Lithium slag leach solution refining by hydroxide precipitation

Lithium-ion batteries contain many of critically important metals and their effective recycling is key to the EU’s sustainable development. In the past, only metals such as Co, Ni, and Cu were recycled by pyrometallurgy, while Li and Al were concentrated in the slags and not further processed. The n...

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Main Authors: Klimko J., Takacova Z., Marcinov V., Piroskova J., Vindt T., Liptai P., Orac D.
Format: Article
Language:English
Published: University of Belgrade, Technical Faculty, Bor 2023-01-01
Series:Journal of Mining and Metallurgy. Section B: Metallurgy
Subjects:
Online Access:https://doiserbia.nb.rs/img/doi/1450-5339/2023/1450-53392300042K.pdf
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author Klimko J.
Takacova Z.
Marcinov V.
Piroskova J.
Vindt T.
Liptai P.
Orac D.
author_facet Klimko J.
Takacova Z.
Marcinov V.
Piroskova J.
Vindt T.
Liptai P.
Orac D.
author_sort Klimko J.
collection DOAJ
description Lithium-ion batteries contain many of critically important metals and their effective recycling is key to the EU’s sustainable development. In the past, only metals such as Co, Ni, and Cu were recycled by pyrometallurgy, while Li and Al were concentrated in the slags and not further processed. The novel approach of pyrometallurgical treatment of the black mass offers the possibility of further hydrometallurgical utilization of the slags. This paper examines the refining of the solution obtained by leaching the slag in sulfuric acid. The most valuable element in the leach solution is Li, but it also contains Al, Si, Co, Mn, Ni and Cu, which must be removed before high-purity Li recovery is possible. Purification is achieved by adjusting the pH by adding NaOH. The results confirm that Al and Mn can be removed by 100%, Si by 93.56%, Cu by 86.36% and Cu by 61.75%. The results also confirmed that solution refining by the adding NaOH causes lithium losses ranging from 10% at pH 7 to 28% at pH 12. Therefore, it is suggested that further solution refining methods should be combined before precipitating pure Li2CO3 with minimal losses.
format Article
id doaj-art-58475a2752c84e6ca12c3ac960f5938b
institution Kabale University
issn 1450-5339
2217-7175
language English
publishDate 2023-01-01
publisher University of Belgrade, Technical Faculty, Bor
record_format Article
series Journal of Mining and Metallurgy. Section B: Metallurgy
spelling doaj-art-58475a2752c84e6ca12c3ac960f5938b2025-02-02T05:24:29ZengUniversity of Belgrade, Technical Faculty, BorJournal of Mining and Metallurgy. Section B: Metallurgy1450-53392217-71752023-01-0159348949610.2298/JMMB231020042K1450-53392300042KLithium slag leach solution refining by hydroxide precipitationKlimko J.0Takacova Z.1Marcinov V.2Piroskova J.3Vindt T.4Liptai P.5Orac D.6Technical University of Košice, Faculty of Materials, Metallurgy and Recycling, Institute of Recycling Technologies, Kosice, SlovakiaTechnical University of Košice, Faculty of Materials, Metallurgy and Recycling, Institute of Recycling Technologies, Kosice, SlovakiaTechnical University of Košice, Faculty of Materials, Metallurgy and Recycling, Institute of Recycling Technologies, Kosice, SlovakiaTechnical University of Košice, Faculty of Materials, Metallurgy and Recycling, Institute of Recycling Technologies, Kosice, SlovakiaTechnical University of Košice, Faculty of Materials, Metallurgy and Recycling, Institute of Recycling Technologies, Kosice, SlovakiaTechnical University of Košice, Faculty of Materials, Metallurgy and Recycling, Institute of Recycling Technologies, Kosice, SlovakiaTechnical University of Košice, Faculty of Materials, Metallurgy and Recycling, Institute of Recycling Technologies, Kosice, SlovakiaLithium-ion batteries contain many of critically important metals and their effective recycling is key to the EU’s sustainable development. In the past, only metals such as Co, Ni, and Cu were recycled by pyrometallurgy, while Li and Al were concentrated in the slags and not further processed. The novel approach of pyrometallurgical treatment of the black mass offers the possibility of further hydrometallurgical utilization of the slags. This paper examines the refining of the solution obtained by leaching the slag in sulfuric acid. The most valuable element in the leach solution is Li, but it also contains Al, Si, Co, Mn, Ni and Cu, which must be removed before high-purity Li recovery is possible. Purification is achieved by adjusting the pH by adding NaOH. The results confirm that Al and Mn can be removed by 100%, Si by 93.56%, Cu by 86.36% and Cu by 61.75%. The results also confirmed that solution refining by the adding NaOH causes lithium losses ranging from 10% at pH 7 to 28% at pH 12. Therefore, it is suggested that further solution refining methods should be combined before precipitating pure Li2CO3 with minimal losses.https://doiserbia.nb.rs/img/doi/1450-5339/2023/1450-53392300042K.pdflithium-ion batteryrecyclinghydrometallurgyprecipitationhydroxidelithium hydroxide
spellingShingle Klimko J.
Takacova Z.
Marcinov V.
Piroskova J.
Vindt T.
Liptai P.
Orac D.
Lithium slag leach solution refining by hydroxide precipitation
Journal of Mining and Metallurgy. Section B: Metallurgy
lithium-ion battery
recycling
hydrometallurgy
precipitation
hydroxide
lithium hydroxide
title Lithium slag leach solution refining by hydroxide precipitation
title_full Lithium slag leach solution refining by hydroxide precipitation
title_fullStr Lithium slag leach solution refining by hydroxide precipitation
title_full_unstemmed Lithium slag leach solution refining by hydroxide precipitation
title_short Lithium slag leach solution refining by hydroxide precipitation
title_sort lithium slag leach solution refining by hydroxide precipitation
topic lithium-ion battery
recycling
hydrometallurgy
precipitation
hydroxide
lithium hydroxide
url https://doiserbia.nb.rs/img/doi/1450-5339/2023/1450-53392300042K.pdf
work_keys_str_mv AT klimkoj lithiumslagleachsolutionrefiningbyhydroxideprecipitation
AT takacovaz lithiumslagleachsolutionrefiningbyhydroxideprecipitation
AT marcinovv lithiumslagleachsolutionrefiningbyhydroxideprecipitation
AT piroskovaj lithiumslagleachsolutionrefiningbyhydroxideprecipitation
AT vindtt lithiumslagleachsolutionrefiningbyhydroxideprecipitation
AT liptaip lithiumslagleachsolutionrefiningbyhydroxideprecipitation
AT oracd lithiumslagleachsolutionrefiningbyhydroxideprecipitation