Recovery of pure lithium phosphate from sulfuric acid leaching solutions of spent LiFePO4 batteries by solvent extraction and chemical precipitation

With the increasing use of electric vehicles, the demand for lithium iron phosphate batteries (LiFePO4) has risen sharply. Therefore, the recycling of metals from these batteries at the end of their life is necessary. In this study, a hydrometallurgical process for the recovery of lithium phosphate...

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Main Authors: Chen J., Tran T. T., Lee M. S.
Format: Article
Language:English
Published: University of Belgrade, Technical Faculty, Bor 2024-01-01
Series:Journal of Mining and Metallurgy. Section B: Metallurgy
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Online Access:https://doiserbia.nb.rs/img/doi/1450-5339/2024/1450-53392400013C.pdf
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author Chen J.
Tran T. T.
Lee M. S.
author_facet Chen J.
Tran T. T.
Lee M. S.
author_sort Chen J.
collection DOAJ
description With the increasing use of electric vehicles, the demand for lithium iron phosphate batteries (LiFePO4) has risen sharply. Therefore, the recycling of metals from these batteries at the end of their life is necessary. In this study, a hydrometallurgical process for the recovery of lithium phosphate from spent LiFePO4 batteries was developed. The effects of the parameters on the recovery process, consisting of leaching, solvent extraction, and precipitation were investigated. The addition of H2O2 to the H2SO4 solution was ineffective for the selective leaching of Li(I) over iron. The results showed that Li(I) and iron were completely dissolved by 1.5 mol/L H2SO4, 100 g/L pulp density at 25 °C for 60 min at 300 rpm. After oxidation of Fe(II) in the leaching solution by addition of H2O2, Fe(III) was completely separated from the solution by five steps of cross-flow extraction with 1.0 mol/L D2EHPA at room temperature. The loaded Fe(III) was successfully separated by four steps of cross-current stripping with 50% (v/v) aqua regia solution. Finally, most Li(I) was recovered by precipitation of lithium phosphate from the iron-free raffinate by maintaining the pH of the solution at 11 and the temperature at 95 °C for 30 min. The optimum conditions for the complete dissolution of LiFePO4 batteries by sulfuric acid solution and for the separation of iron and lithium ions from the leaching solutions were determined. A hydrometallurgical process was proposed for the recovery of pure lithium phosphate from spent LiFePO4 batteries.
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record_format Article
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spelling doaj-art-0787c2c49e904e54b9b49b737fa667892025-02-03T08:18:20ZengUniversity of Belgrade, Technical Faculty, BorJournal of Mining and Metallurgy. Section B: Metallurgy1450-53392217-71752024-01-0160115316410.2298/JMMB231213013C1450-53392400013CRecovery of pure lithium phosphate from sulfuric acid leaching solutions of spent LiFePO4 batteries by solvent extraction and chemical precipitationChen J.0Tran T. T.1Lee M. S.2Department of Advanced Materials Science & Engineering, Mokpo National University, Chonnam, KoreaFaculty of Biological, Chemical and Food Technology, Can Tho University of Technology, Can Tho City, VietnamDepartment of Advanced Materials Science & Engineering, Mokpo National University, Chonnam, KoreaWith the increasing use of electric vehicles, the demand for lithium iron phosphate batteries (LiFePO4) has risen sharply. Therefore, the recycling of metals from these batteries at the end of their life is necessary. In this study, a hydrometallurgical process for the recovery of lithium phosphate from spent LiFePO4 batteries was developed. The effects of the parameters on the recovery process, consisting of leaching, solvent extraction, and precipitation were investigated. The addition of H2O2 to the H2SO4 solution was ineffective for the selective leaching of Li(I) over iron. The results showed that Li(I) and iron were completely dissolved by 1.5 mol/L H2SO4, 100 g/L pulp density at 25 °C for 60 min at 300 rpm. After oxidation of Fe(II) in the leaching solution by addition of H2O2, Fe(III) was completely separated from the solution by five steps of cross-flow extraction with 1.0 mol/L D2EHPA at room temperature. The loaded Fe(III) was successfully separated by four steps of cross-current stripping with 50% (v/v) aqua regia solution. Finally, most Li(I) was recovered by precipitation of lithium phosphate from the iron-free raffinate by maintaining the pH of the solution at 11 and the temperature at 95 °C for 30 min. The optimum conditions for the complete dissolution of LiFePO4 batteries by sulfuric acid solution and for the separation of iron and lithium ions from the leaching solutions were determined. A hydrometallurgical process was proposed for the recovery of pure lithium phosphate from spent LiFePO4 batteries.https://doiserbia.nb.rs/img/doi/1450-5339/2024/1450-53392400013C.pdfspent lifepo4 batteryrecoverysolvent extractionprecipitationlithium
spellingShingle Chen J.
Tran T. T.
Lee M. S.
Recovery of pure lithium phosphate from sulfuric acid leaching solutions of spent LiFePO4 batteries by solvent extraction and chemical precipitation
Journal of Mining and Metallurgy. Section B: Metallurgy
spent lifepo4 battery
recovery
solvent extraction
precipitation
lithium
title Recovery of pure lithium phosphate from sulfuric acid leaching solutions of spent LiFePO4 batteries by solvent extraction and chemical precipitation
title_full Recovery of pure lithium phosphate from sulfuric acid leaching solutions of spent LiFePO4 batteries by solvent extraction and chemical precipitation
title_fullStr Recovery of pure lithium phosphate from sulfuric acid leaching solutions of spent LiFePO4 batteries by solvent extraction and chemical precipitation
title_full_unstemmed Recovery of pure lithium phosphate from sulfuric acid leaching solutions of spent LiFePO4 batteries by solvent extraction and chemical precipitation
title_short Recovery of pure lithium phosphate from sulfuric acid leaching solutions of spent LiFePO4 batteries by solvent extraction and chemical precipitation
title_sort recovery of pure lithium phosphate from sulfuric acid leaching solutions of spent lifepo4 batteries by solvent extraction and chemical precipitation
topic spent lifepo4 battery
recovery
solvent extraction
precipitation
lithium
url https://doiserbia.nb.rs/img/doi/1450-5339/2024/1450-53392400013C.pdf
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