4.4 Article

Extraction of Lithium from Salt Lake Brine with Triisobutyl Phosphate in Ionic Liquid and Kerosene

Journal

CHEMICAL RESEARCH IN CHINESE UNIVERSITIES
Volume 31, Issue 4, Pages 621-626

Publisher

HIGHER EDUCATION PRESS
DOI: 10.1007/s40242-015-4376-z

Keywords

Ionic liquid; Triisobutyl phosphate; Extraction; Lithium; Salt lake brine

Funding

  1. National Natural Science Foundation of China [21276194, U1407113]
  2. Training Program for Changjiang Scholars and Innovative Research Team in University, China [[2013]373]
  3. Innovative Research Team of Tianjin Municipal Education Commission, China [TD12-5004]

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Three ionic liquids(ILs), namely, 1-butyl-3-methylimidazolium hexafluorophosphate, 1-butyl-3-methylimidazolium bis[(trifluoromethyl) sulfonyl] imide and 1-ethyl-3-methylimidazolium bis[(trifluoromethyl) sulfonyl] imide with the triisobutyl phosphate(TIBP) and kerosene system were respectively used to extract lithium ion from salt lake brine with a high concentration ratio of magnesium and lithium experimentally. Results indicate that the highest extraction selectivity for lithium was obtained with IL 1-ethyl-3-methylimidazolium bis[(trifluoromethyl)sulfonyl] imide. The effects of solution pH and phase ratio R(O/A) on the extractive step and the influence of acid concentration of the stripping solution and R(O/A) on the back extraction step were also investigated systematically. The single-step extraction efficiency of lithium ion was 83.71% under the optimal extraction conditions, and the single-step back extraction efficiency was 85.61% with a 1.0 mol/L HCl in 1.0 mol/L NaCl medium as stripping agent at R(O/A)=2. The liquid-liquid extraction mechanism and the complex of the ligand with lithium were proposed.

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