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A separation processing for industrial rare earth feed solution by phosphonium ionic liquid type saponification strategy
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摘要
A novel ionic liquid type saponification processing based on quaternary phosphonium type bifunctional IL is developed for yttrium separation from ion-adsorbed rare earth deposit.The extractabilities of([trihexyl(tetradecyl)phosphonium][sec-octylphenoxy acetate]([P_(6,6,6,14)][SOPAA]) were pronouncedly higher than those of sec-octylphenoxy acetic acid(HSOPAA),mixture of HSOPAA and[P_(6,6,6,14)]CI for rare earth elements(REEs).The ion association extraction mechanism contributes to avoid the numerous saponification procedures using alkali and resulting saponification wastewater.After 13 stages of extraction and 6 stages of scrubbing sections,the Y(lll) was successfully separated from industrial heavy RREs feed,the purity of Y(lll) in raffinate was approximately to be 98.9%.Stripping by distilled water was effectively achieved for REEs,which contributes to decrease the consumption of acid to a considerable extent.
A novel ionic liquid type saponification processing based on quaternary phosphonium type bifunctional IL is developed for yttrium separation from ion-adsorbed rare earth deposit.The extractabilities of([trihexyl(tetradecyl)phosphonium][sec-octylphenoxy acetate]([P_(6,6,6,14)][SOPAA]) were pronouncedly higher than those of sec-octylphenoxy acetic acid(HSOPAA),mixture of HSOPAA and[P_(6,6,6,14)]CI for rare earth elements(REEs).The ion association extraction mechanism contributes to avoid the numerous saponification procedures using alkali and resulting saponification wastewater.After 13 stages of extraction and 6 stages of scrubbing sections,the Y(lll) was successfully separated from industrial heavy RREs feed,the purity of Y(lll) in raffinate was approximately to be 98.9%.Stripping by distilled water was effectively achieved for REEs,which contributes to decrease the consumption of acid to a considerable extent.
引文
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