Zhou Miaomiao, Shen Ji, Zuo Yinze, Liu Ruiping, Zhao Jianjun, Zhou Guangmin
School of Chemical & Environmental Engineering, China University of Mining and Technology (Beijing), Beijing, 100083, China.
Institute for New Energy Materials and Engineering/College of Materials Science and Engineering, Fuzhou University, Fuzhou, 350108, PR China.
Angew Chem Int Ed Engl. 2025 Jan 10;64(2):e202414484. doi: 10.1002/anie.202414484. Epub 2024 Nov 11.
Hydrometallurgy remains a major challenge to simplify its complex separation and precipitation processes for spent lithium-ion batteries (LIBs). Herein, we propose a Fischer-lactonization-driven mechanism for the cascade reaction of leaching and chelation of spent LIBs. Citric acid undergoes a two-step dissociation of the carboxylic acid (-COOH) and complexes with the leached metal ion, while the residual -COOH is attacked by H protons to form a protonated carboxyl ion (-COO -). Subsequently, the lone pair of electrons in the hydroxyl of the same molecule attack the carbon atom in -COO - to facilitate ester bonding, leading to the formation of a lactonized gel. The leaching rates of Li, Ni, Co and Mn are 99.3, 99.1, 99.5 and 99.2 %, respectively. The regenerated monocrystalline LiNiCoMnO (NCM523) has a uniform particle size distribution and complete lamellar structure, with a capacity retention rate of 70.6 % after 250 cycles at 0.5 C. The mechanism achieves a one-step chelation reaction, and the energy consumption and carbon emissions are only 26 % and 44 %, respectively, of that of the conventional hydrometallurgical. The strategy achieves a double breakthrough in simplifying the process and improving environmental friendliness, offering a sustainable approach to the re-utilization of spent LIBs.
湿法冶金要简化其用于废旧锂离子电池(LIBs)的复杂分离和沉淀过程仍然是一项重大挑战。在此,我们提出了一种费歇尔内酯化驱动的机制,用于废旧LIBs的浸出和螯合的级联反应。柠檬酸经历羧酸(-COOH)的两步解离并与浸出的金属离子络合,而残留的-COOH被H质子攻击形成质子化羧基离子(-COO -)。随后,同一分子羟基中的孤对电子攻击-COO -中的碳原子以促进酯键形成,导致形成内酯化凝胶。Li、Ni、Co和Mn的浸出率分别为99.3%、99.1%、99.5%和99.2%。再生的单晶LiNiCoMnO(NCM523)具有均匀的粒度分布和完整的层状结构,在0.5 C下循环250次后的容量保持率为70.6%。该机制实现了一步螯合反应,能耗和碳排放量分别仅为传统湿法冶金的26%和44%。该策略在简化工艺和提高环境友好性方面实现了双重突破,为废旧LIBs的再利用提供了一种可持续的方法。