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Development of a process for the separation of zinc and copper from sulfuric liquor obtained from the leaching of an industrial residue by solvent extraction
Authors:Ligiane R Gouvea  Carlos A Morais
Affiliation:1. Bafgh Zinc Smelting Plant, Iranian Zinc Mines Development Company (IZMDC), Yazd, Iran;2. Department of Mining Engineering, Tehran Science and Research Branch, Islamic Azad University, Tehran, Iran;3. Chemical Engineering Department, Jordan University of Science and Technology, Irbid, 22110, Jordan;4. School of Metallurgy and Materials Engineering, University of Tehran, Tehran, Iran;5. Faculty of Engineering, Tarbiat Modares University, Tehran, Iran
Abstract:This paper describes a study of the separation of zinc and copper from the leach liquor generated in the treatment of the zinc residue (29.6 g/L Zn and 37.4 g/L Cu) by liquid–liquid extraction. In it, the influence of the extractant type and concentration, aqueous phase acidity, contact time and stripping agent concentration were investigated. Organophosphorus extractants (D2EHPA, IONQUEST®801 and CYANEX®272) and the chelating extractants (LIX®63, LIX®984N and LIX®612N-LV) were also investigated. The organophosphorus reagents are selective for zinc, while the chelating extractants are selective for copper. In the experiment, D2EHPA was found to be the best extractant. A sulfuric acid solution was used in the stripping study. Five continuous experiments were carried out until an optimal condition for the separation of the metals Zn and Cu was achieved. Experiment 5 was carried out in three extraction steps, three scrubbing stages and five stripping stages. In this experiment, a pregnant strip solution containing 125 g/L Zn and 0.01 g/L Cu was obtained and the concentration of the metals in the raffinate was 28.3 g/L Cu and 0.49 g/L Zn.
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