Extraction of Lithium from High-Sodium Wastewater Based on DBM/TBP Technology

被引:0
|
作者
Du, Jinjing [1 ]
Wang, Dongbo [1 ]
Ma, Jiayi [1 ]
Zhai, Ruitong [1 ]
Lin, Haiyang [1 ]
Wang, Bin [2 ]
Li, Qian [1 ]
He, Xihong [1 ]
Zuo, Heng [3 ]
机构
[1] Xian Univ Architecture & Technol, Sch Met Engn, Xian 710055, Shaanxi, Peoples R China
[2] Quzhou Huayou Cobalt New Mat Co Ltd, Quzhou 324000, Zhejiang, Peoples R China
[3] Shaanxi Wuzhou Min Co LTD, Shangluo 726000, Shaanxi, Peoples R China
来源
关键词
SOLVENT-EXTRACTION; SEPARATION; BATTERIES; RECOVERY; BRINE; PERFORMANCE; MAGNESIUM;
D O I
10.1007/s11837-024-06827-5
中图分类号
T [工业技术];
学科分类号
08 ;
摘要
A method for selectively extracting lithium from lithium sulfate solution is proposed by using a synergistic DBM/TBP extraction system and employing linear analysis and DFT calculations to explore the synergistic extraction mechanism of lithium. The experimental results showed that, for a simulated solution containing 2.0 g/L lithium and 50 g/L sodium, and 0.5 mol/L DBM + 1 mol/L TBP + sulfonated kerosene as the organic phase, at an O/A phase ratio of 1:1, an equilibrium pH of 13, a temperature of 25 degrees C, and a reaction time of 3 min, the single-stage extraction rate of lithium reached 94.5%, with a beta Li/Na ratio of 210. Through three-stage simulated countercurrent extraction under an O/A phase ratio of 1:3 and an equilibrium pH of 13, more than 99% of the lithium was extracted. Washing with 0.5 mol/L H2SO4 at a phase ratio of 2:1 removed nearly 98% of the sodium. After washing, the loaded organic phase was subjected to three-stage countercurrent re-extraction using 1.5 mol/L H2SO4 under an O/A phase ratio of 3:1, achieving a lithium re-extraction rate greater than 99%. The DBM/TBP synergistic extraction system can effectively selectively recover lithium from lithium sulfate solution, achieve deep separation of lithium and sodium, and achieve high-concentration recovery of lithium.
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页数:13
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