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Volume 30 Issue 5
May  2023

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Yingnan Yang, Yingjie Yang, Chunlin He, Yuezhou Wei, Toyohisa Fujita, Guifang Wang, Shaojian Ma,  and Wenchao Yang, Solvent extraction and separation of cobalt from leachate of spent lithium-ion battery cathodes with N263 in nitrite media, Int. J. Miner. Metall. Mater., 30(2023), No. 5, pp. 897-907. https://doi.org/10.1007/s12613-022-2571-8
Cite this article as:
Yingnan Yang, Yingjie Yang, Chunlin He, Yuezhou Wei, Toyohisa Fujita, Guifang Wang, Shaojian Ma,  and Wenchao Yang, Solvent extraction and separation of cobalt from leachate of spent lithium-ion battery cathodes with N263 in nitrite media, Int. J. Miner. Metall. Mater., 30(2023), No. 5, pp. 897-907. https://doi.org/10.1007/s12613-022-2571-8
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研究论文

N263在亚硝酸盐介质下从废锂离子电池正极材料浸出液中萃取分离钴

  • 通讯作者:

    何春林    E-mail: helink1900@126.com

文章亮点

  • (1) N263在NaNO2体系中选择性配位高效萃取分离Co(II)。
  • (2) 萃取过程萃取剂和钴形成的络合物为[R4NCo(NO2)3]。
  • (3) 钴的反萃率超过97.70%显著提高钴的纯度。
  • (4) 在废锂离子电池材料实际浸出液中Co(II)的萃取效率达到100%。
  • 随着废锂离子电池数量的不断增多,对废锂离子电池材料中钴金属的分离回收成为了近年来的研究热点。为了高效、高选择性地分离回收废锂离子电池正极材料浸出液中的Co(II),本文基于亚硝酸根的选择性配位和Co(II)形成络阴离子的特点,采用了季铵盐N263作为萃取剂在亚硝酸钠体系中对Co(II)进行选择性分离回收。结果表明,当萃取条件为55vol%磺化煤油,30vol% N263和15vol%异丙醇组成的有机相,水相和有机相的体积比(A/O)为2:1,萃取时间为30 min,温度为25°C,0.1 M HNO3和1 M亚硝酸钠时,Co(II)的萃取效率最高达到99.16%,而Ni(II)、Mn(II)和Li(I)的萃取效率仅为9.27%–9.80%。采用FT-IR、XPS、UV探究了N263与Co(II)的相互作用机制。研究发现,溶液中${\rm{NO}}_2^- $与Co(II)选择性结合形成阴离子络合物[Co(NO2)3],并通过N263中的Cl进行离子交换,最终溶液中的Co(II)被萃取到有机相中。根据McCabe–Thiele结果显示,当Co(II)浓度为2544 mg/L时,经过三段逆流萃取后Co(II)的萃取效率能够达到99.00%以上。在反萃实验中,当盐酸浓度为1.5 M,水相与有机相的体积比为1:1时,Co(II)的反萃取效率为91.41%。萃取剂N263经过5次萃取和反萃取循环后,Co(II)的萃取效率仍然可以达到93.89%。另外,在废锂离子电池材料实际浸出液中,可实现对Co(II)100%的高效萃取。
  • Research Article

    Solvent extraction and separation of cobalt from leachate of spent lithium-ion battery cathodes with N263 in nitrite media

    + Author Affiliations
    • To effectively separate and recover Co(II) from the leachate of spent lithium-ion battery cathodes, we investigated solvent extraction with quaternary ammonium salt N263 in the sodium nitrite system. N${\rm{O}}_2^- $ combines with Co(II) to form an anion [Co(NO2)3], and it is then extracted by N263. The extraction of Co(II) is related to the concentration of N${\rm{O}}_2^- $. The extraction efficiency of Co(II) reaches the maximum of 99.16%, while the extraction efficiencies of Ni(II), Mn(II), and Li(I) are 9.27%‒9.80% under the following conditions: 30vol% of N263 and 15vol% of iso-propyl alcohol in sulfonated kerosene, the volume ratio of the aqueous-to-organic phase is 2:1, the extraction time is 30 min, and 1 M sodium nitrite in 0.1 M HNO3. The theoretical stages require for the Co(II) extraction are performed in the McCabe–Thiele diagram, and the extraction efficiency of Co(II) reaches more than 99.00% after three-stage counter-current extraction with Co(II) concentration of 2544 mg/L. When the HCl concentration is 1.5 M, the volume ratio of the aqueous-to-organic phase is 1:1, the back-extraction efficiency of Co(II) achieves 91.41%. After five extraction and back-extraction cycles, the Co(II) extraction efficiency can still reach 93.89%. The Co(II) extraction efficiency in the actual leaching solution reaches 100%.
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    • Supplementary Information-s12613-022-2571-8.docx
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