Haoyan Li, Sohrab Rohani, Minyu He, Xi Jin, Chunlian Ding, Dong Wang, Weizao Liu
{"title":"硫酸盐焙烧-分步沉淀法回收废LiCoO2正极材料的综合工艺研究","authors":"Haoyan Li, Sohrab Rohani, Minyu He, Xi Jin, Chunlian Ding, Dong Wang, Weizao Liu","doi":"10.1016/j.seppur.2025.131710","DOIUrl":null,"url":null,"abstract":"With the rapid development of new energy industry, the quantity of spent lithium-ion batteries (LIBs) is increasing accordingly. From the environmental protection and resource recovery standpoints, it is crucial to recover valuable metals from spent LIBs. In this study, an efficient and integrated process was proposed to extract the valuable metals from spent LIBs with inexpensive Fe<sub>2</sub>(SO<sub>4</sub>)<sub>3</sub> as a reagent. The effects of various process parameters including the mass ratio of Fe<sub>2</sub>(SO<sub>4</sub>)<sub>3</sub> to the cathode material (F/C), roasting temperature, and roasting time on the leaching efficiencies were investigated. The leaching efficiency of Li was approximately 100 %, and that of cobalt reached 96 %, while the iron was hardly leached under the optimal conditions. The reaction mechanism of sulfation roasting process was studied through thermodynamic behavior, phase transformation as well as valence state transition. When roasting at a low temperature (<600 °C), the ion-exchange reaction dominated, which converted lithium into its soluble sulfate prior to cobalt. With increased temperature (600–700 °C), Fe<sub>2</sub>(SO<sub>4</sub>)<sub>3</sub> decomposed and generated SO<sub>2</sub>, promoting the sulfation reaction through gas–solid interaction, and thus increasing the leaching efficiency of Li and Co. Once the temperature reached 800 °C, CoSO<sub>4</sub> decomposed and the resulting cobalt oxide reacted with Fe<sub>2</sub>O<sub>3</sub> to create a spinel phase CoFe<sub>2</sub>O<sub>4</sub>, which is very difficult to dissolve, will reduce the recovery of cobalt. Furthermore, the recovery of Li and Co from the filtrate using H<sub>2</sub>C<sub>2</sub>O<sub>4</sub> and Na<sub>2</sub>CO<sub>3</sub> was investigated, where the recovery efficiency of Co and Li from the filtrate reached 94 % and 88 %, respectively. The findings demonstrated that it is possible to recover valuable metals from the cathode materials of spent LiCoO<sub>2</sub> batteries through the sulfation roasting-water leaching process followed by stepwise precipitation.","PeriodicalId":427,"journal":{"name":"Separation and Purification Technology","volume":"78 1","pages":""},"PeriodicalIF":8.1000,"publicationDate":"2025-01-20","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"An integrated process for recycling spent LiCoO2 cathode materials via sulfate roasting and stepwise precipitation\",\"authors\":\"Haoyan Li, Sohrab Rohani, Minyu He, Xi Jin, Chunlian Ding, Dong Wang, Weizao Liu\",\"doi\":\"10.1016/j.seppur.2025.131710\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"With the rapid development of new energy industry, the quantity of spent lithium-ion batteries (LIBs) is increasing accordingly. From the environmental protection and resource recovery standpoints, it is crucial to recover valuable metals from spent LIBs. In this study, an efficient and integrated process was proposed to extract the valuable metals from spent LIBs with inexpensive Fe<sub>2</sub>(SO<sub>4</sub>)<sub>3</sub> as a reagent. The effects of various process parameters including the mass ratio of Fe<sub>2</sub>(SO<sub>4</sub>)<sub>3</sub> to the cathode material (F/C), roasting temperature, and roasting time on the leaching efficiencies were investigated. The leaching efficiency of Li was approximately 100 %, and that of cobalt reached 96 %, while the iron was hardly leached under the optimal conditions. The reaction mechanism of sulfation roasting process was studied through thermodynamic behavior, phase transformation as well as valence state transition. When roasting at a low temperature (<600 °C), the ion-exchange reaction dominated, which converted lithium into its soluble sulfate prior to cobalt. With increased temperature (600–700 °C), Fe<sub>2</sub>(SO<sub>4</sub>)<sub>3</sub> decomposed and generated SO<sub>2</sub>, promoting the sulfation reaction through gas–solid interaction, and thus increasing the leaching efficiency of Li and Co. Once the temperature reached 800 °C, CoSO<sub>4</sub> decomposed and the resulting cobalt oxide reacted with Fe<sub>2</sub>O<sub>3</sub> to create a spinel phase CoFe<sub>2</sub>O<sub>4</sub>, which is very difficult to dissolve, will reduce the recovery of cobalt. Furthermore, the recovery of Li and Co from the filtrate using H<sub>2</sub>C<sub>2</sub>O<sub>4</sub> and Na<sub>2</sub>CO<sub>3</sub> was investigated, where the recovery efficiency of Co and Li from the filtrate reached 94 % and 88 %, respectively. 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An integrated process for recycling spent LiCoO2 cathode materials via sulfate roasting and stepwise precipitation
With the rapid development of new energy industry, the quantity of spent lithium-ion batteries (LIBs) is increasing accordingly. From the environmental protection and resource recovery standpoints, it is crucial to recover valuable metals from spent LIBs. In this study, an efficient and integrated process was proposed to extract the valuable metals from spent LIBs with inexpensive Fe2(SO4)3 as a reagent. The effects of various process parameters including the mass ratio of Fe2(SO4)3 to the cathode material (F/C), roasting temperature, and roasting time on the leaching efficiencies were investigated. The leaching efficiency of Li was approximately 100 %, and that of cobalt reached 96 %, while the iron was hardly leached under the optimal conditions. The reaction mechanism of sulfation roasting process was studied through thermodynamic behavior, phase transformation as well as valence state transition. When roasting at a low temperature (<600 °C), the ion-exchange reaction dominated, which converted lithium into its soluble sulfate prior to cobalt. With increased temperature (600–700 °C), Fe2(SO4)3 decomposed and generated SO2, promoting the sulfation reaction through gas–solid interaction, and thus increasing the leaching efficiency of Li and Co. Once the temperature reached 800 °C, CoSO4 decomposed and the resulting cobalt oxide reacted with Fe2O3 to create a spinel phase CoFe2O4, which is very difficult to dissolve, will reduce the recovery of cobalt. Furthermore, the recovery of Li and Co from the filtrate using H2C2O4 and Na2CO3 was investigated, where the recovery efficiency of Co and Li from the filtrate reached 94 % and 88 %, respectively. The findings demonstrated that it is possible to recover valuable metals from the cathode materials of spent LiCoO2 batteries through the sulfation roasting-water leaching process followed by stepwise precipitation.
期刊介绍:
Separation and Purification Technology is a premier journal committed to sharing innovative methods for separation and purification in chemical and environmental engineering, encompassing both homogeneous solutions and heterogeneous mixtures. Our scope includes the separation and/or purification of liquids, vapors, and gases, as well as carbon capture and separation techniques. However, it's important to note that methods solely intended for analytical purposes are not within the scope of the journal. Additionally, disciplines such as soil science, polymer science, and metallurgy fall outside the purview of Separation and Purification Technology. Join us in advancing the field of separation and purification methods for sustainable solutions in chemical and environmental engineering.