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An integrated process for the separation and recovery of valuable metals from the spent LiNi0.5Co0.2Mn0.3O2 cathode materials
[Display omitted] •An overall process for recovering LiNi0.5Co0.2Mn0.3O2 cathode materials was proposed.•H2SO4 and H2O2 as leaching agent for high efficiency leaching of valuable metals.•P227, P204 as extractants for the separation of valuable metals by cascade extraction.•The high purity products w...
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Published in: | Separation and purification technology 2020-08, Vol.245, p.116869, Article 116869 |
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Main Authors: | , , , |
Format: | Article |
Language: | English |
Subjects: | |
Citations: | Items that this one cites Items that cite this one |
Online Access: | Get full text |
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Summary: | [Display omitted]
•An overall process for recovering LiNi0.5Co0.2Mn0.3O2 cathode materials was proposed.•H2SO4 and H2O2 as leaching agent for high efficiency leaching of valuable metals.•P227, P204 as extractants for the separation of valuable metals by cascade extraction.•The high purity products were obtained by precipitation method.•This process has showed application values for the separation of lithium-ion batteries.
The recycling of the spent lithium-ion batteries has aroused widespread concern due to the internal harmful substances and valuable metals. In this work, a novel integrated recovery process for the spent LiNi0.5Co0.2Mn0.3O2 cathode materials was proposed, which realized the complete separation of metals via leaching – cascade extraction – precipitation methods. Here, 2 mol/L (M) sulfuric acid (H2SO4) and 3 vol% (volume ratio) hydrogen peroxide (H2O2) were employed as leaching agents, resulting in the leaching rate of all metals are above 99%. Subsequently, the cascade extraction was adopted to separate lithium (Li) – nickel (Ni) – cobalt (Co) – manganese (Mn) by P227 (di-(2-ethylhexyl) phosphinic acid) and P204 (di-(2-ethylhexyl) phosphoric acid) extractants, respectively. Meanwhile, their high purity solid products such as MnO2, Li2CO3, NiO and Co3O4 were also obtained depending on the precipitation procedure. The yield and purity of these metals in the final products are 96.15%/100% for Li, 91.54%/98% for Ni, 91.15%/93% for Co, and 91.56%/100% for Mn, respectively. More importantly, this simple recovery process opens an avenue in the industrial applications for separating critical metals from the spent lithium-ion batteries. |
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ISSN: | 1383-5866 1873-3794 |
DOI: | 10.1016/j.seppur.2020.116869 |