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废旧锂离子电池回收——亚硫酸钠对阴极废料中金属的还原氨浸出

Spent lithium-ion battery recycling - Reductive ammonia leaching of metals from cathode scrap by sodium sulphite.

作者信息

Zheng Xiaohong, Gao Wenfang, Zhang Xihua, He Mingming, Lin Xiao, Cao Hongbin, Zhang Yi, Sun Zhi

机构信息

Division of Environment Technology and Engineering, Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100190, China.

Division of Environment Technology and Engineering, Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100190, China; National Engineering Research Center of Distillation Technology, School of Chemical Engineering and Technology, Tianjin University, Tianjin 300072, China.

出版信息

Waste Manag. 2017 Feb;60:680-688. doi: 10.1016/j.wasman.2016.12.007. Epub 2016 Dec 18.

Abstract

Recycling of spent lithium-ion batteries has attracted wide attention because of their high content of valuable and hazardous metals. One of the difficulties for effective metal recovery is the separation of different metals from the solution after leaching. In this research, a full hydrometallurgical process is developed to selectively recover valuable metals (Ni, Co and Li) from cathode scrap of spent lithium ion batteries. By introducing ammonia-ammonium sulphate as the leaching solution and sodium sulphite as the reductant, the total selectivity of Ni, Co and Li in the first-step leaching solution is more than 98.6% while it for Mn is only 1.36%. In detail understanding of the selective leaching process is carried out by investigating the effects of parameters such as leaching reagent composition, leaching time (0-480min), agitation speed (200-700rpm), pulp density (10-50g/L) and temperature (323-353K). It was found that Mn is primarily reduced from Mn into Mn into the solution as [Formula: see text] while it subsequently precipitates out into the residue in the form of (NH)Mn(SO)·HO. Ni, Co and Li are leached and remain in the solution either as metallic ion or amine complexes. The optimised leaching conditions can be further obtained and the leaching kinetics is found to be chemical reaction control under current leaching conditions. As a result, this research is potentially beneficial for further optimisation of the spent lithium ion battery recycling process after incorporating with metal extraction from the leaching solution.

摘要

废旧锂离子电池的回收因其含有高含量的有价金属和有害金属而备受关注。有效回收金属的难点之一是浸出后从溶液中分离不同金属。本研究开发了一种完整的湿法冶金工艺,用于从废旧锂离子电池的正极废料中选择性回收有价金属(镍、钴和锂)。通过引入氨 - 硫酸铵作为浸出液和亚硫酸钠作为还原剂,第一步浸出液中镍、钴和锂的总选择性超过98.6%,而锰的选择性仅为1.36%。通过研究浸出试剂组成、浸出时间(0 - 480分钟)、搅拌速度(200 - 700转/分钟)、矿浆密度(10 - 50克/升)和温度(323 - 353K)等参数的影响,详细了解了选择性浸出过程。发现锰主要以[化学式:见原文]的形式从锰还原进入溶液,随后以(NH)Mn(SO)·HO的形式沉淀到残渣中。镍、钴和锂被浸出并以金属离子或胺配合物的形式留在溶液中。可以进一步获得优化的浸出条件,并且发现在当前浸出条件下浸出动力学为化学反应控制。因此,本研究对于将浸出液中的金属提取纳入后进一步优化废旧锂离子电池回收工艺具有潜在的益处。

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