化工进展 ›› 2025, Vol. 44 ›› Issue (10): 6032-6041.DOI: 10.16085/j.issn.1000-6613.2024-1351

• 资源与环境化工 • 上一篇    

采用Versatic 10从废旧三元锂电池中回收锂及再生正极材料

李泽鹏1(), 刘翔2, 胡庆喜1(), 李金蓉1, 陈伟1   

  1. 1.华南理工大学制浆造纸工程国家重点实验室,广东 广州 510641
    2.广州市迈源科技有限公司,广东 广州 510700
  • 收稿日期:2024-08-19 修回日期:2024-10-24 出版日期:2025-10-25 发布日期:2025-11-10
  • 通讯作者: 胡庆喜
  • 作者简介:李泽鹏(2000—),男,硕士研究生,研究方向为废旧锂离子电池资源化利用。E-mail:591407422@qq.com
  • 基金资助:
    蒸发结晶杂盐固废资源化工艺研究横向项目(x2qs-D9214750)

Recovery of lithium from spent lithium-ion batteries and regeneration of cathode materials by Versatic 10

LI Zepeng1(), LIU Xiang2, HU Qingxi1(), LI Jinrong1, CHEN Wei1   

  1. 1.State Key Laboratory of Pulp and Paper Engineering, South China University of Technology, Guangzhou 510641, Guangdong, China
    2.Guangzhou Maiyuan Technology Co. , Ltd. , Guangzhou 510700, Guangdong, China
  • Received:2024-08-19 Revised:2024-10-24 Online:2025-10-25 Published:2025-11-10
  • Contact: HU Qingxi

摘要:

有效回收废旧锂离子电池中的有价金属,有利于资源的合理利用和环境保护。为了缩短回收过程,直接获得高纯度的再生产品,本文提出了一种基于共萃取和共沉淀的过渡金属萃取、锂回收和正极材料再生新工艺。本文采用盐酸为浸出剂,使用新癸酸(Versatic 10)直接从浸出液中共萃取过渡金属并与锂分离。首先,分别考察了盐酸浓度、固液比、浸出温度、浸出时间对各金属浸出率的影响,以及萃取剂Versatic 10浓度、pH、萃取相比(O∶A)、萃取时间对各金属萃取率的影响。结果表明,盐酸浓度3mol/L、固液比0.02g/mL、温度80℃、时间60min的条件下,Li、Ni、Co、Mn浸出率分别为100%、99.7%、99.3%和99.7%。在Versatic 10体积分数40%、pH=7、相比(O∶A)为1∶1、温度25℃、时间6min的萃取条件下,经过两级萃取镍、钴和锰的总萃取效率分别达到97.47%、96.18%和98.05%。然后,通过沉淀法从萃余液中回收Li,得到纯度为99.2%的Li2CO3。最后,用0.4mol/L HCl反萃有机负载相,并通过共沉淀法从反萃液中直接再生正极材料LiNi1/3Co1/3Mn1/3O2,而不单独分离金属。所制备的可再生正极材料LiNi1/3Co1/3Mn1/3O2为微球形,不含任何杂质,符合国家LiNi1/3Co1/3Mn1/3O2生产标准。

关键词: 废旧三元锂电池, 浸取, 共萃取, 新癸酸(Versatic 10), 共沉淀, 再生, 回收

Abstract:

The effective recovery of valuable metals from waste lithium-ion batteries is beneficial to the rational utilization of resources and environmental protection. In order to shorten the recovery process and directly obtain high purity recycled products, a new process of transition metal extraction, lithium recovery and cathode material regeneration based on co-extraction and coprecipitation was proposed. In this paper, the transition metal was co-extracted from the leaching solution and separated from lithium by using hydrochloric acid as leaching agent and neo-decanoic acid (Versatic 10). The effects of hydrochloric acid concentration, solid-liquid ratio, leaching temperature and leaching time on the extraction rate of each metal were investigated, and the effects of extractant Versatic 10 concentration, pH, extraction ratio and extraction time on the extraction rate of each metal were investigated. The results showed that the leaching rates of Li, Ni, Co and Mn were 100%, 99.7%, 99.3% and 99.7%, respectively, under the conditions of hydrochloric acid concentration 3mol/L, solid-liquid ratio 0.02g/mL, acid leaching temperature 80℃ and acid leaching 60 minutes. The total extraction efficiency of cobalt, nickel and manganese after two-stage extraction was 97.47%, 96.18% and 98.05%, respectively, under the extraction conditions of 40% Versatic 10, pH=7, extraction ratio was 1∶1, temperature was 25℃ and time was 6 minutes. Then, the Li was recovered from the raffinate by precipitation method and the Li2CO3 with a purity of 99.2% was obtained. Finally, the organic supported phase was stripped with 0.4mol/L HCl and the cathode material LiNi1/3Co1/3Mn1/3O2 was regenerated directly from the stripping solution by coprecipitation without separate metal separation. The prepared renewable cathode material LiNi1/3Co1/3Mn1/3O2 was micro-spherical and did not contain any impurities, which met the national LiNi1/3Co1/3Mn1/3O2 production standard.

Key words: spent lithium-ion battery, leaching, co-extraction, neo-decanoic acid(Versatic 10), coprecipitation, regeneration, recovery

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