640 with three-stage extraction using an A/O phase ratio of 2/1. Copper in the loaded Acorga M5640 organic phase was stripped by a synthetic spent electrolyte solution containing 25 g/L Cu and 180 g/L H2SO4. Based on the experimental results, a flowsheet for the separation and recovery of indium and copper from the reductive leach solution was developed and tested. The results showed that 95.4% of indium and 95.5% of copper were extracted, and the measured separation factors beta(In/Cu), beta(In/Fe), beta(CuZn), and beta(CuFe) were 4979, 1975, 3719, 1719, and 2446, respectively. (C) 2015 Elsevier B.V. All rights reserved.

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