Hydrometallurgical Leaching of Metals from Button Batteries: Effect of the Citric Acid-to-Manganese Ratio on Extraction Efficiency

Sustainable recovery of critical metals from spent lithium-ion batteries requires high extraction efficiencies under mild conditions and elevated solid loadings. In this work, a citric acid-based hydrometallurgical system was investigated for manganese and lithium recovery from spent LiMnO 2 , focusing on the effect of the citric acid-to-manganese (CA:Mn) molar ratio at different solid-to-liquid (S/L) ratios. Experiments were conducted at 60 °C and 60 min, varying CA:Mn from 1.5 to 12.0 mol mol −1 and S/L from 7.5 to 30.0 g L −1 . Manganese extraction reached 96.0 ± 3.5%, 95.0 ± 2.6%, 91.4 ± 2.9%, and 85.0 ± 1.7% at S/L ratios of 7.5, 15.0, 22.5, and 30.0 g L −1 , respectively, at CA:Mn ratios between 4.5 and 9.0. Notably, high extraction efficiencies were maintained even at 30 g L −1 , demonstrating the effectiveness of molar ratio adjustment under intensified conditions. At higher S/L ratios and extreme CA:Mn values, the formation of a white precipitate suggests secondary phase formation and reprecipitation phenomena. Lithium extraction remained consistently high (> 90%), reaching ~ 95% across most conditions, with a slight decrease to 88.3 ± 0.3% at the lowest CA:Mn ratio and highest S/L ratio. These results demonstrate that tuning the CA:Mn ratio enables efficient metal recovery under mild conditions, providing a more sustainable alternative for battery recycling.

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Publication Details

Journal
Journal of Sustainable Metallurgy
Published
2026-08-26
DOI
https://doi.org/10.1007/s40831-026-01644-3
Primary Topic
Extraction and Separation Processes
Type
article
Field-Weighted Citation Impact
0.00

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article

Hydrometallurgical Leaching of Metals from Button Batteries: Effect of the Citric Acid-to-Manganese Ratio on Extraction Efficiency

Mayara Teixeira da Silva, Rafael Bruno Vieira, Miriam Maria de Resende, Victor Santos et al.
Journal of Sustainable Metallurgy
Extraction and Separation Processes
article

Hydrometallurgical Leaching of Metals from Button Batteries: Effect of the Citric Acid-to-Manganese Ratio on Extraction Efficiency

Mayara Teixeira da Silva, Rafael Bruno Vieira, Miriam Maria de Resende, Victor Santos, JOSÉ SEVERIANO MARCHIORI DE GOUVÊA, Vicelma Luiz Cardoso
article en

Abstract

Sustainable recovery of critical metals from spent lithium-ion batteries requires high extraction efficiencies under mild conditions and elevated solid loadings. In this work, a citric acid-based hydrometallurgical system was investigated for manganese and lithium recovery from spent LiMnO 2 , focusing on the effect of the citric acid-to-manganese (CA:Mn) molar ratio at different solid-to-liquid (S/L) ratios. Experiments were conducted at 60 °C and 60 min, varying CA:Mn from 1.5 to 12.0 mol mol −1 and S/L from 7.5 to 30.0 g L −1 . Manganese extraction reached 96.0 ± 3.5%, 95.0 ± 2.6%, 91.4 ± 2.9%, and 85.0 ± 1.7% at S/L ratios of 7.5, 15.0, 22.5, and 30.0 g L −1 , respectively, at CA:Mn ratios between 4.5 and 9.0. Notably, high extraction efficiencies were maintained even at 30 g L −1 , demonstrating the effectiveness of molar ratio adjustment under intensified conditions. At higher S/L ratios and extreme CA:Mn values, the formation of a white precipitate suggests secondary phase formation and reprecipitation phenomena. Lithium extraction remained consistently high (> 90%), reaching ~ 95% across most conditions, with a slight decrease to 88.3 ± 0.3% at the lowest CA:Mn ratio and highest S/L ratio. These results demonstrate that tuning the CA:Mn ratio enables efficient metal recovery under mild conditions, providing a more sustainable alternative for battery recycling.

Journal of Sustainable Metallurgy
Universidade Federal de Uberlândia (BR)
Coordenação de Aperfeiçoamento de Pessoal de Nível Superior, Universidade Federal de Uberlândia, Conselho Nacional de Desenvolvimento Científico e Tecnológico, Fundação de Amparo à Pesquisa do Estado de Minas Gerais
Responsible consumption and production
Openalex Percentile: Top 19%
Extraction and Separation Processes
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