无机盐工业
主管:中海油天津化工研究设计院有限公司
主办:中海油天津化工研究设计院有限公司
   中海油炼油化工科学研究院(北京)有限公司
   中国化工学会无机酸碱盐专业委员会
ISSN 1006-4990 CN 12-1069/TQ
研究与开发

离子液体体系卤水提锂的洗涤工艺研究

  • 秦亚茹 ,
  • 石成龙 ,
  • 王兴权 ,
  • 宋桂秀 ,
  • 李宏霞 ,
  • 张净净
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  • 1. 青海民族大学化学化工学院,青海西宁 810007
    2. 青海省盐化工产品质量监督检验中心
秦亚茹(1989— ),女,博士研究生,讲师,研究方向为盐湖卤水资源综合利用;E-mail:qhmdqyr@126.com。

收稿日期: 2019-06-20

  网络出版日期: 2020-03-31

基金资助

青海省自然科学基金项目(2018-ZJ-950Q);青海省自然科学基金项目(2020-ZJ-953Q);青海民族大学高层次人才项目(2017XJG01);青海民族大学高层次人才项目(2019XJG04)

Study on scrubbing process of lithium extraction from brine in ionic liquid system

  • Yaru Qin ,
  • Chenglong Shi ,
  • Xingquan Wang ,
  • Guixiu Song ,
  • Hongxia Li ,
  • Jingjing Zhang
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  • 1. College of Chemistry and Chemical Engineering,Qinghai Nationalities University,Xining 810007,China
    2. Qinghai Salt Chemical Products Supervision and Inspection Center

Received date: 2019-06-20

  Online published: 2020-03-31

摘要

溶剂萃取法是盐湖提锂的重要工艺方法。采用磷酸三丁酯(TBP)/1-丁基-3-甲基咪唑双三氟甲基磺酰亚胺盐([C4mim][NTf2])离子液体体系对高镁锂比盐湖卤水中的锂进行萃取分离提取实验,对负载有机相的洗涤和反萃过程进行了研究。萃取实验:在TBP与[C4mim][NTf2]体积比为9∶1、相比(有机相与水相的体积比)为2∶1条件下,锂离子与其他离子的分离系数分别为β(锂/钠)=94.70、β(锂/钾)=148.85、β(锂/镁)=131.81。洗涤实验:系统考察了洗涤剂种类及浓度、相比、洗涤次数等因素对杂质离子洗脱率的影响,结果发现氯化锂和盐酸的混合溶液是从负载有机相中洗涤除去杂质离子的有效洗涤剂。洗涤过程适宜条件:洗涤剂中氯化锂浓度为4 mol/L、盐酸浓度为0.5 mol/L,相比为5∶1,洗涤次数为2次。反萃实验:用稀盐酸(1.0 mol/L)对负载有机相进行反萃取,在相比为1∶1条件下,单级反萃率达到97.81%。研究表明,离子液体体系作为一种新型萃取体系,在高镁锂比盐湖卤水中提取锂具有较好的应用前景。

本文引用格式

秦亚茹 , 石成龙 , 王兴权 , 宋桂秀 , 李宏霞 , 张净净 . 离子液体体系卤水提锂的洗涤工艺研究[J]. 无机盐工业, 2020 , 52(3) : 55 -58 . DOI: 10.11962/1006-4990.2019-0220

Abstract

Solvent extraction was considered to be a importing technique for lithium extraction from the salt lake brine.The ionic liquid system containing tributyl phosphate(TBP) and 1-butyl-3-methylimidazolium bistrifluoromethylsulfonimide salt([C4mim][NTf2]) was used to extract lithium ions from salt lake brine with a high Mg/Li ratio.The scrubbing and stripping processes from the loaded organic phase were also studied.In the extraction experiment,under the condition of a volume ratio of TBP to[C4mim][NTf2] of 9∶1 and a phase ratio (O/A) of 2∶1,the separation factor βLi/Na,βLi/K and βLi/Mg were 94.70,148.85 and 131.81,respectively.In the scrubbing experiment,the effect of the types and concentration of scrubbing agent,phase ratio and scrubbing times on scrubbing efficiencies were investigated systematically.The results showed that the mixed solution of lithium chloride and hydrochloric acid was an effective scrubbing agent for removing impurity ions from the loaded organic phase.Optimal extraction conditions of the scrubbing process included 4 mol/L LiCl and 0.5 mol/L HCl in scrubbing agent,phase ratio(O/A) of 5∶1 and the scrubbing times of two times.In the stripping experiment,the loaded organic phase was stripped by 1.0 mol/L HCl and the single-stage stripping rate reached 97.81% at the phase ratio(O/A) of 1/1.This study showed that the new ionic liquid system had a good application prospect for extracting lithium from salt lake brine with a high Mg/Li ratio.

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