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The efficient recovery of lithium (Li+) from salt lakes has become a pressing issue for the lithium battery industry. In this study, an electrochemically enhanced extraction system with industrialization potential was developed, which increased the separation efficiency of Li+ by coupling an electric field with ionic liquid extraction. A promising 1-butyl-3-methylimidazolium-2-thiophenecarbonyl trifluoroacetone ([C4mim][TTA]) extraction agent was developed. Furthermore, the functionalized ionic liquid (FIL) was dissolved in an ionic liquid mixture to further increase its extraction capacity. The separation performance and mechanisms of Li+ through [C4mim][TTA] liquid–liquid extraction were investigated. The results showed that within a pH range greater than 2, [C4mim][TTA] had a very high separation efficiency for Li+. Additionally, liquid–liquid extraction in solutions simulating the concentrations of Li+, Na+, and K+ found in salt lakes revealed very high Li+ separation coefficients of βLi/K = 3746 and βLi/Na = 1287. Under an applied electric field of 2.4 V, the electrochemically enhanced extraction system achieved separation coefficients of βLi/K = 6678 and βLi/Na = 3068 within 2 h, which represent the highest reported values to date. In this study, a novel electrochemically coupled ionic liquid extraction system with potential for industrialization is proposed. © 2025 Elsevier B.V.
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Hydrometallurgy
ISSN: 0304-386X
Year: 2025
Volume: 237
4 . 8 0 0
JCR@2023
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ESI Highly Cited Papers on the List: 0 Unfold All
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