Metal Recovery of LiCoO2/LiNiO2 Cathode Materials by Hydrothermal Leaching and Precipitation Separation
Here, Ni, Co, and Li ions in the leachate obtained from commercial LiCoO2/LiNiO2 cathode materials by hydrothermal leaching with citric acid were precipitated and separated in order using a series of precipitants, dimethylglyoxime (DMG), (NH4)2C2O4, and Na3PO4, respectively. The parameters including...
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Published in | ACS sustainable chemistry & engineering Vol. 10; no. 38; pp. 12852 - 12863 |
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Main Authors | , , , , |
Format | Journal Article |
Language | English |
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American Chemical Society
26.09.2022
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Abstract | Here, Ni, Co, and Li ions in the leachate obtained from commercial LiCoO2/LiNiO2 cathode materials by hydrothermal leaching with citric acid were precipitated and separated in order using a series of precipitants, dimethylglyoxime (DMG), (NH4)2C2O4, and Na3PO4, respectively. The parameters including the pH value, precipitant amount, and reaction temperature were optimized during the metal separation step. Finally, the recovery rates of Ni, Co, and Li were 97.2, 96.1, and 94.1%, respectively, with the purities of Ni, Co, and Li in the corresponding precipitate being 96.3, 96.2, and 99.9%, respectively. The method of hydrothermal leaching was compared with the method of traditional leaching in terms of the leaching mechanism and the metal separation performance of the obtained leachates. Compared with the traditional leaching with a reductant (e.g., H2O2), hydrothermal leaching is performed at higher temperatures and requires pressure-resistant reactors, but it can reduce the consumption of chemicals such as reductants, promote the reaction rate, and improve industrial applicability. Even though the leaching mechanisms were different, the leachates obtained by hydrothermal and traditional leaching showed comparable performance in the metal separation step, indicating hydrothermal leaching is qualified to produce leachates for lithium-ion battery (LIB) recycling. With the success of isolating metal components from the leachate obtained by hydrothermal leaching, an upgraded hydrometallurgical method, composed of hydrothermal leaching and precipitation separation steps, was officially launched for LIB recycling and is subject to further development. |
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AbstractList | Here, Ni, Co, and Li ions in the leachate obtained from commercial LiCoO₂/LiNiO₂ cathode materials by hydrothermal leaching with citric acid were precipitated and separated in order using a series of precipitants, dimethylglyoxime (DMG), (NH₄)₂C₂O₄, and Na₃PO₄, respectively. The parameters including the pH value, precipitant amount, and reaction temperature were optimized during the metal separation step. Finally, the recovery rates of Ni, Co, and Li were 97.2, 96.1, and 94.1%, respectively, with the purities of Ni, Co, and Li in the corresponding precipitate being 96.3, 96.2, and 99.9%, respectively. The method of hydrothermal leaching was compared with the method of traditional leaching in terms of the leaching mechanism and the metal separation performance of the obtained leachates. Compared with the traditional leaching with a reductant (e.g., H₂O₂), hydrothermal leaching is performed at higher temperatures and requires pressure-resistant reactors, but it can reduce the consumption of chemicals such as reductants, promote the reaction rate, and improve industrial applicability. Even though the leaching mechanisms were different, the leachates obtained by hydrothermal and traditional leaching showed comparable performance in the metal separation step, indicating hydrothermal leaching is qualified to produce leachates for lithium-ion battery (LIB) recycling. With the success of isolating metal components from the leachate obtained by hydrothermal leaching, an upgraded hydrometallurgical method, composed of hydrothermal leaching and precipitation separation steps, was officially launched for LIB recycling and is subject to further development. Here, Ni, Co, and Li ions in the leachate obtained from commercial LiCoO2/LiNiO2 cathode materials by hydrothermal leaching with citric acid were precipitated and separated in order using a series of precipitants, dimethylglyoxime (DMG), (NH4)2C2O4, and Na3PO4, respectively. The parameters including the pH value, precipitant amount, and reaction temperature were optimized during the metal separation step. Finally, the recovery rates of Ni, Co, and Li were 97.2, 96.1, and 94.1%, respectively, with the purities of Ni, Co, and Li in the corresponding precipitate being 96.3, 96.2, and 99.9%, respectively. The method of hydrothermal leaching was compared with the method of traditional leaching in terms of the leaching mechanism and the metal separation performance of the obtained leachates. Compared with the traditional leaching with a reductant (e.g., H2O2), hydrothermal leaching is performed at higher temperatures and requires pressure-resistant reactors, but it can reduce the consumption of chemicals such as reductants, promote the reaction rate, and improve industrial applicability. Even though the leaching mechanisms were different, the leachates obtained by hydrothermal and traditional leaching showed comparable performance in the metal separation step, indicating hydrothermal leaching is qualified to produce leachates for lithium-ion battery (LIB) recycling. With the success of isolating metal components from the leachate obtained by hydrothermal leaching, an upgraded hydrometallurgical method, composed of hydrothermal leaching and precipitation separation steps, was officially launched for LIB recycling and is subject to further development. |
Author | Zheng, Qingxin Hirama, Seiya Nakajima, Akitoshi Ogawa, Tetsufumi Watanabe, Masaru |
AuthorAffiliation | Faculty of Engineering Tohoku University Research Center of Supercritical Fluid Technology, Department of Chemical Engineering, Graduate School of Engineering |
AuthorAffiliation_xml | – name: Research Center of Supercritical Fluid Technology, Department of Chemical Engineering, Graduate School of Engineering – name: Faculty of Engineering – name: Tohoku University |
Author_xml | – sequence: 1 givenname: Akitoshi surname: Nakajima fullname: Nakajima, Akitoshi organization: Faculty of Engineering – sequence: 2 givenname: Qingxin orcidid: 0000-0002-6002-7438 surname: Zheng fullname: Zheng, Qingxin email: qingxin.zheng.a2@tohoku.ac.jp organization: Tohoku University – sequence: 3 givenname: Tetsufumi surname: Ogawa fullname: Ogawa, Tetsufumi organization: Faculty of Engineering – sequence: 4 givenname: Seiya surname: Hirama fullname: Hirama, Seiya organization: Faculty of Engineering – sequence: 5 givenname: Masaru surname: Watanabe fullname: Watanabe, Masaru email: masaru.watanabe.e2@tohoku.ac.jp organization: Tohoku University |
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Keywords | metal recovery hydrothermal leaching citric acid precipitation separation lithium-ion battery LIB recycling LiCoO2/LiNiO2 |
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Snippet | Here, Ni, Co, and Li ions in the leachate obtained from commercial LiCoO2/LiNiO2 cathode materials by hydrothermal leaching with citric acid were precipitated... Here, Ni, Co, and Li ions in the leachate obtained from commercial LiCoO₂/LiNiO₂ cathode materials by hydrothermal leaching with citric acid were precipitated... |
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SubjectTerms | cathodes citric acid green chemistry industrial applications leachates lithium batteries reducing agents temperature |
Title | Metal Recovery of LiCoO2/LiNiO2 Cathode Materials by Hydrothermal Leaching and Precipitation Separation |
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