Selective oxidative leaching of Li+ and utilization of FePO4 for regeneration of LiFePO4 cathode material

The recycling and regeneration processes of spent LiFePO 4 (SLFP) batteries have become a research hotspot due to their significant environmental and economic value. Current industrial recycling strategies for SLFP predominantly focus on improving lithium leaching rates, while paying less attention to the resulting ferric phosphate (FePO 4 ) solid residues, leading to the waste of iron and phosphorus resources. Herein, we propose a closed-loop process for selectively leaching lithium (Li) from spent LFP batteries and regenerating new LFP cathode materials using the FePO 4 from leaching residues. The spent LFP powder is co-ground in a combined hydrogen peroxide-citric acid (H 2 O 2 -H 3 Cit) solution system, with mechanical activation-assisted oxidative leaching, to achieve effective separation of lithium and iron under optimal conditions. The recovered FePO 4 was purified and used to prepare new LiFePO 4 cathode materials. The regenerated LiFePO 4 materials show good electrochemical properties, with the discharge capacity of 144.42 mA h g −1 at 1 C and the capacity retention rate of 95.94 % after 200 cycles. After undergoing high-rate charge/discharge at 5 C and returning to 0.1 C rate, the discharge specific capacity remains stable at 127.24 mA h g −1 . A closed-loop process route for spent LFP batteries consisting of "pretreatment-selective oxidative leaching-lithium carbonate and ferric phosphate (Li 2 CO 3 +FePO 4 )-regenerated LFP material" is established and it provides a reference idea and practical experience for the high-efficiency closed-loop development of LFP batteries.

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Publication Details

Journal
International Journal of Electrochemical Science
Published
2025-10-09
DOI
https://doi.org/10.1016/j.ijoes.2025.101201
Primary Topic
Extraction and Separation Processes
Type
article
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article

Selective oxidative leaching of Li+ and utilization of FePO4 for regeneration of LiFePO4 cathode material

Li Zhao, Changsong Dai, Chaoyue Yang, Wei Zhang et al.
International Journal of Electrochemical Science
Extraction and Separation Processes
article

Selective oxidative leaching of Li+ and utilization of FePO4 for regeneration of LiFePO4 cathode material

Li Zhao, Changsong Dai, Chaoyue Yang, Wei Zhang, X. Qi, Deying Mu
article en

Abstract

The recycling and regeneration processes of spent LiFePO 4 (SLFP) batteries have become a research hotspot due to their significant environmental and economic value. Current industrial recycling strategies for SLFP predominantly focus on improving lithium leaching rates, while paying less attention to the resulting ferric phosphate (FePO 4 ) solid residues, leading to the waste of iron and phosphorus resources. Herein, we propose a closed-loop process for selectively leaching lithium (Li) from spent LFP batteries and regenerating new LFP cathode materials using the FePO 4 from leaching residues. The spent LFP powder is co-ground in a combined hydrogen peroxide-citric acid (H 2 O 2 -H 3 Cit) solution system, with mechanical activation-assisted oxidative leaching, to achieve effective separation of lithium and iron under optimal conditions. The recovered FePO 4 was purified and used to prepare new LiFePO 4 cathode materials. The regenerated LiFePO 4 materials show good electrochemical properties, with the discharge capacity of 144.42 mA h g −1 at 1 C and the capacity retention rate of 95.94 % after 200 cycles. After undergoing high-rate charge/discharge at 5 C and returning to 0.1 C rate, the discharge specific capacity remains stable at 127.24 mA h g −1 . A closed-loop process route for spent LFP batteries consisting of "pretreatment-selective oxidative leaching-lithium carbonate and ferric phosphate (Li 2 CO 3 +FePO 4 )-regenerated LFP material" is established and it provides a reference idea and practical experience for the high-efficiency closed-loop development of LFP batteries.

International Journal of Electrochemical ScienceVol. 20(11)
Yichun University (CN), Harbin Institute of Technology (CN)
Openalex Percentile: Top 71%
Extraction and Separation Processes
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