Gui Chu
a,
Yu Huang
a,
William Hawker
*d,
Lianzhou Wang
*bc and
Xiaobo Zhu
*a
aCollege of Materials Science and Engineering, Changsha University of Science and Technology, Changsha, 410114, P. R. China. E-mail: xbzhu@csust.edu.cn
bNanomaterials Centre, School of Chemical Engineering, Australian Institute of Bioengineering and Nanotechnology, The University of Queensland, Brisbane, QLD 4072, Australia. E-mail: l.wang@uq.edu.au
cDept of Applied Biology and Chemical Technology, The Hong Kong Polytechnic University, Hung Hom, Kowloon, Hong Kong SAR, China
dPure Battery Technologies, Brisbane, QLD 4000, Australia. E-mail: will@purebatterytech.com
First published on 31st July 2025
Sustainable end-of-life management is crucial for widely used lithium-ion batteries (LIBs), particularly those employing high-energy and expensive nickel-rich layered oxides (NRLOs). Unlike other cathode active materials, NRLOs face higher production costs and exhibit more complex, severe degradation—including phase evolution, stoichiometric imbalance, surface contamination, and morphological damage—necessitating the development of efficient and high-value recycling technologies. Direct recycling including direct regeneration and direct upcycling offers promising closed-loop solutions specifically tailored to address these intricate structural and chemical changes. Regeneration restores original performance, while upcycling enhances properties through methods like compositional tuning, morphological control, doping, and surface engineering. This review uniquely contextualizes recent advances in the direct recycling of NRLOs by linking degradation analysis with recovery strategies. Despite significant progress, practical challenges in impurity management, process complexity, scalability, and economics remain. The discussion highlights future perspectives for developing efficient and sustainable NRLO direct recycling technologies.
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Fig. 1 Growing interest for direct recycling. (a) A forecasted demand of LIBs by their cathode chemistries. Reproduced under terms of the CC-BY license.1 Copyright 2023, Nature Publishing Group. (b) Amount of spent LIBs from EVs and storage from 2020 to 2040 based on data from the IEA Sustainable Development Scenario. Reproduced under terms of the CC-BY license.3 (c) Energy densities of different CAMs. (d) Cost breakdown of NCM523, NCM622, and NCM811. (e) Recycling processes of retired NRLOs by hydrometallurgical, pyrometallurgical, and direct regeneration methods. Inset shows the annual publications relating to direct regeneration or upcycling from Web of Science. (f) CO2 emissions and (g) total energy consumption associated with the direct regeneration of NCM523, compared to other recycling processes and virgin material production. Reproduced under terms of the CC-BY license.20 Copyright 2023, Elsevier B.V. (h) Techno-economic analysis illustrating net recycling profits for pyrometallurgical, hydrometallurgical, and direct recycling routes applied to EV batteries with various cathode chemistries in the US and China. Reproduced under terms of the CC-BY license.21 Copyright 2021, Elsevier B.V. |
Central to LIBs is the cathode active material (CAM), which governs battery performance, cost, and environmental impact.4,5 CAMs are typically lithiated transition metal (TM) compounds categorized by their crystal structure into major types, including layered oxides (e.g., LiCoO2 (LCO), LiNixCoyMn1−x−yO2 (NCM), LiNixCoyAl1−x−yO2 (NCA), Li-rich Mn-based layered oxides), spinel oxides (e.g., LiMn2O4 (LMO), LiNi0.5Mn1.5O4 (LNMO)), and olivine-type phosphates (e.g., LiFePO4 (LFP), LiFexMn1−xPO4 (LFMP)).6,7 Currently, the commercial CAMs are dominated by NCM/NCA and LFP due to their intensive use in EV batteries. While LFP is notable for its cost efficiency and electrochemical/thermal stability, NCM/NCA offers superior energy densities.8,9 For example, as the Ni content increases, the energy density rises from 564.1 Wh kg−1 for NCM111 (LiNi1/3Co1/3Mn1/3O2) to 619.4 Wh kg−1 for NCM523 (LiNi0.5Co0.2Mn0.3O2) and 764.7 Wh kg−1 for NCM811 (LiNi0.8Co0.1Mn0.1O2), compared to 517.1 Wh kg−1 for LFP (Fig. 1c).10 NCM/NCA containing ≥50% nickel in transition metals (TMs) are generally classified as Ni-rich layered oxides (NRLOs).11 This advantage in energy density makes NRLOs indispensable for weight- and volume-sensitive applications, particularly long-range EVs.12,13 As illustrated in Fig. 1a, NRLOs are projected to continue dominating battery demand in the foreseeable future.
However, the widespread adoption of NRLOs is hindered by both economic and technical challenges. High production costs stem from the elevated prices of nickel (∼18 USD kg−1), comparable to cobalt (∼24 USD kg−1), as well as the reliance on lithium hydroxide (LiOH), a more expensive Li source than lithium carbonate (Li2CO3) used for the production of lower-Ni cathodes.14 Additionally, the synthesis of NRLOs often necessitates oxygen-rich atmosphere rather than ambient air to maintain high-valence Ni states and suppress Ni2+/Li+ cation mixing, further driving costs upward.11,15 Fig. 1d presents the current prices of three representative NRLOs,16 along with the breakdown of raw material cost contributions. It is evident that as the Ni content increases from NCM523 to NCM811, a significant portion of the overall cost rise stems not only from raw materials but also from increased processing requirements. Their high reactivity with ambient moisture further necessitates stringent environmental controls during storage and handling, adding to operational costs.17–19 Performance degradation during storage and battery cycling is another limitation of NRLOs. These materials undergo a series of irreversible transformations including phase transitions (e.g., layered-to-spinel or rock-salt), particle fracturing, TM dissolution, lithium/oxygen loss, etc. Collectively, these degradation pathways accelerate capacity fade compared to LFP or lower-Ni CAMs, leading to premature battery retirement and amplifying both commercial and environmental concerns.
Currently, the dominant recycling approaches for spent LIBs—pyrometallurgy and hydrometallurgy—are designed primarily for elemental recovery.22–25 As schematically shown in Fig. 1e, pyrometallurgical processes involve high-temperature smelting that recovers Ni, Co, Cu, Li, Al as alloys or in slag, requiring further extraction and purification. Hydrometallurgical methods, in contrast, use leaching and solvent extraction to isolate target elements but generate significant secondary waste and reduce high-value CAMs to metal salt precursors. Although both are widely implemented, they fail to preserve the structure or electrochemical function of cathode materials, diminishing their value return.
In response to these limitations, direct regeneration—and more recently, direct upcycling—has emerged as a promising closed-loop recycling strategy aimed at restoring or even enhancing the structure and performance of spent cathode materials.26–34 As shown in the inset of Fig. 1e, a surge in related publications retrieved from the Web of Science database highlights growing research interest in the direct regeneration and upcycling of CAMs. Unlike conventional recycling routes that decompose materials into elemental constituents, direct regeneration and direct upcycling address specific degradation mechanisms—such as lithium loss, phase transitions, or surface contamination—through targeted post-treatment. Direct regeneration focuses on restoring the spent cathode to its original composition and structure, while direct upcycling intentionally modifies or upgrades its chemical or structural features to achieve improved performance. This capability is particularly significant for NRLOs, as upcycling offers a breakthrough pathway to mitigate their inherent challenges, such as high production costs and susceptibility to severe degradation, by transforming spent materials into higher-value, more robust products that can even surpass original performance baselines.35–37 These approaches enable the reuse of high-value cathode materials with significantly reduced environmental impact, energy consumption, and production cost. Taking NCM523 as an example, direct regeneration show clear advantages in terms of less greenhouse gas (CO2) emissions and energy consumption (Fig. 1f and g).20 As shown in Fig. 1h, techno-economic analysis also demonstrates the financial benefit of direct recycling over pyrometallurgical and hydrometallurgical methods, with direct recycling of NRLOs including NCM622, NCM811, and NCA proving much more profitable than for LFP and LMO.21 Given the rapid deployment of NRLOs and their considerable manufacturing expense, direct regeneration and upcycling represent especially compelling pathways for sustainable and economically viable cathode material recovery.
This review presents a comprehensive overview of recent advances in the direct regeneration and upcycling of NRLOs cathode materials. We begin by examining the key degradation mechanisms affecting NRLOs during storage and cycling—specifically phase evolution, stoichiometric imbalance, surface contaminations, and morphological damage. Unlike previous reviews detailing the degradation mechanisms,8,9,11,12,38,39 this work contextualizes these structural and chemical changes specifically in relation to the design and effectiveness of recovery strategies. Subsequently, we evaluate contemporary direct regeneration techniques—including solid-state sintering, hydro/solvothermal treatment, molten-salt fluxing, chemical lithiation, and electrochemical lithiation—assessing their efficacy in restoring both the structural integrity and electrochemical performance of spent NRLOs. Furthermore, we explore recent advances in direct upcycling, an approach that moves beyond simple restoration to actively enhance the properties of degraded CAMs. This strategy offers novel pathways to potentially mitigate intrinsic NRLO limitations by strategically leveraging the structural or chemical features present in the spent material itself, employing techniques such as compositional tuning, morphological reconstruction (e.g., single-crystallization), targeted elemental doping, and functional surface modifications. Finally, we identify the key challenges and outline future opportunities for advancing direct regeneration and upcycling technologies, aligning these developments with the growing imperative for sustainable LIB recycling and the establishment of closed-loop material flows within the battery industry.
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Fig. 2 (a) c-Lattice variation of NCM811 alongside its dQ/dV profile. Reproduced under terms of the CC-BY license.41 Copyright 2015, IOP Publishing Limited. (b) Schematic illustration of phase evolution in NRLOs. Reproduced under terms of the CC-BY license.40 Copyright 2024, Springer Nature. |
From a chemical perspective, Ni4+ in H3 or even the O1 phase of fully delithiated TMO2 is unstable that increases the covalent character of Ni–O bonds. This facilitates electron transfer from lattice oxygen (O2−) to Ni4+, leading to the oxygen release from the lattice and the reduction of Ni4+ back to the more stable Ni2+ state.43,44 Owing to their similar ionic radii (r(Ni2+) ≈ r(Li+)), these newly formed Ni2+ ions tend to migrate into vacant lithium sites within the layered structure. This cation mixing, coupled with lattice densification, transforms the ordered layered arrangement into electrochemically inactive spinel or rock-salt phases (Fig. 2b).40 Such phase evolution is particularly prominent near the particle surface, exacerbated by high states of charge during cycling.45–47 Additionally, analogous phase evolution can occur during ambient storage via surface reduction of Ni3+, generating NiO-like rock-salt phase independent of electrochemical processes.48
These newly formed phases are electrochemically inert and lack continuous pathways for Li+ diffusion, which degrades battery performance (e.g., capacity loss, increased impedance) and physically hinders lithium reinsertion during subsequent regeneration attempts. Consequently, effective direct regeneration strategies must aim to reverse these structural transformations and recover electrochemical activity by reconstructing the desired layered framework. Beyond mere restoration, direct upcycling approaches may integrate structural stabilization mechanisms—such as engineering the grain boundaries, inducing single-crystal morphology, or incorporating specific dopants—to suppress subsequent phase transitions during operation, thereby offering the potential to exceed the original performance baseline and extend the cycle life of the recycled material.
For severely degraded NRLOs, successful regeneration therefore necessitates not only the replenishment of lost lithium but often also the precise assessment and rebalancing of the TM composition, typically achieved by supplementing deficient elements (e.g., adding Ni sources during relithiation) in appropriate ratios. Direct upcycling leverages this need for compositional control not just for restoration but as an opportunity for targeted performance enhancement. For instance, strategies can involve intentionally increasing the Ni content, introducing specific stabilizing dopants during the regeneration process, or potentially even harnessing beneficial impurity elements already present within the reclaimed “black mass”. These approaches aim to boost specific capacity, improve thermal/structural stability, or impart other desirable properties, thereby shifting the objective from simple repair towards value-added material engineering.
Once NRLOs are assembled into an LIB, additional surface contamination occurs via the dynamic formation and evolution of the cathode–electrolyte interphase (CEI). The CEI is a complex, heterogeneous layer composed of various organic species (e.g., lithium alkyl carbonates, lithium alkoxides, polymers) and inorganic species (e.g., LiF, Li2CO3, TM fluorides, and LixPFyOz) resulting from electrolyte oxidation and decomposition reactions at the cathode surface.53 While a thin, stable, and ionically conductive CEI can initially passivate the surface from further electrolyte decomposition, excessive or uncontrolled buildup leads to increased interfacial impedance, hindered Li+ transport kinetics, and continuous consumption of active materials (both Li and TM).
During direct recycling workflows, surface contaminants—particularly persistent fluorine- and phosphorus-containing species derived from the CEI—often remain adsorbed on or embedded within the reclaimed black mass. These residues can be trapped within particle cracks, along grain boundaries, or inside internal voids, making their complete removal by simple washing procedures challenging. As a result, they can inadvertently become uncontrolled elemental impurities in the final regenerated NRLOs. From an upcycling perspective, however, there is emerging interest in whether these deeply integrated species could potentially be leveraged for functional benefit. For example, elements like fluorine, if accurately quantified and strategically retained or incorporated in a controlled manner, might theoretically enhance surface passivation or improve thermal stability. However, realizing such benefits demands precise compositional analysis, rigorous process control, and a thorough understanding of the distribution and chemical states of impurities. Without careful management, these same impurities are far more likely to induce undesirable side reactions and increase interfacial resistance, compromising the electrochemical performance of the regenerated material. Therefore, upcycling strategies aiming to harness embedded impurities must be grounded in robust characterization, well-calibrated processing, and potentially adaptive design frameworks to ensure the reliability and consistency of the final NRLO products.
The development of cracks can lead to particle fragmentation. The loss of electrical contact between fragments and the conductive matrix/current collector results in capacity decay. Furthermore, the formation of cracks facilitates electrolyte infiltration deep into the particle interior. This accelerates parasitic side reactions along the newly exposed surfaces, leading to further TM dissolution, gas generation, and the formation of thick, resistive CEI layers that impede Li+ transport along the crack surfaces. Collectively, these chemo-mechanical degradation effects drive rapid structural and interfacial deterioration, ultimately resulting in accelerated capacity fade and premature battery failure. It is noteworthy that even NRLO materials designed as “single-crystals” (intended to eliminate intergranular cracking observed in polycrystalline aggregates) can still suffer from intragranular fractures under demanding conditions,55,57,59,60 highlighting the difficulty in combating this mechanical degradation of NRLOs.
Therefore, effective direct regeneration strategies must ideally address existing mechanical damage, for instance, through high-temperature annealing aimed at sintering microcracks. However, even successful regeneration processes may leave behind or introduce other structural imperfections—such as tilt boundaries, stacking faults, and residual lattice strain—inherited from the spent material or resulting from the treatment itself. These defects can act as stress concentration points, compromising the long-term mechanical stability of the regenerated material by increasing its susceptibility to fracture during subsequent cycling.61,62 Consequently, merely repairing apparent cracks may be insufficient. Addressing this persistent challenge often necessitates moving towards upcycling approaches for enhanced mechanical robustness. This requires continued innovation in developing crack-tolerant material architectures (e.g., core–shell structures, concentration gradients), advanced interface engineering techniques (e.g., protective coatings), and precisely controlled synthesis/regeneration protocols designed to minimize detrimental defects. Such advancements are essential to enable the reliable and sustainable reuse of high-performance NRLOs in next-generation LIBs.
As summarized schematically in Fig. 3, the degradation of NRLOs involves a complex interplay of phase instability, stoichiometric deviation, surface reactions, and mechanical failure, presenting a significantly more multifaceted challenge compared to other cathode chemistries like LFP or LiCoO2 (LCO). Consequently, the rejuvenation of degraded NRLOs requires a holistic approach that addresses not only the replenishment of lost lithium but potentially also the restoration of the layered crystal structure, readjustment of TM stoichiometry, removal or conversion of surface contaminants, and healing of mechanical damage. This complexity underscores the formidable challenges faced in developing robust, efficient, and economically viable direct regeneration and upcycling processes specifically tailored for NRLO materials.
Initial studies established the fundamental feasibility of regenerating NRLOs via solid-state routes. For instance, Zhou et al.66 demonstrated that employing a two-step calcination protocol (500 °C for 5 h followed by 900 °C for 12 h) with lithium acetate as the lithium source effectively restored the electrochemical properties of degraded NCM523. Similar outcomes were reported using other lithium precursors like LiOH·H2O67 and Li2CO368 for the regeneration NCM523. A primary challenge frequently encountered, however, is the presence of electrochemically inactive impurity phases, particularly rock-salt NiO, formed during degradation. These phases possess poor ionic conductivity and can significantly impede the solid-state diffusion of Li+ ions during the annealing process. This kinetic limitation often necessitates extended heating durations or higher calcination temperatures, which can, in turn, lead to undesirable consequences such as particle coarsening, increased levels of Li/Ni cation mixing, and compositional or structural heterogeneity within the regenerated material.
To address these kinetic limitations and enhance the efficiency and homogeneity of solid-state regeneration, various process modifications and pretreatment strategies have been investigated.
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Fig. 4 Strategies for solid-state regeneration of NRLOs. (a) Schematic illustrating how mechanical activation can induce defects and provide driving force for Li migration. Reproduced with permission.71 Copyright 2025, Wiley-VCH. (b) Concept of catalytic structural healing by co-adding fresh TM hydroxide precursor. Reproduced with permission.73 Copyright 2004, American Chemical Society. (c) Enhanced particle coating and reduced thermodynamic barrier using a liquid amyloxylithium precursor. Reproduced with permission.74 Copyright 2024, Nature Publishing Group. (d) Rapid acid solution pretreatment to remove F-rich surface impurities hindering Li+ diffusion. Reproduced with permission.76 Copyright 2025, Royal Society of Chemistry. (e) Solvent-free pretreatment via flash Joule heating (impurity removal, decomposition) followed by magnetic separation (carbon removal). Reproduced under terms of the CC-BY license.77 Copyright 2024, Nature Publishing Group. |
Despite these advancements and strategic modifications, solid-state regeneration methods applied to NRLOs continue to face inherent constraints. The diffusion of lithium within the solid phase remains comparatively slow and susceptible to heterogeneity, particularly when impeded by structural defects or surface impurity layers. This kinetic constraint can result in non-uniform lithium replenishment across particles or within individual particles, leading to variability and potentially suboptimal electrochemical performance in the regenerated products. Furthermore, achieving precise control over the final Li/TM stoichiometry is paramount for optimizing NRLO performance but presents significant challenges due to the often substantial and variable stoichiometric deviations present in retired NRLO feedstocks, coupled with the difficulty in accurately quantifying these deviations beforehand.78 Beyond restoring the average composition and primary crystal structure, residual nanoscale defects—such as Li/Ni cation disorder (antisite defects) and nanoporosity resulting from incompletely healed microcracks or phase transformations—warrant careful consideration.79 The inheritance of these subtle defects could consequently continue to compromise the long-term cycling stability and overall electrochemical performance characteristics of the regenerated cathode materials.
The applicability of hydrothermal treatment for NRLO regeneration was demonstrated by Shi and coworkers.80 They investigated the regeneration of NCM111 and NCM523 using an aqueous LiOH solution. Their findings indicated that the NCMs necessitated higher hydrothermal processing temperatures (220 °C) to achieve effective relithiation compared to LCO (which required only 180 °C) (Fig. 5a). This difference was ascribed to potentially slower lithiation kinetics in NCM materials, possibly arising from a higher intrinsic degree of Li/Ni cation mixing. Furthermore, for the higher-Ni NCM523 composition, annealing under an oxygen-rich atmosphere was essential to facilitate the complete transformation of residual rock-salt impurity phases back into the desired layered structure.
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Fig. 5 Hydrothermal and solvothermal regeneration approaches for NRLOs. (a) Illustration of temperature dependence (NCM vs. LCO) on hydrothermal relithiation. Reproduced with permission.80 Copyright 2018, American Chemical Society. (b) Schematic of additive-assisted (e.g., H2O2, ethanol) low-temperature hydrothermal relithiation of NCM. Reproduced with permission.81 Copyright 2022, Elsevier B.V. (c) Hydrothermal pretreatment using ammonium hydroxide solution to convert surface rock-salt/spinel phases into a hydroxide intermediate, facilitating subsequent thermal regeneration. Reproduced with permission.83 Copyright 2023, American Chemical Society. (d) Ethanol-based solvothermal regeneration designed to suppress reverse lithium dissolution. Reproduced with permission.84 Copyright 2024, Elsevier B.V. |
Seeking to mitigate the high-temperature requirement, Chen and coworkers81 explored the addition of reducing agents—specifically ethanol, hydrogen peroxide, or ethylene glycol—into the aqueous lithium precursor solution during hydrothermal treatment. This innovative modification enabled the successful relithiation of NCM111 and NCM622 materials at a significantly lower temperature of 100 °C (Fig. 5b). Intriguingly, in another study, H2O2 was identified as a necessary oxidizing agent required to re-oxidize Ni2+ species back to the desired Ni3+ state within the layered structure, thereby repairing structural defects of degraded NCM622.82 This apparent contradiction in the reported function of H2O2 highlights the complexity of the underlying redox chemistry occurring during hydrothermal regeneration and underscores the critical need for more precise mechanistic investigations to fully comprehend the role of various additives in facilitating NRLO restoration.
Hydrothermal treatment has also been strategically employed as a pretreatment step to modify the surface of degraded materials, thereby facilitating subsequent high-temperature regeneration processes. Zhou's team83 developed a pretreatment protocol using ammonium hydroxide solution. This treatment was designed to chemically transform the inactive rock-salt or spinel phases present on the surface of spent NCM523 particles into a layered Ni0.5Co0.2Mn0.3(OH)2 intermediate phase (Fig. 5c). This surface conversion was shown to significantly improve the efficiency of Li+ transport during the subsequent high-temperature solid-state regeneration step.
Furthermore, a significant challenge within aqueous hydrothermal systems stems from the intrinsic sensitivity of NRLOs towards water as discussed above. Exposure to the aqueous medium can lead to lithium leaching from the structure and surface degradation, counteracting the relithiation effort. In response to these issues related to aqueous processing, Zhou et al.84 investigated a solvothermal approach utilizing a saturated ethanol solution of LiNO3 for the treatment of degraded NCM at 150 °C (Fig. 5d). The use of ethanol, a non-aqueous solvent with a lower boiling point than water, not only generated higher system pressure at a comparatively lower temperature but, more importantly, effectively suppressed the reverse dissolution of lithium ions due to the lower solubility of lithium salts in ethanol compared to water. This resulted in improved overall lithium retention within the regenerated cathode material. Ionic liquids (ILs) represent another category of alternative, proton-free solvents that have been considered for solvothermal-type processes. In pioneering work by Dai and colleagues,85 an IL was employed as a fluxing solvent in conjunction with LiBr as the lithium source to regenerate delithiated NCM111 via a process termed “ionothermal” treatment. While demonstrating feasibility for lower-Ni NCM, the application of ionothermal methods specifically for the relithiation of higher Ni content NRLOs has not yet been reported. Furthermore, it should be noted that many ILs are associated with relatively high production costs, which might potentially limit the economic scalability of ionothermal regeneration methods for widespread industrial application.
Presently, the successful and comprehensive regeneration of NRLOs with very high nickel content (e.g., NCM811 and beyond) using hydro/solvothermal methods remains an area with limited reported validation. The increased complexity of degradation mechanisms prevalent in these materials—including more severe phase transformations to rock-salt structures, higher degrees of cation disorder, and extensive formation of microcracks—coupled with their heightened sensitivity towards chemical attack or corrosion induced by protic solvents, likely impacts the full restoration via these techniques. Moreover, a practical constraint is that hydro/solvothermal regeneration protocols frequently necessitate a subsequent solid-state annealing step to achieve complete restoration of crystallinity, remove residual solvent species, and ensure phase purity. While necessary for optimal performance, this additional high-temperature step partially counteracts the primary potential advantages of hydro/solvothermal processing, namely lower energy consumption compared to direct solid-state sintering.
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Fig. 6 Molten salt methods for NRLO regeneration. (a) Relithiation using a binary LiNO3–LiOH eutectic system, often requiring post-annealing. Reproduced with permission.87 Copyright 2019, Wiley-VCH. (b) Low-temperature regeneration attempt with a LiI–LiOH eutectic system. Reproduced with permission.91 Copyright 2022, American Chemical Society. (c) Conversion of polycrystalline NCA to single crystals using a LiOH–Na2SO4 mixture. Reproduced with permission.92 Copyright 2023, Wiley-VCH. (d) Ternary molten salt system incorporating an organic Li salt for regenerating low state-of-health NCM523. Reproduced with permission.96 Copyright 2023, Wiley-VCH. |
To further minimize processing temperatures, Zhou's team91 explored a LiI–LiOH eutectic system, which is recognized as having one of the lowest melting points (approximately 200 °C) among common binary lithium salt combinations (Fig. 6b). While this allowed for initial treatment at a lower temperature, achieving effective recovery of NCM523 still necessitated the addition of small amounts of Co2O3 and MnO2 to the regeneration medium, aiding in the repair of defects related to Co and Mn, and required a subsequent high-temperature annealing step (850 °C for 5 h) for optimal performance restoration.
Beyond systems composed solely of lithium salts, eutectic mixtures incorporating sodium salts have attracted interest, potentially offering cost advantages and unique fluxing effects. Chen's group92 successfully employed a LiOH–Na2SO4 mixture to transform degraded polycrystalline LiNi0.88Co0.095Al0.025O2 (NCA88) particles into uniform single-crystal particles during regeneration. This morphological transformation significantly enhanced the structural stability and minimized voltage polarization during subsequent electrochemical cycling (Fig. 6c). In a related study, the same research group utilized a LiOH–NaCl eutectic medium to regenerate NCM811, reporting effective suppression of detrimental phase transitions and a consequent boost in cycling stability.93 These results underscore the potential role of sodium salts not merely as diluents to lower melting points but potentially as active fluxing agents that promote ion migration and facilitate particle healing processes alongside the primary lithium replenishment.
For potential cost reduction and leveraging different fluxing properties, the use of low-cost alkali metal salts has also attracted attention in complex molten systems. Deng et al.97 utilized a ternary KCl–KNO3–LiNO3 eutectic system for regenerating NCM523, incorporating conductive carbon into the mixture. The molten salt network was reported to enhance Li+ diffusion pathways and accelerate the relithiation kinetics. Wang et al.98 introduced a “reciprocal ternary molten salt” system composed of LiCl:
NaNO3
:
NaOH
:
NaCl (mass ratio 0.9
:
1.7
:
0.2
:
1.6), achieving relithiation below 300 °C. The eutectic system, containing dual cations (Li+/Na+) and multiple anions (Cl−, NO3−, OH−), served as both a lithium source and a highly charged flux, enabling oxygen-rich conditions and rapid phase recovery. The regenerated NCM622 demonstrated restored stoichiometry, a pure layered structure, and comparable electrochemical properties.
Molten salt methods, while demonstrating promise and versatility, face practical challenges. These include ensuring desired morphological evolution without negatively impacting kinetics or powder properties, the essential yet environmentally and economically challenging post-treatment removal of residual salts, and the increased complexity and energy consumption from subsequent high-temperature annealing often required for full restoration. In recent years, machine learning (ML) has emerged as a powerful tool to address some of these challenges, particularly in optimizing molten salt composition design. By establishing complex mapping relationships between molten salt components/properties (such as melting point, viscosity, and ion diffusion rate) and recrystallization effects (e.g., grain size, morphology, and phase purity), ML can accelerate the screening of optimal molten salt systems (e.g., specific eutectic salt ratios or additives).99–101 This capability allows for more precise control over crystal growth processes and can significantly improve recycling rates. Further advancements in ML models, supported by accessible and reliable experimental and computational databases, will be crucial for optimizing molten salt mixtures for desired thermophysical properties and extending their predictive capabilities beyond current limitations.
An early example by Wu et al.102 utilized specific polycyclic aryllithium compounds (e.g., pyrene–Li, perylene–Li). These organometallic reagents functioned dually as Li sources and reducing agents, reportedly enabling rapid relithiation (∼10 min) of various cathodes including LFP, LCO, and NCM622 under ambient conditions, with the added benefit of recyclable reagents, suggesting potential for sustainable processing. Further exploration has focused on utilizing redox mediators to facilitate electron transfer for lithiation. Expanding this concept, Ko et al.103 investigated other organic electron-donating molecules as mediators, including 5,10-dimethylphenazine, ferrocene, and N,N′-diphenyl-p-phenylenediamine. Employed in conjunction with standard Li salts in organic solutions, these mediators were carefully chosen based on their redox potentials to enable controlled, topotactic lithiation of a range of spent NRLOs including NCM622 and NCM811 within their stable voltage window at room temperature, thus offering another potentially scalable route (Fig. 7a). In addition, quinone-based molecules, such as 3,5-di-tert-butyl-o-benzoquinone (DTBQ), were also demonstrated as effective electron shuttles. A pre-formed Li-coordinated DTBQ complex dissolved in an organic solution was used to directly immerse and relithiate Li-deficient NCM622 electrodes (Fig. 7b).104
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Fig. 7 Chemical and electrochemical relithiation techniques. (a) Room-temperature chemical relithiation using organic electron-donating molecules. Reproduced with permission.103 Copyright 2024, Royal Society of Chemistry. (b) Schematic of DTBQ-mediated chemical relithiation of NCM622 electrodes. Reproduced with permission.104 Copyright 2025, Wiley-VCH. (c) Spontaneous electrochemical regeneration of NCM622 via galvanic coupling with the Al current collector as a sacrificial anode. Reproduced with permission.105 Copyright 2025, Wiley-VCH. (d) Non-conventional plasma electrolysis method generating reactive species for Li insertion and surface cleaning. Reproduced with permission.106 Copyright 2025, Elsevier B.V. |
While potentially effective for robust structures like LFP where Li deficiency is the primary degradation mode, chemical relithiation alone is often insufficient for highly degraded NRLOs. These materials frequently require a subsequent high-temperature annealing step to fully restore the ordered layered crystal structure and eliminate defect phases formed during cycling. This necessity increases process complexity and partially negates the primary energy-saving advantage of the low-temperature chemical treatment. Furthermore, practical implementation challenges persist regarding the reagents themselves. Many of the effective reagents are costly, reactive organic compounds, raising concerns about handling safety, stability, potential environmental impact from disposal or side reactions, and the efficiency and cost-effectiveness of reagent recycling. These factors currently limit the scalability and industrial viability of chemical relithiation, highlighting the critical need for the development of more benign, cost-effective, stable, and readily recyclable reagent systems, alongside robust and environmentally sound waste management protocols, to fully realize its potential for NRLO regeneration.
Several innovative electrochemical regeneration strategies have been reported. Song et al.105 developed a room-temperature electrochemical method leveraging spontaneous galvanic corrosion principles to restore Li-deficient NCM622 without external power. In their setup, the aluminum current collector, inherently present with the cathode material, served as a sacrificial anode (reducing agent) due to its electrochemical potential relative to the lithiated cathode (Al/Al3+ ≈ 1.37 V vs. Li/Li+). This spontaneous electrochemical couple drove the insertion of Li+ ions (present in the electrolyte) into the spent NCM622 cathode material (Fig. 7c), recovering electrochemical performance almost equivalent to that of the pristine material. In a distinct approach employing non-conventional electrochemical conditions, Beletskii et al.106 proposed a plasma electrolysis method for cathode regeneration. This technique involves generating electrical discharges directly within a liquid electrolyte containing the cathode material. The localized plasma zones create extreme conditions characterized by shock waves, high temperatures, and the formation of highly reactive species, including hydrogen atoms and solvated electrons. These synergistic physicochemical and electrochemical effects were reported to facilitate lithium reinsertion while simultaneously removing surface contaminants from composite LiMn2O4/NCM622 materials, leading to significant improvements in their power capability and cycling performance (Fig. 7d). Electrochemical methods have also proven useful specifically for surface restoration, particularly for NRLOs degraded by ambient air or moisture exposure. Wang et al.107 demonstrated that performing several initial galvanostatic charge–discharge cycles within a specific voltage window (3.0–4.5 V) could effectively decompose detrimental Li2CO3 residues formed on the cathode surface due to air exposure, thereby restoring the subsequent electrochemical performance in assembled cells.
Overall, electrochemical relithiation operates under mild conditions, potentially saving energy compared to thermal methods, and enables precise Li stoichiometry control without harsh chemical reducers. Its primary limitation, shared with chemical methods, is its focus on Li replenishment; it struggles to remove bulk impurities (NiO, spinel) or repair deep lattice disorder (TM loss, antisite defects). Therefore, post-annealing at high temperatures is frequently required for NRLOs to achieve full structural restoration, adding process steps and energy costs that diminish the low-temperature benefit. Achieving homogeneous lithiation, particularly within large particles or thick electrodes, and carefully managing cell electrochemistry to avoid side reactions remain additional practical challenges for this regeneration approach.
In this section, contemporary direct regeneration methodologies applied to spent NRLOs have been reviewed based on their processing environment. Solid-state sintering represents a widely explored thermal approach, effective for structural repair but often limited by slow solid-state diffusion and heterogeneity. Hydro/solvothermal and molten-salt methods leverage liquid environments to enhance mass transport and facilitate crystal repair under potentially milder conditions, offering versatility but facing challenges related to solvent/salt removal and the common requirement for post-annealing. In contrast, chemical and electrochemical lithiation offer lower-temperature alternatives primarily focused on lithium replenishment, but often struggle with comprehensive structural repair and impurity removal, frequently necessitating subsequent thermal treatment. While significant progress has been made in adapting these techniques for NRLOs by incorporating pre-treatment steps and process modifications, each method presents distinct trade-offs in terms of energy consumption, process complexity, scalability, and effectiveness in addressing the multifaceted degradation of high-nickel materials. A detailed comparison of the reported process parameters and electrochemical performance results across these different regeneration strategies is presented in Table 1.
Direct regeneration method | Cathode type | Procedure | Performance of regenerated materials | Ref. |
---|---|---|---|---|
Solid-state sintering | NCM523 | Mixed with CH3COOLi, then sintered in the process of 500 °C for 5 h and 900 °C for 12 h | 164.6 mAh g−1 at 0.1C and 147 mAh g−1 at 1C, 89.12% after 100 cycles at 1C | 66 |
NCM523 | Mixed with LiOH·H2O, then sintered at 550 °C for 6 h and 850 °C for 12 h in air | 161.25 mAh g−1 at 0.1C, 95.29% after 50 cycles at 0.5C | 67 | |
NCM523 | Mixed with Li2CO3 and then sintered at 850 °C for 12 h in air | 162.0 mAh g−1 at 0.1C, 91.9% after 100 cycles at 1C | 68 | |
NCM523 | Pretreated spent NCM523 was mixed with Li2CO3 by high-energy ball milling (400 rpm, 12 h, ethanol), then sintered at 950 °C | 140 mAh g−1 at 0.2C, 97% after 50 cycles at 0.2C | 69 | |
NCM523 | Pretreated spent NCM523 was mixed with LiOH·H2O by ball milling, then sintered at 500 °C for 2 h and 800 °C for 16 h | 174.26 mAh g−1 at 0.1C, 90% after 200 cycles at 0.5C | 71 | |
NCM523 | Mixed with LiOH and fresh polycrystalline Ni0.5Co0.2Mn0.3(OH)2 precursor, then sintered at 500 °C for 5 h and 900 °C for 2 h | 88.4% after 1000 cycles in a 1.3 Ah pouch cell | 73 | |
NCM523 | Pre-treatment of spent NCM523 and then sintered at 850 °C for 6 h in air | 170 mAh g−1 at 0.1C, 96.3% after 500 cycles at 1C in a 1.2 Ah pouch cell | 20 | |
NCM55 | Mixed with LiOH and sintered at 300 °C for 2 h and 750 °C for 8 h | 166 mAh g−1 at 0.1C, 94% after 100 cycles at 0.3C | 108 | |
NCM622 | Pre-oxidation of spent NCM 622 with Na2S2O8 and NaOH solution, then sintered at 850 °C in an oxygen-rich atmosphere for 5 h | 153.82 mAh g−1 at 1C, 94.74% after 100 cycles at 1C | 72 | |
NCM622 | Pre-coated of NCM622 with amyloxylithium solution, then sintered at 800 °C for 4 h | 80.5% after 500 cycles in a 1 Ah pouch cell | 74 | |
NCM70 | Mixed with Li2CO3 by ball milling, then sintered at 750 °C for 2 h | 168.4 mAh g−1 at 0.1C, 70.8% after 50 cycles at 0.1C | 70 | |
NCM70 | Sintered at 800 °C for 3 h under oxygen flow | 169.8 mAh g−1 at 1C, 90.2% after 100 cycles at 1C | 18 | |
NCA80 | Mixed with LiOH·H2O, then sintered in the pure oxygen at 750 °C for 2 h | 191.3 mAh g−1 at 0.1C, 90.1% after 100 cycles at 1C | 17 | |
NCM811 | Combined flash Joule heating (transiently reaching ∼2500 K) with magnetic separation, then mixed with Li2CO3 and sintered at 800 °C for 12 hours in air | Not given | 77 | |
NCM811 | Spent NCM811 was heat-treated at 600 °C, then mixed with LiOH·H2O and sintered at 750 °C for 15 h in oxygen | 162 mAh g−1 at 0.25C, 78% after 100 cycles at 0.25C | 78 | |
NCM83 | Pre-coating of NCM83 with biphenyl-Li solution, then sintered at 700 °C for 5 h in pure oxygen | 181.6 mAh g−1 at 0.5C, 80.7% after 150 cycles at 0.5C | 75 | |
NCM83 | The spent cathodes were ultrasonically washed in HNO3 diluent, then mixed with Li2CO3 and sintered at 850 °C for 10 hours in pure oxygen | 171.4 mAh g−1 at 0.1C, 91.7% after 100 cycles at 0.3C | 76 | |
NCM83 | Sintered with LiOH at 800 °C for 6 h | 196 mAh g−1 at 0.1C, 81.6% after 300 cycles at 0.1C | 79 | |
Molten-salt fluxing | NCM523 | Utilized a LiNO3–LiOH eutectic mixture for the relithiation under ambient pressure, then mixed with Li2CO3 and sintered at 850 °C for 4 h | 149.3 mAh g−1 and retained 90.2% of the initial capacity after 100 cycles at 1C | 87 |
NCM523 | Mixed with LiNO3–LiOH, sintered at 320 °C for 4 h and 850 °C for 4 h in air, then annealed at 600 °C for 6 h after washing and drying | 152.5 mAh g−1 and retained 86% of the initial capacity after 100 cycles at 0.2C | 88 | |
NCM523 | Mixed with LiOH–Li2CO3, sintered at 440 °C for 5 h and 850 °C for 12 h | 146.3 mAh g−1 and retained 89.06% of the initial capacity after 200 cycles at 1C | 90 | |
NCM523 | Mixed with eutectic salt (LiI, LiOH), Co2O3, and MnO2, heating at 200 °C for 4 h, then sintered at 850 °C for 5 h | 150 mAh g−1 at 0.1C, 80.9% after 200 cycles and 73% after 300 cycles at 0.5C | 91 | |
NCM523 | Sintered with ternary molten salts (LiNO3, LiOH, CH3COOLi) at 400 °C for 4 h; then annealed with Li2CO3 at 850 °C for 6 h under oxygen atmosphere | 160 mAh g−1 and retained 93.7% of the initial capacity after 100 cycles at 0.5C | 94 | |
NCM523 | Mixed with organic lithium salt-assisted eutectic salts (LiOH, LiNO3, C7H5LiO3), heating at 300 °C for 4 h, sintering at 850 °C for 6 h | 155.5 mAh g−1 at 0.1C with retention rate of 95.6% after 100 cycles | 96 | |
NCM523 | Mixed with ternary molten salts (KCl, KNO3, LiNO3) and conductive carbon, sintered at 750 °C for 12 h | 160 mAh g−1 at 0.2C with retention rate of 95.5% after 100 cycles | 97 | |
NCM523 | Eutectic molten salt reaction in LiOH, Li2CO3, LiNO3 at 500 °C for 5 h, and annealing at 950 °C for 10 h | 157 mAh g−1 at 0.1C, 91.7% after 100 cycles at 1C | 109 | |
NCM622 | Mixed with LiOH–Li2SO4, sintered at 900 °C for 20 h in oxygen, then annealed at 750 °C for 6 h in oxygen after washing and drying | 125.4 mAh g−1 and retained 99.4% of the initial capacity after 250 cycles at 1C | 89 | |
NCM622 | Mixed with molten salt (LiCl, NaNO3, NaOH, NaCl) and sintered at 750 °C for 5 h, then annealed at 60 0 °C for 2 h | 180 mAh g−1 and retained 87.5% of the initial capacity after 100 cycles at 0.1C | 98 | |
NCM811 | Mixed with LiOH, NaCl binary molten salt, sintering 850 °C for 15 h, then mixed with LiOH and annealed at 800 °C for 10 h under oxygen atmosphere after washing and drying | 180.1 mAh g−1 and retained 86.5% of the initial capacity after 200 cycles at 1C | 93 | |
NCA88 | Mixed with LiOH, Na2SO4 binary molten salt, and sintered at 750 °C for 10 h in air | 204.8 mAh g−1 at 0.1C, 85.1% after 250 cycles at 1C | 92 | |
NCM90 | Sintered with ternary molten salts (LiOH, Li2 CO3, LiNO3) at 300 °C for 15 min and 500 °C for 3 h, then mixed with Li salt and sintered at 850 °C for 6 h | 122.2 mAh g−1 at 1C with retention rate of 99.97% after 100 cycles | 95 | |
Hydro/solvothermal treatment | NCM523 | Hydrothermal treatment (220 °C) with LiOH solution, then washed with deionized water and sintered with Li2CO3 at 850 °C for 4 h in oxygen | 146.6 mAh g−1 at 1C, 88.9% after 100 cycles at 1C | 80 |
NCM523 | Hydrothermal treatment with LiOH solution and NH3·H2O at 180 °C for 6 h; then sintered with LiOH at 850 °C for 10 h | 167 mAh g−1 at 0.5C, 90% after 100 cycles and 75% after 250 cycles at 0.5C | 83 | |
NCM523 | Utilized saturated ethanol solution of LiNO3 for the treatment of degraded NCM at 150 °C, then sintered at 850 °C for 12 h | 146.2 mAh g−1 at 0.1C, 90.23% after 560 cycles at 1C | 84 | |
NCM55 | Hydrothermal re-lithiation is employed to create a lithium water-balance structure for spent NCM, mixed with LiOH and sintered at 500 °C for 4 h, then higher temperatures for 12 h in oxygen | 153.2 mAh g−1 at 1C with a retention of 84.5% after 100 cycles | 110 | |
NCM622 | Hydrothermal treatment (100 °C) with LiOH solution with addition of green additive (ethanol, hydrogen peroxide or ethylene glycol), then annealed in oxygen at 850 °C for 4 h | 175 mAh g−1 at 0.1C, 76% after 60 cycles at C/3 | 81 | |
NCM622 | Hydrothermal treatment (125 °C) with a saturated, high ionic strength (with hydrogen peroxide oxidizing agents), lithium aqueous solution, then sintered at 800 °C for 3 h | Not given | 82 | |
NCM622 | Hydrothermal treatment with LiOH solution at 220 °C for 4 h, then mixed with Li2CO3 and annealed at 850 °C for 4 h | 155 mAh g−1 at 0.1C, 98% after 100 cycles at C/3 | 111 | |
Chemical relithiation | NCM523 | Spent NCM was dispersed in a lithium-rich solution (residual lithium in graphite reacts with water) and reacted in a reactor at 220 °C, then mixed with Li2CO3 and sintered at 850 °C for 4 h | 163 mAh g−1 at 0.1C, 92.69% after 50 cycles at 0.5C | 112 |
NCM622 | Polycyclic aryl–lithium compounds (pyrene–Li and perylene–Li) served as both the reducing agent and Li donor to heal the Li loss in degraded cathodes under ambient temperature and pressure in 10 minutes | The initial discharge capacity recovered from 139.4 mAh g−1 to 165.4 mAh g−1 | 102 | |
NCM622 | Immersing Li-deficient cathode electrodes in Li-coordinated DTBQ solution | 178.2 mAh g−1 at 0.1C, 76.7% after 100 cycles at 0.1C in full cell | 104 | |
NCM622 | Organic redox mediators (5,10-dimethylphenazine, ferrocene, and N,N′-diphenyl-p-phenylenediamine) were used in conjunction with LiPF6 and LiTFSI in organic solutions | 177.7 mAh g−1 at 0.1C, 85.5% after 200 cycles at 0.5C | 103 | |
NCM811 | 202.3 mAh g−1 at 0.1C, 63.5% after 300 cycles at 0.5C | |||
Electrochemical relithiation | NCM622 | Spontaneous reduction was achieved using an aluminium collector as the spontaneous reducing agent (Al/Al3+ = 1.37 V vs. Li/Li+) | 177.3 mAh g−1 and 167.6 mAh g−1 at 0.1C in half cell and full cell, respectively | 105 |
NCM622 | Useing electrical discharge in a liquid to create localized plasma conditions—producing shock waves, high temperature, hydrogen atoms, and solvated electrons | 90 mAh g−1 at 0.1C and approximately 50 mAh g−1 at 3C, 90% after 500 cycles at 0.25C | 106 | |
NCA80 | Decomposition of air-induced Li2CO3 by introducing an electrostatic cycle of 3.0–4.5 V in the initial cycle | 126.7 mAh g−1 at 3C with a retention of 72.6% after 100 cycles | 113 |
Achieving homogeneous incorporation of the supplementary TMs throughout the existing particle structure is crucial for successful compositional upcycling. Molten salt methods are favored due to the facilitated mass transport in the liquid flux environment, which promotes the diffusion necessary for compositional homogenization alongside structural repair. Numerous studies have demonstrated this approach, successfully converting Ni-lean NCM111 to Ni-rich NCM622 and NCM811.114–116 The method has also been applied to NRLOs; for example, Qian et al.35 upcycled degraded polycrystalline NMC532 to single-crystal NCM66 and NCM811 by adding specific TM hydroxide precursors to a LiOH–Li2SO4 molten system. Similarly, Li et al.117 utilized a LiOH–Li2CO3 mixture with added NiCO3 and MnCO3 to convert degraded NCM523 into NCM712, achieving performance comparable to commercial counterparts (Fig. 8a). Kim et al.118 implemented a selective lithium extraction pre-treatment via chlorination on degraded NCM622, aiming to homogenize the starting material before proceeding with upcycling to single-crystal NCM811. Recently, Yoon et al.119 introduced a liquified-salts-assisted upcycling approach by using Ni(NO3)2·6H2O as both a Ni source and a eutectic component in combination with a LiOH–LiNO3 mixture. Aided by planetary centrifugal mixing, the mixture transformed into a liquidized environment for enhanced precursor integration and mass diffusion, enabling efficient conversion of spent NCM523 to single-crystal NCM811.
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Fig. 8 Compositional and morphological upcycling of NRLOs. (a) Compositional upcycling of NCM523 to NCM712 using molten salt with TM additives. Reproduced with permission.117 Copyright 2025, Royal Society of Chemistry. (b) Solid-state morphological upcycling of cracked polycrystalline NCM into single crystals after surface phase management Reproduced with permission.36 Copyright 2024, Wiley-VCH. |
Overall, compositional upcycling offers a chance to upgrade the formula, especially increasing the nickel fraction for higher capacity. However, achieving the target stoichiometry requires precise control of precursor addition and reaction conditions. Ensuring homogenous composition without inducing detrimental phase separation represents a difficulty, particularly for substantial compositional shifts.120 Also, the costs of processing and supplementary TM sources (especially virgin Ni salts) require economic considerations, which may impact the overall viability compared to simpler regeneration or hydrometallurgical routes.
While molten salts readily promote single-crystallization, solid-state annealing can also achieve morphological upcycling but requires careful management of kinetic barriers. Zhou et al.,121 for example, used segmental calcination for NCM622, suggesting that air passages formed in cracked particles during initial calcination aided lithium transport and structural remodeling from irregular collapsed morphologies to octahedral crystals. Fan et al.36 demonstrated a solid-state approach for severely cracked polycrystalline NCM111, NCM523, and NCM811. They identified the presence of surface rock-salt phases as a primary obstacle hindering crystal growth. By implementing a pre-sintering step to first revive this surface layer, subsequent high-temperature annealing successfully induced the reshaping of the fragmented particles into upcycled single-crystalline NRLOs with substantially improved capacity retention (Fig. 8b).
The control of crystal regrowth and morphological evolution during upcycling remains a significant technical challenge. The initial state and degree of degradation of the NRLO feedstock are often overlooked but inevitably influence the process kinetics and outcomes, adding variability. Moreover, while mechanically beneficial, excessively large single crystals can suffer from slow Li+ diffusion kinetics due to long pathways, impairing rate performance and potentially causing heterogeneous lithiation, strain, and fracture.57,122,123 Therefore, precise optimization of process parameters (temperature, time, atmosphere, salt chemistry etc.) is required. The goal is to achieve not just single-crystallinity, but also optimal particle size, morphology, density, and minimal internal defects.
An intriguing avenue within this technique involves the in situ utilization of impurity elements commonly found in the recovered black mass from dismantled LIBs. These impurities (e.g., Al and Cu from current collectors, Fe from casings, F and P from electrolyte decomposition) are often considered contaminants requiring removal.124,125 However, if their presence can be managed and their incorporation into the NRLO lattice managed effectively, they could potentially serve as beneficial dopants. Zhang's group37 explored this concept in a two-step regeneration of spent NCM523 using a molten salt reaction followed by thermal treatment. They simulated the incorporation of aluminum impurities as a dopant by Al removal and subsequent addition of Al particles. The electrochemical performance of the Al-doped regenerated NCM compared to regenerated NCM without Al showed improvement (Fig. 9a). Their further mechanistic studies suggested that this in situ Al doping could increase the diffusion barrier for Ni migration, thereby suppressing detrimental Li/Ni cation mixing during cycling of the regenerated NCM523.126
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Fig. 9 Doping strategies integrated with NRLO upcycling. (a) Proposed mechanism for Al doping suppressing Li/Ni mixing. Reproduced with permission.37 Copyright 2023, American Chemical Society. (b) Synergistic dual doping using Al and Cu sourced from current collector scrap. Reproduced with permission.127 Copyright 2023, Wiley-VCH. (c) Phosphate doping enabled upcycling of NCM523.128 Copyright 2021, Elsevier B.V. (d) Beneficial effects observed from low-concentration fluorine impurities on NCM622 properties. Reproduced with permission.129 Copyright 2023, American Chemical Society. |
Taking this concept further towards a closed-loop system, Zhou's team127 intentionally used Al powder and Cu(OH)2 converted from waste current collector debris as dopant sources during the molten salt upcycling of highly degraded polycrystalline NCM83. Their findings indicated a synergistic effect, with Al3+ preferentially occupying TM vacancies (strengthening bonding, reducing antisite defects) and Cu2+ occupying Li vacancies (supporting the layered structure, reducing distortion). This dual doping reportedly improved lattice stability, mitigated strain accumulation, stabilized surface oxygen, and enabled stable high-voltage (4.6 V) operation (Fig. 9b).
Beyond cationic doping, the incorporation of specific anions has also been investigated. Species like phosphate or fluoride ions can be intentionally introduced during the process or potentially derived from binder and electrolyte remnants (e.g., LiPF6 decomposition products). Fan et al.128 explored the benefits of phosphate doping during NCM523 regeneration. They suggested that incorporating the large PO43− polyanion, with its high electronegativity, could form strong bonds with TM cations (especially Ni), thereby reducing the degree of cation mixing within the layered structure (Fig. 9c). Separately, Zheng et al.129 investigated the impact of fluorine impurities, often present in recycled streams, on the repreparation of NCM622 via hydrometallurgical coprecipitation. This study found that low concentrations (up to 1 at%) of fluorine impurity beneficially modified surface chemistry (increasing the Ni2+ ratio) and induced particle porosity, enhancing bulk Li+ diffusivity and leading to improvements in specific capacity and cycling stability (Fig. 9d).
Integrating elemental doping into the direct regeneration/upcycling workflow presents a promising pathway for enhancing the performance and durability of recovered NRLO materials. While the in situ utilization of beneficial elements from inherent impurities is an intriguing possibility, directly leveraging the variable contaminants present in raw black mass remains challenging due to significant variations in impurity type, concentration, and chemical state. Consequently, most successful strategies to date focus on adding controlled amounts of dopant elements (sourced from virgin materials or purified recycled streams) to relatively clean, pre-treated spent NRLOs. Further research is demanded to optimize controlled additive doping methods and develop advanced strategies for the controlled utilization of specific inherent impurities, addressing feedstock variability to advance upcycling towards practical application.
A range of metal oxides have been explored for their protective effects in upcycling NRLOs. These oxides, such as MoO3,130,131 TiO2,132 La2O3,133 tend to react with surface residues or the NRLO surface itself to form Li-contained surface layers, permitting improved interfacial charge transfer and stability. For example, Tong et al.132 demonstrated the in situ formation of Li2TiO3 coating during molten salt regeneration of NCM523 using a TiO2 additive. The modification boosted charge transfer and inhibited TM dissolution. Recently, Zhou and colleagues134 proposed a channel-assisted regeneration strategy utilizing waste spinel LiMn2O4 (LMO). This approach was applied to spent NCM523 and extended to NCM811, reconstructing their surfaces into a 3-dimensional (3D) structure. This surface reconstruction facilitated efficient replenishment of lithium into the particle lattice, and the resulting 3D ion channels improved fast-charging performance. For NCM523, this resulted in regenerated material achieving a capacity retention rate of 87.9% after 500 cycles at 10C, with overall electrochemical performance significantly outperforming commercial materials (Fig. 10a). Oxide-type surface reconstruction is also applicable to humidity-degraded NRLO. For example, a La salt, La(NO3)3·6H2O, was proposed to scavenge residual Li/NiO impurities from degraded NCM811 to form a conductive La4NiLiO8 coating surfaces, allowing improved Li+ transport and durability.135 Recently, Chen et al.136 developed an Nb-assisted eutectic upcycling method for NCM523. During this process, Nb2O5 reacted with the degraded NCM to form a Li3Ni2NbO6 epitaxial layer. This layer effectively filled the grain boundaries, helping to maintain the microstructure and significantly enhancing structural recovery.
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Fig. 10 Surface modification strategies for NRLO upcycling. (a) Channel-assisted regeneration using waste LMO for surface reconstruction. Reproduced with permission.134 Copyright 2025, Wiley-VCH. (b) In situ LiF coating derived from CEI/PVDF. Reproduced with permission.137 Copyright 2021, Elsevier B. V. (c) Borate channel formation for enhanced relithiation. Reproduced with permission.140 Copyright 2024, Wiley-VCH. |
Beyond oxide coatings, fluorides,137 phosphates,138 borates,139,140 and silicates141 are also explored as protective barriers or functional layers during upcycling. Guo et al.137 combined hydrothermal and molten-salt annealing to regenerate the degraded NCM523, where LiF derived from CEI and PVDF binder in situ coated on the surface of the cathode (Fig. 10b). Ryu et al.138 treated spent NCM811 with (NH4)2HPO4 to form a nanoscale Li3PO4 coating from residual surface lithium, which protected against environmental degradation and parasitic reactions while improving Li+ migration. In another study. Zhou's team140 developed LiCo0.5Mn0.5BO3 (LCMB) channels applied to degraded NCM523, aiming to clear CEI and provide low-barrier pathways for faster relithiation (Fig. 10c). A Li4SiO4/SiO2 coating layered was used as structural regulators and protective layers against electrolyte corrosion for air-degraded NCM83.141
Despite demonstrated benefits, surface modification during NRLO upcycling remains challenging. Precisely controlling coating thickness, composition, and crystallinity during high-temperature processing is difficult, even when modifying pristine CAMs.142,143 The achievement of uniform and conformal coverage on particles with varied degradation levels becomes considerably more complex due to the unpredictable nature of variable residual impurities. Scalability further presents a significant concern. Addressing these multifaceted difficulties necessitates focused future investigation aimed at developing novel materials (especially those designed to interact favorably with or potentially utilize residual contaminants), optimizing in situ formation mechanisms and process control, enhancing coverage uniformity and adhesion on complex substrates, and devising cost-effective, scalable application techniques. Such advancements are vital for the practical implementation of surface modification as a key upcycling strategy for NRLOs.
These upcycling efforts extend beyond simple regeneration by incorporating intentional modifications to compositional tuning, morphological control, lattice doping, and surface engineering. Compositional upcycling focuses on adjusting the metal ratios, primarily increasing nickel content, to upgrade the material feedstock. Morphological upcycling seeks to transform particle shape, often targeting robust single-crystal structures from degraded polycrystals. Lattice doping introduces beneficial elements into the crystal structure to enhance properties, including exploring the potential of controlled impurity utilization. Surface modification aims to engineer protective or functional layers on the particle surface to improve interfacial stability and ion transport. Notably, these distinct upcycling strategies are often applied in combination to achieve synergistic outcomes. While common challenges include achieving precise control over the introduced modifications, effectively managing the variable impurities inherent in spent materials, and ensuring the scalability and economic viability of the processes. Despite these complexities, upcycling offers a compelling pathway for value addition in LIB recycling by leveraging aspects of the degraded material itself. Table 2 provides a detailed summary of reported research across these various upcycling strategies and their outcomes.
Upcycling method | Cathode type | Upcycling procedure | Result | Ref. |
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NCM523 → NCM66 and NCM80 | Mixed with Ni0.83Mn0.09Co0.08(OH)2 precursors, Li2SO4 and LiOH, then sintered at 900 °C for 5 h and 860 °C for 15 h | Single-crystal NCM66 (179 mAh g−1 at 0.1C, 95% retention at 1C after 200 cycles) | 35 | |
Single-crystal NCM80 (200 mAh g−1 at 0.1C, 85% retention at 1C after 200 cycles) | ||||
NCM523 → NCM712 | Utilized a LiOH–Li2CO3 mixture with added NiCO3 and MnCO3, heated under oxygen gas at 500 °C and 950 °C for 6 and 11 h, then sintered at 750 °C for 5 h after washing and drying | Single-crystal NCM712 (191 mAh g−1 at 0.1C, 91% retention at 0.5C after 100 cycles) | 117 | |
NCM622 → NCM811 | Implemented a selective lithium extraction pre-treatment via chlorination on spent NCM (550 °C 4 h), then sintered at 250 °C for 6 h, 860 °C for 15 h and 700 °C for 10 h | Single-crystal NCM811 (191.3 mAh g−1 at 0.2C, 81.4% retention at 1C after 300 cycles) | 118 | |
NCM811 | Mixed spent NCM with Ni(NO3)2·6H2O, LiOH, and LiNO3 by using a planetary centrifugal mixer, then sintered at 920 °C for 2 h and 760 °C for 8 h in flowing oxygen | Single-crystal NCM811 (198 mAh g−1 at 0.1C, 94.1% retention at 1C after 100 cycles) | 119 | |
Morphological upcycling | NCM622 | The pretreated spent NCM was mixed with Li2CO3 and pre-calcined at 200 °C and 500 °C for 3 h, respectively, and then calcined at 700–1000 °C for 10 h | Transformed from polycrystalline NCM622 to single-crystal NCM622 (151.4 mAh g−1 after 100 cycles at 0.2C with a capacity retention of 95.6% in full cell) | 121 |
NCM622 | Sintered with binary molten salt (LiOH, LiNO3) at 500 °C for 5 h and 850 °C for 11 h, then annealed at 750 °C for 5 h | Transformed from polycrystalline NCM622 to plate-like single-crystal NCM622 (155.1 mAh g−1 at 1C, 94.1% retention at 1C after 240 cycles) | 144 | |
NCM622 | Sintered with ternary molten salts (LiOH, Li2SO4·H2O, CH3COOLi) at 450 °C for 4 h; then annealing with LiOH at 750 °C for 10 h | Transformed from polycrystalline NCM622 to single-crystal NCM622 (83.3% at 1C after 200 cycles) | 145 | |
NCM523 | A mixture of polycrystalline NCM523 and Li2CO3 was pressed into 12 mm diameter pellets, annealed at 750 °C for 5 h and further calcined at 950 °C in air and oxygen | Single-crystal NCM523 (167 mAh g−1 at 0.1C, 93.5% retention at 1C after 150 cycles) | 36 | |
NCM811 | Polycrystalline NCM811 was treated with aqueous potassium persulfate, then mixed with Li2CO3 and sintered at 750 °C for 5 h, followed by further calcination at 850 °C in oxygen | Single-crystal NCM811 (191 mAh g−1 at 0.1C) | ||
Doping | Al-doped NCM523 | Mixed with Al particles and Li salt (LiNO3, LiOH), sintering at 300 °C for 4 h. After washing and drying, mixed with LiOH and annealed at 800 °C for 8 h | 158.6 mAh g−1 at 0.1C, 91.6 mAh g−1 at 5C, 89.6% retention after 200 cycles at 1C | 37 |
Al-doped NCM523 | The spent NCM material was thoroughly washed before subjected to a molten salt (LiNO3, LiOH) reaction (at 300 °C for 4 h) with a trace amount of Al, then sintered at 800 °C for 8 h | 129.7 mAh g−1 at 1C with a retention of 93.7% after 100 cycles in full cell | 126 | |
Phosphate-doped NCM523 | Mixed with LiOH, NiO, MnO2 and NH4H2PO4, calcined at 450 °C for 5 h and then heated to 850 °C and kept for 15 h in oxygen | 189.8 mAh g−1 at 0.1C, 83.2% after 300 cycles at 1C | 128 | |
F-doped NCM622 | The F-doped NCM622 precursor was prepared by co-precipitation, mixed with Li2CO3 and sintered at 450 °C for 5 h, then 850 °C for 18 h | 177 mAh g−1 at 0.05C, 98% after 100 cycles at 0.33C | 129 | |
Al–Cu co-doped NCM83 | Sintered with Al powder and Cu(OH)2 in ternary molten salt (LiOH·H2O, NaCl, KCl) at 500 °C for 3 h in oxygen, then 850 °C for 8 h | 91.1% retention after 200 cycles in a 1.2 Ah pouch cell | 127 | |
Coating | TiO2-coated NCM523 | Spent NCM523 was mixed with molten salt (LiOH, Li2CO3) and TiO2, then sintered at 450 °C for 9 h and 700 °C for 2 h | 150.6 mAh g−1 at 1C, 92% retention after 100 cycles at 1C | 132 |
LiMn2O4-coated NCM523 | Spent NCM523 was mixed with LiMn2O4 and citric acid (C6H8O7) and dissolved in 100 ml of deionized water, completely evaporated under an oil bath at 80 °C, then heated at 300 °C for 2 h, sintered at 500 °C for 2 h and 900 °C for 4 h | 151.6 mAh g−1 at 0.1C, 82.9% retention after 300 cycles at 0.5C | 134 | |
Li3Ni2NbO6-coated NCM523 | Degraded NCM523 was mixed with molten salt (LiOH·H2O, LiNO3) and heated at 300 °C for 4 h, washed, and further mixed with Nb2O5, followed by calcinating at 850 °C for 5 h in an oxygen | 183.13 mAh g−1 t 0.1C (3–4.5 V), 83.4% after 300 cycles at 1C | 136 | |
LiF-coated NCM523 | Spent NCM523 was dispersed in LiOH solution and hydrothermally treated (220 °C) for 3 h, then mixed with LiOH and sintered at 810 °C for 4 h in oxygen, annealed at 600 °C for 4 h in O2, and annealed at 810 °C for 6 h in air | 166.1 mAh g−1 at 0.1C, 90.8% retention for 500 cycles at 1C | 137 | |
LCMB-coated NCM523 | Spent NCM523 was dispersed in an ethanol solution of H3BO3, heated to complete evaporation, mixed with LiOH and sintered at 500 °C for 30 minutes and calcined at 850 °C for 2 h | 160 mAh g−1 at 0.1C, 78% retention at 0.5C after 300 cycles | 140 | |
LiAlO2-coated NCM | Sintered with Li2CO3 at 950 °C for 10 h, then mixed with Al isopropanol and LiOH, annealed at 500 °C for 5 h | 97.49% after 100 cycles of 0.2C charge/1C discharge cycling at 3.0–4.5 V | 146 | |
Li3PO4-coated NCM523 | Mixed with LiOH and (NH)4H2PO4, then annealed at 850 °C | 80% capacity retention at 1C after 100 cycles | 147 | |
MoO3-coated NCM55 | Purified NCM55 precursor mixed with LiOH and sintered at 450 °C in air for 4 h, then at 750 °C for 8 h | 184.2 mAh g−1 at 0.1C, 81% retention after 450 cycles at 0.5C | 148 | |
LiBO2-coated NCM622 | Spent NCM622 was dispersed in an aqueous LiOH solution and hydrothermally treated (220 °C), after washed and dried, mixed with Li2CO3 and sintered at 850 °C for 4 h in an oxygen. It was then dry chemically coated with H3BO3 and annealed at 300 °C for 5 h | 177 mAh g−1 at 0.1C, 92.3% retention at C/3 after 100 cycles | 139 | |
MoO3-coated NCM811 | Spent NCM811 dispersed in MoO3 solution, sintered at 480 °C for 5 h and 800 °C for 15 h | 86.5% retention at 1C after 100 cycles | 130 | |
LiLaO2-coated NCM811 | Spent NCM811 was mixed with LiOH and La2O3 with a ball-milled speed (400 rpm for 2 h), then sintered at 775 °C for 10 h and 800 °C for 10 h in oxygen | 208.8 mAh g−1 at 0.1C, 81.4% retention at 1C after 200 cycles | 133 | |
La4NiLiO8-coated NCM811 | The spent NCM811 was dispersed in an ethanol solution of La(NO3)3·6H2O, heated in an oil bath until the ethanol was completely evaporated, and then sintered at 700 °C for 6 h in oxygen | 210.4 mAh g−1 at 0.1C, 73.2% retention at 1C after 300 cycles | 135 | |
Li3PO4-coated NCM811 | Spent NCM811 is dispersed in an ethanol solution of (NH4)2HPO4, heated until the ethanol is completely evaporated, and then heat-treated in air at 400 °C for 5 h | 185 mAh g−1 at 0.5C, 96% retention at 0.5C after 100 cycles | 138 | |
Li3PO4-coated NCM811 | Spent NCM811 was dispersed in an ethanol solution of LiPO3, evaporated to dryness and sintered at 600 °C in oxygen for 6 hours, residual lithium impurities on the sample surface can be converted into a repair/coating layer | 198.3 mAh g−1 with a retention of 85.5% after 50 cycles | 149 | |
Li4SiO4/SiO2-coated NCM83 | Spent NCM83 and CH3COOLi were dissolved in N-methyl pyrrolidone (NMP), fully dried, and then NCM83 and C8H20O4Si were dissolved in NMP again, fully dried and then sintered at 700 °C for 4 h in oxygen | 199.94 mAh g−1 at 0.1C, 82.2% retention at 0.3C after 250 cycles | 141 |
While direct regeneration and upcycling methods inherently offer distinct advantages over traditional pyrometallurgical and hydrometallurgical routes—including their non-destructive nature, streamlined processes, reduced costs, and enhanced environmental profiles—a more granular comparison among these direct strategies themselves is necessary for guiding future development. To facilitate a comprehensive understanding, Table 3 provides a systematic comparison of the diverse direct recycling strategies detailed in Sections 3 and 4. This table meticulously outlines the key advantages and disadvantages intrinsic to each direct regeneration and upcycling technique. Crucially, it explicitly links each method to the main NRLO degradation mechanisms (as elucidated in Section 2) that it is most adept at addressing or the specific objective it aims to achieve, thereby enabling readers to discern the optimal approach for various degradation scenarios.
Methods | Advantages | Disadvantages | Main degradation/objective addressed | |
---|---|---|---|---|
Direct regeneration | Solid-state sintering | Effective structural repair; simple process; high scalability potential | High energy consumption; significant Li volatilization; risks of stubborn impurity phases and reaction heterogeneity | Stoichiometric imbalance; phase evolution; morphological damage |
Molten-salt fluxing | Enhanced ion diffusion kinetics; promoted element homogenization; facilitated recrystallization | Equipment corrosion; additional salt separation; morphological change | Stoichiometric imbalance; phase evolution; surface contamination; morphological evolution | |
Hydro/solvothermal treatment | Low-temperature processing; surface impurity removal; morphological preservation | Li redissolution; high water/solvent costs; limited bulk structural repair | Surface contamination; Li loss; minor structural defects | |
Chemical relithiation | Facile operation (liquid/solid phase); precise Li replenishment | High chemical costs; challenging by-product removal; limited bulk structural repair | Li loss; surface contamination (possible) | |
Electrochemical relithiation | Non-destructive structural repair; precise Li replenishment | Complex equipment; long processing cycles; low efficiency; high costs; difficult for continuous production | Li loss; surface contamination (possible) | |
Direct upcycling | Compositional upcycling | Higher energy density; high-value element reuse; high product value | Complex process design; demands precise compositional control; increased costs | Stoichiometric redesign |
Morphological upcycling | Healing of particle cracks/fractures; optimized ion diffusion pathways; enhanced mechanical stability | High technical complexity; low throughput; complex process design | Morphological damage | |
Upcycling with doping | Improved structural stability; suppressed phase transformation & O2 release; extended cycle life | Challenging uniformity control; potential specific capacity reduction | Surface contamination; phase evolution | |
Upcycling with coating | Less surface side reactions; extended cycle life | Coating may impede ion conduction; increases material resistance | Surface contamination; phase evolution |
Complementing this, Fig. 11 presents radar charts visually comparing these direct recycling methods across five key practical considerations: energy consumption, pollution emission, regeneration efficiency, scalability, and cost. It is important to note that for liquid-processing regeneration methods like hydro/solvothermal, chemical, and electrochemical approaches, the actual energy use, emission, and overall cost could be substantially higher than initially perceived due to the necessity of a subsequent re-annealing step. For the upcycling methodologies, while generally entailing higher cost and energy input due to the incorporation of additional chemicals or extended processes, they typically yield upcycled NRLOs that exhibit superior electrochemical performance and consequently, higher intrinsic value.
Direct regeneration has emerged as a promising closed-loop alternative that aims to restore the properties of spent CAMs by repairing chemical and structural degradations to recover original performance. This review systematically examined contemporary methods, including solid-state sintering, hydro/solvothermal treatment, molten-salt fluxing, chemical lithiation, and electrochemical lithiation, in regenerating NRLOs. Solid-state sintering is an established method, adaptable but facing kinetic limitations. Hydro/solvothermal and molten-salt methods leverage liquid environments for enhanced mass transport but often require complex multi-step processes involving post-treatment for solvent/salt removal. Lower-temperature chemical and electrochemical routes offer energy-saving potential but are currently primarily limited to lithium replenishment, often necessitating subsequent thermal annealing for full structural repair.
Extending beyond simple restoration, direct upcycling strategies target enhanced electrochemical performance by employing intentional modifications to the spent material. These approaches build upon regeneration techniques by incorporating strategic modifications such as compositional upgrades, morphological control, lattice doping, and surface engineering. These strategies are often applied in combination to achieve synergistic outcomes, leveraging aspects of the degraded material itself to impart improved or new functionalities and present a compelling pathway for value addition in LIB recycling.
While significant progress has been made in developing these direct recycling methods for NRLOs, their practical implementation and widespread adoption face considerable challenges. These include the effective and scalable management of varied impurities from reclaimed black mass, achieving precise control over the restoration or modification process amidst feedstock variability, ensuring scalability, and establishing economic viability. A comprehensive visual overview of the key stages and concepts discussed throughout this review is provided in Fig. 12. The diagram illustrates the journey from NRLO-based spent LIBs through the two primary direct recycling pathways: direct regeneration, aimed at restoring original performance, and direct upcycling, targeting enhanced performance. The figure also emphasizes the overarching challenges, such as feedstock variability, impurity stubbornness, process complexity, and scalability and economic concerns.
Building upon this comprehensive understanding and the challenges highlighted, the outlook ahead focuses on key areas for advancing NRLO direct recycling towards industrial reality. Future directions should prioritize:
(1) Efficient feedstock treatment: a significant challenge currently limiting the industrialization of direct regeneration and upcycling is the difficulty in obtaining a clean and consistent feedstock from commercial spent batteries. Unlike controlled laboratory settings, real-world black mass collected from diverse sources is often highly contaminated. This contamination manifests in two primary forms: cross-contamination from varying types of cathode materials within the same LIB stream (e.g., mixtures of LFP, NCM111, NCM523, NCM622, and NCM811) or even different battery chemistries entirely (e.g., lead-acid and nickel–cadmium batteries mixed alongside LIBs). Additionally, internal contamination stems from residual battery components like aluminum foil, binder, conductive carbon, polymer separators, residual electrolyte, anode components, and shell parts. Such mixed and impure feedstocks pose substantial obstacles, as direct recycling processes typically require a relatively pure and compositionally uniform input to effectively restore or upgrade the material.
Therefore, a crucial future direction involves the development of efficient and scalable pretreatment methods specifically designed to handle these complex, mixed waste streams. This includes exploring sophisticated sorting technologies to address cross-contamination, as well as delicate physical and chemical separation processes (e.g., magnetic separation, froth flotation, solvent immersion, molten salt melting, incineration) for internal component contaminants, which have been summarized elsewhere.150,151 Critically, the selection of pretreatment methods should ensure the preservation of the cathode structure, a fundamental requirement for direct recycling approaches.
(2) Innovative recycling methods: future efforts should focus on designing processes that intelligently leverage specific characteristics of the degraded feedstock and significantly improve the efficiency of key steps, such as achieving rapid and homogeneous relithiation and complete phase recovery. In terms of morphological control, while single-crystallization is extensively reported for regenerated NRLOs, the drawbacks of extended diffusion pathways and internal stress accumulation cannot be overlooked.55,152 Innovative methods must therefore aim for optimized particle morphologies, meticulously controlling crystal growth and minimizing adverse crystal defects to ensure the long-term reliability of reproduced materials.
(3) Development of computational tools: applying advanced computational tools, particularly ML and artificial intelligence (AI), holds significant potential for accelerating advancements in direct recycling.153 Unlike conventional computational methods, ML/AI excels at analyzing vast, high-dimensional datasets and identifying complex, non-linear relationships.154 This capability is particularly attractive for simulating degraded NRLOs with heterogeneous and compositionally varied degraded phases across multiple dimensions, enabling significantly faster screening of materials and optimization of processes from atomic-level interactions to macroscopic parameters.
The effectiveness of these tools, however, is critically dependent on the availability of reliable, comprehensive databases for training. These databases, ideally integrating both experimental data and reliable simulation data (e.g., from density functional theory (DFT) or molecular dynamics (MD) simulations), are essential for building robust models. When trained with such high-quality data, ML/AI techniques can effectively predict material behavior, forecast optimal recycling parameters, and even guide the de novo design of novel, highly efficient recycling routes and materials. For instance, ML has been successfully applied to optimize molten salt composition design by mapping properties like melting point, viscosity, and ion diffusion. This capability allows for accelerated screening of optimal salt systems and more precise control over crystal growth processes, which is crucial for complex phase reconstruction from degraded materials.
(4) Environmental friendliness Ensuring sustainability is critical throughout the entire direct recycling chain. This requires minimizing energy consumption, reducing chemical waste generation, and developing eco-friendly reagents and processes at every step.
(5) Scalability and economic viability: translating laboratory successes to industrial scale is a significant challenge. This necessitates designing cost-effective processes, optimizing resource utilization, improving process throughput, and conducting comprehensive techno-economic assessments to demonstrate commercial viability.
Advancing these technologies requires concerted efforts encompassing fundamental materials science, chemical engineering, and interdisciplinary collaboration. Ultimately, realizing robust and economically viable direct regeneration and upcycling of NRLOs is essential for closing the loop in the battery supply chain, enabling resource security and contributing to a sustainable energy future.
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