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Extraction kinetics of lithium from salt lake brine by N,N-bis(2-ethylhexyl) acetamide using Lewis Cell
Li, Hui-Fang ; Li, Li-Juan ; Peng, Xiao-Wu ; Ji, Lian-Min ; Li, Wu
2018-06-01
Source PublicationHYDROMETALLURGY
AbstractLithium, as the green energy, its application and exploitation attract much attention. The lithium extraction kinetics with N,N-bis(2-ethylhexyl) acetamide(N523) in sulfonated kerosene has been investigated experimentally using Lewis Cell. The effects of diffusion resistance area, interfacial area, temperature and the concentration of reagents were studied. The results showed that the diffusion resistance mainly existed in aqueous phase, the extraction process was a diffusion-controlled kinetics process with an interfacial reaction and the extraction kinetic equation was obtained.
PublisherELSEVIER SCIENCE BV
Document Type期刊论文
Identifierhttp://ir.isl.ac.cn/handle/363002/7188
Collection中国科学院青海盐湖研究所
Recommended Citation
GB/T 7714
Li, Hui-Fang,Li, Li-Juan,Peng, Xiao-Wu,et al. Extraction kinetics of lithium from salt lake brine by N,N-bis(2-ethylhexyl) acetamide using Lewis Cell[J]. HYDROMETALLURGY,2018.
APA Li, Hui-Fang,Li, Li-Juan,Peng, Xiao-Wu,Ji, Lian-Min,&Li, Wu.(2018).Extraction kinetics of lithium from salt lake brine by N,N-bis(2-ethylhexyl) acetamide using Lewis Cell.HYDROMETALLURGY.
MLA Li, Hui-Fang,et al."Extraction kinetics of lithium from salt lake brine by N,N-bis(2-ethylhexyl) acetamide using Lewis Cell".HYDROMETALLURGY (2018).
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