Study on the Recovery of Li2CO3 from Cathode Active Material NCM(LiNiCoMnO2) of Spent Lithium Ion Batteries
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In this study, an experiment is performed to recover the Li in Li2CO3 phase from the cathode active material NMC (LiNiCoMnO2) in waste lithium ion batteries. Firstly, carbonation is performed to convert the LiNiO, LiCoO, and Li2MnO3 phases within the powder to Li2CO3 and NiO, CoO, and MnO. The carbonation for phase separation proceeds at a temperature range of 600oC~800oC in a CO2 gas (300 cc/min) atmosphere. At 600~700oC, Li2CO3 and NiO, CoO, and MnO are not completely separated, while Li and other metallic compounds remain. At 800 oC, we can confirm that LiNiO, LiCoO, and Li2MnO3 phases are separated into Li2CO3 and NiO, CoO, and MnO phases. After completing the phase separation, by using the solubility difference of Li2CO3 and NiO, CoO, and MnO, we set the ratio of solution (distilled water) to powder after carbonation as 30:1. Subsequently, water leaching is carried out. Then, the Li2CO3 within the solution melts and concentrates, while NiO, MnO, and CoO phases remain after filtering. Thus, Li2CO3 can be recovered.
Abstract
In this study, an experiment is performed to recover the Li in Li2CO3 phase from the cathode active material NMC (LiNiCoMnO2) in waste lithium ion batteries. Firstly, carbonation is performed to convert the LiNiO, LiCoO, and Li2MnO3 phases within the powder to Li2CO3 and NiO, CoO, and MnO. The carbonation for phase separation proceeds at a temperature range of 600oC~800oC in a CO2 gas (300 cc/min) atmosphere. At 600~700oC, Li2CO3 and NiO, CoO, and MnO are not completely separated, while Li and other metallic compounds remain. At 800 oC, we can confirm that LiNiO, LiCoO, and Li2MnO3 phases are separated into Li2CO3 and NiO, CoO, and MnO phases. After completing the phase separation, by using the solubility difference of Li2CO3 and NiO, CoO, and MnO, we set the ratio of solution (distilled water) to powder after carbonation as 30:1. Subsequently, water leaching is carried out. Then, the Li2CO3 within the solution melts and concentrates, while NiO, MnO, and CoO phases remain after filtering. Thus, Li2CO3 can be recovered.
참고문헌 (17)
- S. W. Lee, , Ceramist, 13, pp.32~ (2010)
- H. C. Jung, , J. Korean Powder Metall. Inst., 17, pp.175~ (2010)[DOI]
- 박홍규, "리튬이차전지용 양극재 개발 동향", 전기화학회지, 11(3), pp.197~210 (2008), 한국전기화학회
- H. S. Hong, , Trends in Metals & Materials Engineering, 24, pp.26~ (2011)
- G. C. Shim, , Trends in Metals & Materials Engineering, 24, pp.49~ (2011)
- 이정주, "二次電池 製造工程스크랩으로부터 高效率 親環境 코발트(Co)와 리튬(Li)의 回收에 關한 硏究", 자원리싸이클링, 19(6), pp.51~60 (2010), 한국자원리싸이클링학회
- 이재천, "리튬이온電池 製造工程의 廢陽極活物質로부터 濕式製鍊工程에 의한 코발트의 回收", 자원리싸이클링, 14(6), pp.28~36 (2005), 한국자원리싸이클링학회
- C. K. Lee, , J. Korean Ind. Eng. Chem., 12, pp.890~ (2001)
- C. K. Lee, , J. of Korean Inst. of Resources Recycling, 10, pp.9~ (2001)
- C. K. Lee, , J. of Korean Inst. of Resources Recycling, 9, pp.37~ (2000)
- L. Li, , Waste Management, 30, pp.2615~ (2010)[DOI]
- Y. Yamaji, , Resource Processing, 58, pp.9~ (2011)[DOI]
- C. Liang, , The Chinese Journal of Nonferrous Metals, 21, pp.1192~ (2011)
- M. Petranikova, , Acta Metallugica Slovaca, 17, pp.106~ (2011)
- E. M. Garcia, , J. Appl. Electrochem., 41, pp.1373~ (2011)[DOI]
- T. Georgi-Maschler, , J. Power Sources, 207, pp.173~ (2012)[DOI]
- S. K. Kim, , The 2011 spring meeting and 36the conference, pp.84~ (2011), Korean Inst. of Resources Recycling
