Extraction of Lithium from Salt Lake Brine and Mechanism Research

被引:0
|
作者
Sun Shu-Ying [1 ]
Ye Fan [1 ]
Song Xing-Fu [1 ]
Li Yun-Zhao [1 ]
Wang Jin [1 ]
Yu Jian-Guo [1 ]
机构
[1] E China Univ Sci & Technol, State Key Lab Chem Engn, Shanghai 200237, Peoples R China
关键词
extraction; brine; lithium; TBP; CHLORIDE; SYSTEM;
D O I
暂无
中图分类号
O61 [无机化学];
学科分类号
070301 ; 081704 ;
摘要
The paper presents extraction of lithium from salt lake brine by tributyl phosphate (TBP)- kerosene-FeCl3 extraction system. Extraction, washing and back extraction stages were studied systematically. The best conditions were determined by studying the single factors of extraction V-o/V-A ratio, extractant composition, molar ratio of Fe3+ to Li+ and so on, and the results were: extraction V-o/V-A is 1.5, TBP% is 75%, c(Fe)(3+)/c(Li+) is 2, c(H+) is 0.02 mol.L-1, extraction time is 20 min; washing V-o/V-A is 15; back extraction V-o/V-A is 20. The interaction of lithium complex with TBP was investigated by IR and NMR. The results showed that the complex and TBP were associated by hydrogen bond.
引用
收藏
页码:439 / 444
页数:6
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