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June 2, 2026Advanced Functional Materials0 citations

Selective Interfacial Repair Enables Low‐Energy Regeneration of Spent LiFePO 4 to High‐Performance Cathode

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YYYajing YuShanghai University of Electric PowerSGShuaiqi GongMinistry of Public Security of the People's Republic of China晨何晨旭 何Shanghai University of Electric Power

Key Points

  • This research aims to develop a low-energy method for regenerating degraded LiFePO4 cathodes in a sustainable manner.
  • Utilized air pre-oxidation at 500°C to remove carbon/binder and convert Li-deficient olivine.
  • Applied hydrothermal treatment with ascorbic acid for selective Fe3+ reduction and Li+ replenishment.
  • Conducted technology-economic analysis to evaluate energy consumption and profitability.
  • Regenerated OR-LFP provides an initial capacity of 155.7 mAh g−1 at 0.1 C and 147.1 mAh g−1 at 1 C.
  • Maintained 94.5% capacity after 500 cycles at 1 C and 93.8% at 5 C.
  • Required only 5.87 MJ kg−1 energy and yielded approximately $0.80 kg−1 profit, indicating over tenfold higher profitability than conventional methods.

Abstract

ABSTRACT Recycling degraded LiFePO 4 (LFP) cathodes via conventional pyro‐ (pyrometallurgy) or hydro‐ (hydrometallurgy) is energy‐intensive, generates toxic emissions, and yields meagre profits. Here, we report a low‐energy oxidation‐reduction (O‐R) strategy that bypasses element separation: air pre‐oxidation (500°C) removes carbon/binder, converting lithium‐deficient olivine into Li 3 Fe 2 (PO 4) 3 /Fe 2 O 3 intermediates; hydrothermal treatment with ascorbic acid enables selective Fe 3+ reduction (adsorption energy −2. 98 eV) and concurrent Li + replenishment. This reconstructs the lattice, halves Fe‐Li antisite defects (4. 38% to 2. 00%) and lowers Li + migration activation energy to 54. 48 kJ mol −1. Regenerated OR‐LFP delivers an initial capacity of 155. 7 mAh g −1 at 0. 1 C and 147. 1 mAh g −1 at 1 C, retains 94. 5% capacity after 500 cycles at 1 C and 93. 8% at 5 C, and shows superior rate capability. Technology‐economic analysis reveals O‐R requires only 5. 87 MJ kg −1 (less than half the energy of hydro‐ or pyro‐) and yields ≈0. 80 kg −1 profit, over tenfold higher than conventional routes, with minimal CO 2 emission. The process uses existing hydrothermal reactors and moderate‐temperature furnaces, enabling feasible industrial scaling. This work bridges high‐performance cathode regeneration with circular‐economy viability for sustainable LIB recycling.

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Cite This Study

Yu et al. (2026) studied this question.

synapsesocial.com/papers/6a1e72cb30b38c64201b6007https://doi.org/10.1002/adfm.76162
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