Highly selective and near-complete electrochemical recovery of cobalt and nickel from spent batteries through multifunctional deep eutectic solvent

材料科学 共晶体系 深共晶溶剂 电化学 溶剂 阳极 氧化还原 过渡金属 化学工程 电池(电) 乙二醇 无机化学 金属 氯化物 成核 电化学电池 卤化物 分离过程 石油化工 电极
作者
Seongmin Choi,Kenta Motobayashi,Kwiyong Kim
出处
期刊:Energy Storage Materials [Elsevier BV]
卷期号:82: 104646-104646 被引量:8
标识
DOI:10.1016/j.ensm.2025.104646
摘要

• Ligand-assisted DES broadens Ni-Co separation via selective metal coordination • Low-overpotential regime enables selective Ni nucleation without Co deposition • Anodic redox chemistry induces in-situ self-purification in a single-chambered cell • Sequential electrodeposition enables selective Ni, Co, and Mn recovery • Technoeconomic analysis confirms the viability of the proposed recovery system Electrochemical recovery presents a sustainable route for battery recycling, yet it is hindered by a trade-off between achieving purity and yield. This challenge arises because, as the target metal depletes during electrodeposition, mass transport limitations reduce its availability, thereby shifting the electrochemical environment in favor of co-deposition of competing metal – particularly during prolonged deposition intended for near-complete recovery. Here, we report a strategy that leverages a multifunctional deep eutectic solvent (DES), ethaline, where ethylene glycol preferentially coordinates with nickel while chloride stabilizes cobalt as tetrachlorocobaltate complexes. Even at elevated temperatures, where nickel undergoes a partial thermochromic transition to chloride coordination, the system maintains a broadened Ni–Co separation window of ∼0.3 V at 85°C. By fine-tuning the applied potential and utilizing the intrinsic chlorine redox activity of the DES, self-purification was achieved during electrodeposition, yielding a Ni/Co separation factor >3,000 and >97% nickel recovery in a single-step electrodeposition from a synthetic Ni/Co mixture. Building upon this binary separation, we developed a sequential strategy to recover nickel, cobalt, and manganese from real battery leachates. Applied to real NMC leachates, our process enabled the sequential recovery of nickel, cobalt, and manganese with purities of 99.1%/96.3% (NMC111) and 99.2%/98.8% (NMC811) for nickel and cobalt, respectively, all with >95% recovery. For NMC111, >97% nickel purity and >93% cobalt purity were retained over repeated reuse of the DES, enabling minimal wastewater discharge, with Cl 2 -assisted refining enhancing purity to >99.9%. A technoeconomic analysis validated the economic feasibility and revealed further potential through thermal optimization.
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