Lithium extraction from synthetic brine with high Mg2+/Li+ ratio using the polymer inclusion membrane

被引:83
作者
Zhang, Chengyi [1 ]
Mu, Yingxin [1 ]
Zhao, Song [1 ]
Zhang, Wen [1 ]
Wang, Yuxin [1 ]
机构
[1] Tianjin Univ, State Key Lab Chem Engn, Tianjin Key Lab Membrane Sci & Desalinat Technol, Sch Chem Engn & Technol, Tianjin 300350, Peoples R China
基金
中国国家自然科学基金;
关键词
High Mg2+/Li+ ratio solution; Lithium extraction; Polymer inclusion membrane; TBP/FeCl3 extraction system; SALT LAKE BRINE; METHYL ISOBUTYL KETONE; ACTINIDE ION UPTAKE; TRIBUTYL-PHOSPHATE; SELECTIVE EXTRACTION; SOLVENT-EXTRACTION; AQUEOUS-SOLUTION; CROWN-ETHER; METAL-IONS; RECOVERY;
D O I
10.1016/j.desal.2020.114710
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Lithium extraction from brines with the high Mg2+/Li+ ratio is crucial for sustainable lithium resource and environmental protection. This study incorporated the classic tributylphosphate (TBP)/FeCl3 system into the polyvinyl chloride (PVC) based polymer inclusion membrane (PIM) to extract Li+ from the solution which is rich of Mg2+ (The initial Mg2+/Li+ molar ratio is 15). The morphology and composition of PIMs were characterized systematically, and the content of TBP/FeCl3 carrier in the PIM was optimized. Compared to liquid-liquid extraction, the extraction ratio of Li+ for PIM extraction increases by 20% and the separation factor of Li+ over Mg2+ increases by 5%. Besides, the loss ratio of Fe3+ after one loop of liquid-liquid extraction is 17.79%, which is close to that of PIM extraction after three loops (18.30%), demonstrating that the PIM showed a good stability. Furthermore, the separation factor of Li+ over Mg2+ for the PIM with 50 wt% TBP/FeCl3 is as high as 176 and the initial flux for Li+ is 8.12 x 10(-4) mol m(-2) h(-1). This study displays a TBP/FeCl3 based PIM with high selectivity for Li+, providing a possible membrane technology for lithium extraction from brines.
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页数:12
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