Recovery of High-Purity Lithium Compounds from the Dust of the Smelting Reduction Process for Spent Lithium-Ion Batteries

The recovery of valuable metals such as cobalt, nickel, and lithium from spent lithium-ion batteries (LIBs) has attracted much attention. In this study, a hydrometallurgical process for the recovery of high-purity lithium compounds like Li2CO3 and Li3PO4 from dust containing Li, Co, Ni, Cu, Fe, Mn,...

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Bibliographic Details
Main Authors: Lee, M.S (Author), Son, S.H (Author), Tran, T.T (Author)
Format: Article
Language:English
Published: Korean Institute of Metals and Materials 2022
Subjects:
Online Access:View Fulltext in Publisher
LEADER 03187nam a2200529Ia 4500
001 10.3365-KJMM.2022.60.4.291
008 220510s2022 CNT 000 0 und d
020 |a 17388228 (ISSN) 
245 1 0 |a Recovery of High-Purity Lithium Compounds from the Dust of the Smelting Reduction Process for Spent Lithium-Ion Batteries 
260 0 |b Korean Institute of Metals and Materials  |c 2022 
856 |z View Fulltext in Publisher  |u https://doi.org/10.3365/KJMM.2022.60.4.291 
520 3 |a The recovery of valuable metals such as cobalt, nickel, and lithium from spent lithium-ion batteries (LIBs) has attracted much attention. In this study, a hydrometallurgical process for the recovery of high-purity lithium compounds like Li2CO3 and Li3PO4 from dust containing Li, Co, Ni, Cu, Fe, Mn, and Si produced during the smelting reduction of spent LIBs was investigated. The separation of Li over other metals from the dust was achieved by two methods. The first method was to leach metals from the dust with distilled water and then to precipitate the dissolved metal ions from the leaching solution at pH 10. The second one was to mix the dust with solid NaOH, following the dissolution of the mixture with distilled water. Optimum conditions for the second method were a 1:0.17 weight ratio of dust to NaOH, 50 g/L pulp density for 120 min at 22oC. These two methods resulted in a solution containing only Li(I) and Na(I). The precipitation of Li(I) to Li2CO3 from the leaching solution by Na2CO3 with the addition of acetone or ethanol was optimized a 1:0.5 molar ratio of Li(I) to Na2CO3, 6:5 volume ratio of solvent to Li(I) solution for 30 min at 22oC. Under the optimum conditions, the precipitation percentage of Li(I) was higher than 92.0% with above 99.0% purity. Additionally, using Na3PO4, 97.1 % Li(I) was precipitated from the leaching solution to Li3PO4 with 93.1% purity. An optimized process for the recovery of lithium compounds from the dust is proposed. Copyright © The Korean Institute of Metals and Materials. 
650 0 4 |a Acetone 
650 0 4 |a Cobalt compounds 
650 0 4 |a Cobalt-nickel 
650 0 4 |a Copper compounds 
650 0 4 |a Distilled water 
650 0 4 |a dust 
650 0 4 |a Dust 
650 0 4 |a High purity lithium compounds 
650 0 4 |a leaching 
650 0 4 |a Leaching 
650 0 4 |a Leaching solution 
650 0 4 |a lithium 
650 0 4 |a Lithium compounds 
650 0 4 |a lithium-ion batteries 
650 0 4 |a Lithium-ion batteries 
650 0 4 |a Metal ions 
650 0 4 |a Metals 
650 0 4 |a Nickel compounds 
650 0 4 |a Optimum conditions 
650 0 4 |a Organic solvents 
650 0 4 |a Phosphorus compounds 
650 0 4 |a Precipitation (chemical) 
650 0 4 |a Recovery of valuable metals 
650 0 4 |a Reduction process 
650 0 4 |a Smelting reduction 
650 0 4 |a Sodium Carbonate 
650 0 4 |a Sodium hydroxide 
650 0 4 |a Solvent extraction 
650 0 4 |a solvent precipitation 
650 0 4 |a Solvent precipitation 
650 0 4 |a Spent lithium-ion batteries 
700 1 |a Lee, M.S.  |e author 
700 1 |a Son, S.H.  |e author 
700 1 |a Tran, T.T.  |e author 
773 |t Journal of Korean Institute of Metals and Materials