Removal of Magnesium in Zinc Hydrometallurgical System via Freezing Crystallization: From Laboratory Experiments to Industrial Application

Xin Jin, Yong Zhen, Xingbin Li, Min Du, Xingguo Luo (), Chang Wei, Zhigan Deng and Minting Li
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Xin Jin: Faculty of Metallurgical and Energy Engineering, Kunming University of Science and Technology, No. 68, Wenchang Road, 121 Street, Kunming 650093, China
Yong Zhen: Faculty of Metallurgical and Energy Engineering, Kunming University of Science and Technology, No. 68, Wenchang Road, 121 Street, Kunming 650093, China
Xingbin Li: Faculty of Metallurgical and Energy Engineering, Kunming University of Science and Technology, No. 68, Wenchang Road, 121 Street, Kunming 650093, China
Min Du: Sichuan Sihuan Zn & Germanium Technology Co., Ltd., Ya’an 625400, China
Xingguo Luo: Faculty of Metallurgical and Energy Engineering, Kunming University of Science and Technology, No. 68, Wenchang Road, 121 Street, Kunming 650093, China
Chang Wei: Faculty of Metallurgical and Energy Engineering, Kunming University of Science and Technology, No. 68, Wenchang Road, 121 Street, Kunming 650093, China
Zhigan Deng: Faculty of Metallurgical and Energy Engineering, Kunming University of Science and Technology, No. 68, Wenchang Road, 121 Street, Kunming 650093, China
Minting Li: Faculty of Metallurgical and Energy Engineering, Kunming University of Science and Technology, No. 68, Wenchang Road, 121 Street, Kunming 650093, China

Sustainability, 2023, vol. 15, issue 23, 1-13

Abstract: Magnesium (Mg) is not only a typical impurity but also an important valuable metal in the zinc (Zn) hydrometallurgical process. This study proposed the use of freezing crystallization to recover Mg and reduce the Mg 2+ concentration in waste electrolyte solutions, meeting the requirements of Zn hydrometallurgy. The experimental results indicated that the Mg 2+ concentration decreased from 23.60 g/L to 14.28 g/L under optimal conditions at a temperature of 263.15 K, holding time of 90.00–120.00 min, H 2 SO 4 concentration of 143.00 g/L, crystal seed addition of 50.00 g/L, and agitation speed of 300.00 rpm. The crystallization mother liquor was returned to the Zn hydrometallurgical process. The crystallization product was a mixture of MgSO 4 ·7H 2 O and ZnSO 4 ·7H 2 O with an aspect of 17. Notably, this method resulted in no discharge of waste gas, waste liquid, or waste residue. Additionally, during the industrial application process, the average removal efficiency of Mg 2+ was 40.15%. The concentration of Mg 2+ in waste electrolyte was reduced from 25.00–27.00 g/L to 13.00–15.00 g/L. These results indicated that the method effectively controlled the concentration of Mg 2+ in the waste electrolyte and facilitated the recovery of Mg resources from Zn hydrometallurgy.

Keywords: Zn hydrometallurgy; waste electrolyte; freezing crystallization; equilibrium solubility; removal of Mg (search for similar items in EconPapers)
JEL-codes: O13 Q Q0 Q2 Q3 Q5 Q56 (search for similar items in EconPapers)
Date: 2023
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