首页|利用有机酸浸出系统从废旧磷酸铁锂中回收Li和Fe

利用有机酸浸出系统从废旧磷酸铁锂中回收Li和Fe

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采用湿法冶金从废旧LiFePO4正极粉末中回收有价金属锂和铁,回收产物作为原料制备磷酸铁锂.通过优化浸出工艺参数,在丙酮酸浓度为3.0mol/L、H2O2体积为2mL、固液比为0.1 g/mL、反应温度为80 ℃以及反应时间为20 min的条件下,Li的浸出效率达到96.56%.采用XRD、XPS、FE-SEM和EDS对浸出残渣进行表征.结果表明,浸出残渣为FePO4,Fe/P摩尔比为0.974.将浸出液的pH值调整到12.0,并在80 ℃搅拌2 h后,浸出液中的Li通过原位沉淀以Li3PO4形式回收,其纯度为96.5%(质量分数).丙酮酸/H2O2溶液浸出Li的反应动力学数据符合Avrami模型(R2>0.95).Li浸出过程的活化能较低,表明扩散限制浸出过程中的反应速率.
Recovery of Li and Fe from spent lithium iron phosphate using organic acid leaching system
The valuable metals,lithium and iron,were recovered from spent LiFePO4 cathode powder by hydro-metallurgy,and the recycled products were used as raw materials for the preparation of lithium iron phosphate.By the optimization of the leaching process parameters,the leaching efficiency of Li reached 96.56%at pyruvic acid concentration of 3.0 mol/L,volume of H2O2 of 2 mL,solid-to-liquid ratio of 0.1 g/mL,reaction temperature of 80 ℃,and reaction time of 20 min.The leached residue was characterized by XRD,XPS,and FE-SEM coupled with EDS,and the results showed that the leached residue was FePO4 with an Fe/P molar ratio of 0.974.After adjusting the pH of the leaching solution to 12.0 and stirring for 2 h at 80 ℃,the recovery of Li from the leaching solution was enabled by in-situ precipitation in the form of Li3PO4 with a purity of 96.5 wt.%.The reaction kinetic data of Li leaching using the pyruvic acid/H2O2 solution were fit to the Avrami model with R2>0.95.The low activation energy of the Li leaching process indicated that diffusion step limited the reaction rate during the leaching process.

spent LiFePO4pyruvic acidleaching kineticsAvrami modellithium ion batteries

王亚辉、伍继君、胡国琛、马文会

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昆明理工大学冶金与能源工程学院,昆明 650093

昆明理工大学真空冶金国家工程实验室,昆明 650093

废旧磷酸铁锂 丙酮酸 浸出动力学 Avrami模型 锂离子电池

Talent Training Program of Yunnan Province,ChinaMajor R&D Project of Yunnan Province of China

202005AC 160041202002AB0800020102

2024

中国有色金属学报(英文版)
中国有色金属学会

中国有色金属学报(英文版)

CSTPCD
影响因子:1.183
ISSN:1003-6326
年,卷(期):2024.34(1)
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