Streamlining Ni‐Rich LiNi <sub>x</sub> Mn <sub>y</sub> Co <sub>z</sub> O <sub>2</sub> Cathode Black Mass Purification for Direct Recycling and Upcycling through the Alkoxythermal Process

Abstract The rapid accumulation of end‐of‐life lithium‐ion batteries necessitates sustainable recycling pathways, particularly for the industry‐prominent nickel‐rich NCM (LiNi x Mn y Co z O 2 , x+y+z = 1, x&gt;0.8) materials. Direct recycling presents a promising solution but is hindered by the susceptibility of these materials to impurities, moisture, particle cracking, and thermal degradation, especially in hydrothermal relithiation methods. This study reveals that impurities lead to severe surface degradation in nickel‐rich NCM cathodes, resulting in critical material transformations during high‐temperature hydrothermal processes. To address these issues, the alkoxythermal (AT) process is introduced, a low temperature relithiation and purification strategy operating at 80 °C. Applied to nickel‐rich scrap, low‐nickel spent cathodes, and mixed‐stream materials, the process achieves relithiation of the crystal alongside majority fluorine impurity removal. The AT process is also successfully demonstrated on a 100‐gram batch of spent NCM (89% nickel) cathode black mass, showcasing its scalability. The resulting spent material post‐AT process is upcycled to a single‐crystal morphology, yielding a specific capacity of 196 mAh/g. With scalability, integration potential, and broad applicability, the AT process marks a significant advancement in direct recycling for nickel‐rich chemistries, addressing key challenges in sustainable battery material recovery.

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Publication Details

Journal
Advanced Energy Materials
Published
2025-04-21
DOI
https://doi.org/10.1002/aenm.202406083
Citations
7
Primary Topic
Extraction and Separation Processes
Type
article
Field-Weighted Citation Impact
4.99

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article

Streamlining Ni‐Rich LiNi x Mn y Co z O 2 Cathode Black Mass Purification for Direct Recycling and Upcycling through the Alkoxythermal Process

Duc Tran, M. Li, Christopher Potts, Jiao Lin et al.
7 citations
Advanced Energy Materials
Extraction and Separation Processes
4.99
article

Streamlining Ni‐Rich LiNi x Mn y Co z O 2 Cathode Black Mass Purification for Direct Recycling and Upcycling through the Alkoxythermal Process

Duc Tran, M. Li, Christopher Potts, Jiao Lin, Hongpeng Gao, Zheng Chen, Varun Gupta
article en
7 citations

Abstract

Abstract The rapid accumulation of end‐of‐life lithium‐ion batteries necessitates sustainable recycling pathways, particularly for the industry‐prominent nickel‐rich NCM (LiNi x Mn y Co z O 2 , x+y+z = 1, x&gt;0.8) materials. Direct recycling presents a promising solution but is hindered by the susceptibility of these materials to impurities, moisture, particle cracking, and thermal degradation, especially in hydrothermal relithiation methods. This study reveals that impurities lead to severe surface degradation in nickel‐rich NCM cathodes, resulting in critical material transformations during high‐temperature hydrothermal processes. To address these issues, the alkoxythermal (AT) process is introduced, a low temperature relithiation and purification strategy operating at 80 °C. Applied to nickel‐rich scrap, low‐nickel spent cathodes, and mixed‐stream materials, the process achieves relithiation of the crystal alongside majority fluorine impurity removal. The AT process is also successfully demonstrated on a 100‐gram batch of spent NCM (89% nickel) cathode black mass, showcasing its scalability. The resulting spent material post‐AT process is upcycled to a single‐crystal morphology, yielding a specific capacity of 196 mAh/g. With scalability, integration potential, and broad applicability, the AT process marks a significant advancement in direct recycling for nickel‐rich chemistries, addressing key challenges in sustainable battery material recovery.

Advanced Energy MaterialsVol. 15(46)
University of California San Diego (US)
U.S. Department of Energy, California Energy Commission
Openalex Percentile: Top 5%
Extraction and Separation Processes
4.99
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