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Comparison of Two Acidic Leaching Processes for Selecting the Effective Recycle Process of Spent Lithium ion Battery

Authors
손정수김수경이철경Shun-Myung ShinDong-Hyo Yang
Issue Date
2006
Publisher
한국자원공학회
Keywords
spent lithium ion battery; sulfuric acid leaching; oxalic acid leaching; cobalt recovery; spent lithium ion battery; sulfuric acid leaching; oxalic acid leaching; cobalt recovery
Citation
Geosystem Engineering, v.9, no.1, pp 1 - 6
Pages
6
Journal Title
Geosystem Engineering
Volume
9
Number
1
Start Page
1
End Page
6
URI
https://scholarworks.bwise.kr/kumoh/handle/2020.sw.kumoh/22810
ISSN
1226-9328
2166-3394
Abstract
Physical treatment and chemical treatment of spent lithium-ion battery were studied in our research team. Especially we developed two types of acidic leaching for crushed powders containing LiCoO2 of spent lithium ion battery. One of them is sulfuric acid leaching with H2O2 as a reducing agent. The leaching rates of cobalt, lithium and the other metals were above 99 % at the condition of 2 M H2SO4, 10 vol. % H2O2, 75oC, 300 rpm agitation speed, 250 g/5L solid liquid ratio and 75 minutes reaction time. And the other leaching process is the oxalic acid leaching. In this process more than 99% of Li and less than 1% of Co were dissolved at the condition of 3M oxalic acid, 80oC reaction temperature, 300rpm agitation speed, 50g/L initial solid/liquid ratio and 90min extraction time. Each process has its advantage and disadvantage. In sulfuric acid leaching, leaching reagent is very cheap and cobalt could be recovered into cobalt hydroxide. On the other hand, oxalic acid is more expensive than sulfuric acid but lithium could be dissolved selectively. Also cobalt could be recovered into cobalt oxalate and it could be changed into cobalt oxide after heat treatment. In order to select the effective recycling process, recovery rate and purity of cobalt hydroxide and cobalt oxalate were compared and it was investigated which process was more environment- friendly and economical.
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