Recovery of Li2SO4 from lithium -precipitated mother liquor via a Pb/FePO4 membrane -free electrochemical system

被引:19
作者
Huang, Zian [1 ]
Xu, Wenhua [2 ]
Zhao, Zhongwei [1 ,3 ]
Liu, Dongfu [1 ]
He, Lihua [1 ]
Liu, Xuheng [1 ]
机构
[1] Cent South Univ, Sch Met & Environm, Changsha 410083, Peoples R China
[2] Cent South Univ, Sch Mat Sci & Engn, Changsha 410083, Peoples R China
[3] Key Lab Hunan Prov Met & Mat Proc Rare Met, Changsha 410083, Peoples R China
基金
国家自然科学基金重大项目;
关键词
Lithium-precipitated mother liquor; Lithium extraction; LiFePO4; Pb; Electrochemical membrane-free system; SOLVENT-EXTRACTION; LIFEPO4/FEPO4; SEAWATER; IONS;
D O I
10.1016/j.cej.2023.143247
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Ore is the primary source of Li2CO3 production, but approximately 10-15% of lithium remains in the lithiumprecipitated mother liquor for each ton of Li2CO3 produced. Therefore, efficient recovery of Li2SO4 from this solution is essential to ensure Li2CO3 supply. The conventional "(+) LiFePO4/FePO4 (-)" membrane system has been successfully used to extract LiC1 from brine. However, the large radius of SO4- in the mother liquor significantly increases the cell voltage of this system, which is not favorable for separating Li+ and Nat We therefore developed a novel "(+) Pb/FePO4 (-)" membrane-free Li2SO4 extraction system that uses Pb and FePO4 to capture SO4- and Li+, which was then released by switching the electrode polarity after the adsorption was completed. The Li+ concentration in the mother liquor decreased from 1.3 to 0.014 g.L-1 in two cycles, and the Li+ recovery rate was 98.9%. The Li+ concentration in the recovery liquor reached 1.356 0,-1, with a Li-Na separation coefficient of 304. In addition, the new system did not suffer from lead dissolution loss, and the adsorption capacity of Li+ was 95.44% of the initial capacity after 15 cycles. Overall, this membrane-free lithium extraction system can provide a direction for extracting Li2SO4 from sulfate systems.
引用
收藏
页数:11
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