Solvent extraction is a critical process for lithium (Li) recovery from salt lake brine. The use of tributyl phosphate (TBP) as the extractant and ferric chloride (FeCl3) as the co-extractant significantly enhances Li extraction efficiency and selectivity. However, this method is seldom applied for lithium recovery from spent lithium batteries (LIB). This study, proposes a novel process for recovering Li from the leachate of spent lithium iron phosphate batteries (LiFePO4), using the iron source of LiFePO4 to exert the effect of FeCl3 co-extractant in the system. The system used TBP as the extractant and sulfonated kerosene as the diluent. Chlorine sources (NaCl, MgCl2, AlCl3) were added to investigate their effects on the extraction of Li from simulated leachate of LiFePO4. Additionally, Li was extracted from the real leachate. Through experiments using simulated solution, it was found that the extraction efficiency of Li could reach up to 73.1 % using AlCl3 as the external chlorine source, with a chloride ion concentration (c(Cl−)) of 6 mol/L, a TBP volume ratio of 70 %, an acidity of 0.025 mol/L, and an extraction time of 15 min. Under these optimal extraction conditions, the extraction efficiency of Li from the actual leachate was demonstrated to be 36.0 %, showing the feasibility of Li extraction solely by relying on iron(III) ions in the leachate. Due to the limited iron content in the leachate, the secondary extraction efficiency of Li was increased to 61.0 % by adding FeCl3, which resulted in a final total extraction efficiency of 74.0 %.
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