SHI Chenglong, JIA Yongzhong, JING Yan. Lithium and magnesium separation from salt lake brine by ionic liquids containing tributyl phosphate[J]. CIESC Journal, 2015, (S1): 253-259.
DOI:
SHI Chenglong, JIA Yongzhong, JING Yan. Lithium and magnesium separation from salt lake brine by ionic liquids containing tributyl phosphate[J]. CIESC Journal, 2015, (S1): 253-259.DOI: 10.11949/j.issn.0438-1157.20141824.
Lithium and magnesium separation from salt lake brine by ionic liquids containing tributyl phosphate
was used as an alternative solvent to study liquid/liquid extraction of lithium from salt lake brine. In this system
the ionic liquids and tributyl phosphate (TBP) were used as extraction medium and extractant respectively. The effects of solution pH value
phase ratio and other factors on lithium extraction efficiency had been investigated. The preliminary experimental results had demonstrated that
compared with using conventional extraction system
the extraction efficiency had been increased greatly in this ionic liquid system. Optimal extraction conditions of this system include the ratio of TBP/ILs at 9/1(vol)
O/A at 2:1 and unadjusted pH. Under the optimal conditions
the single extraction efficiency of lithium ion and magnesium ion were 80.64% and 5.30%
respectively. And total extraction efficiency of 99.42% was obtained by triple-stage countercurrent extraction. The single stripping rate of lithium ion and magnesium ion were 98.78% and 99.15%
respectively
at 80℃ when the A/O phase ratio was 2. The Mg/Li ratio was 3.03 in the aqueous phase after stripping
which have dropped 93.41% when compared with the initial value. To evaluate the potential use of RTILs to replace traditional volatile organic compounds (VOCs) in liquid/liquid extraction of lithium
the extractions of lithium ion with VOCs and ionic liquid were compared. Compared with using conventional extraction system
the extraction efficiency had been increased greatly in this ionic liquid system. In addition
the equipment corrosion and the environmental pollution had been avoided in this new extraction system. The extraction mechanism was deduced based on the ultraviolet-visible(UV) absorption. Cation exchange was proposed to be the mechanism of extraction followed in ionic liquid. So the ionic liquid was not only regarded as the solvent but also the co-extraction reagent to some extent. Preliminary results indicated that the ionic liquids had the potential to replace traditional volatile organic solvents in liquid/liquid extraction of metal ions.