Recovery of lithium from alkaline brine by solvent extraction with functionalized ionic liquid
文献类型:期刊论文
作者 | Yang, Shicheng1,2; Liu, Guowei2; Wang, Junfeng2; Cui, Li2; Chen, Yongmei1 |
刊名 | FLUID PHASE EQUILIBRIA |
出版日期 | 2019-08-01 |
卷号 | 493页码:129-136 |
ISSN号 | 0378-3812 |
关键词 | Lithium extraction Alkaline brine Functionalized ionic liquid Mechanisms |
DOI | 10.1016/j.fluid.2019.04.015 |
英文摘要 | Lithium recovery from alkaline brine was carried out by solvent extraction (SX) using a hydroxyl-functionalized ionic liquid, 1-hydroxyethyl-3-methyl imidazolium bis(trifluoromethylsulfonyl)imide ([OHEMIM][NTf2]) and a neutral ligand, trialkyl phosphine oxide (Cyanex923) as the extractants. Effect of extraction parameters, i.e. concentration of ionic liquid, extraction time, pH value of aqueous phase, phase ratio and mole ratio of sodium to lithium, on lithium extraction efficiency have been studied. Under the optimal parameters, over 93% of lithium was extracted in one single run. The extraction mechanism of lithium was investigated by the combination method of experiment and UV-visible spectroscopic characterization, and it was found that the ion exchange predominated during the extraction process. The extraction complex was determined by a slope analysis method, indicating that Cyanex923, Li+ and [NTf2](-) formed a 2:1:1 complex. The thermodynamic study indicated that lithium extraction reaction was spontaneous. Based on the above results, [OHEMIM][NTf2]-Cyanex923 extraction system showed a promising application in the recovery of lithium from alkaline brine. (C) 2019 Elsevier B.V. All rights reserved. |
WOS关键词 | AQUEOUS-SOLUTION ; SELECTIVE EXTRACTION ; TRIBUTYL-PHOSPHATE ; MECHANISM ; EQUILIBRIA ; SEPARATION ; ELECTRODE ; KEROSENE ; BUTYL |
资助项目 | Fujian Institute of Innovation ; Chinese Academy of Sciences[FJCXY18040101] ; Key Program of National Natural Science Foundation of China[91434203] ; Key Research Program of Frontier Sciences CAS[QYZDY-SSW-JSC011] ; National Natural Science Foundation of China[21706257] ; National Natural Science Foundation of China[21776292] |
WOS研究方向 | Thermodynamics ; Chemistry ; Engineering |
语种 | 英语 |
出版者 | ELSEVIER SCIENCE BV |
WOS记录号 | WOS:000470338600014 |
资助机构 | Fujian Institute of Innovation ; Chinese Academy of Sciences ; Key Program of National Natural Science Foundation of China ; Key Research Program of Frontier Sciences CAS ; National Natural Science Foundation of China |
源URL | [http://ir.ipe.ac.cn/handle/122111/29917] |
专题 | 中国科学院过程工程研究所 |
通讯作者 | Wang, Junfeng; Chen, Yongmei |
作者单位 | 1.Beijing Univ Chem Technol, Beijing 100029, Peoples R China 2.Chinese Acad Sci, State Key Lab Multiphase Complex Syst, Beijing Key Lab Ion Liquids Clean Proc, CAS Key Lab Green Proc & Engn,Inst Proc Engn, Beijing 100190, Peoples R China |
推荐引用方式 GB/T 7714 | Yang, Shicheng,Liu, Guowei,Wang, Junfeng,et al. Recovery of lithium from alkaline brine by solvent extraction with functionalized ionic liquid[J]. FLUID PHASE EQUILIBRIA,2019,493:129-136. |
APA | Yang, Shicheng,Liu, Guowei,Wang, Junfeng,Cui, Li,&Chen, Yongmei.(2019).Recovery of lithium from alkaline brine by solvent extraction with functionalized ionic liquid.FLUID PHASE EQUILIBRIA,493,129-136. |
MLA | Yang, Shicheng,et al."Recovery of lithium from alkaline brine by solvent extraction with functionalized ionic liquid".FLUID PHASE EQUILIBRIA 493(2019):129-136. |
入库方式: OAI收割
来源:过程工程研究所
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