基于离子液体的水相钴回收工艺开发

E. Othman, A. V. D. Ham, H. Miedema, S. Kersten
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引用次数: 2

摘要

采用离子液体[P8888 +][油酸盐-],研究了液-液萃取法回收水中Co2+。以Na2CO3(aq)为再生液,连续5次进行萃取再生实验。在0.7 ~ 1 M Na2CO3(aq)条件下,Co2+以CoCO3(s)的形式回收率达到99%以上。Co2+的转移由第一个循环的离子对萃取转变为后续循环的离子交换。因此,单个提取-再生循环的测量不足以感知有关该过程稳态条件的结论性信息。在该技术可行性的背景下,解决了四个关键方面:提取效率,IL的回收,IL的损失和最终产品。离子液体[P8888 +][油酸盐-]从水中提取钴,使用Na2CO3溶液回收钴是一种高效和可持续的再生策略,因为它以高再生效率为市场提供了有趣的最终产品。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Ionic Liquid-Based Process Development for Cobalt Recovery from Aqueous Streams
Using the ionic liquid [P8888 +][Oleate-], liquid-liquid extraction has been studied to recover Co2+ from water. Extractionregeneration experiments were followed during five consecutive cycles with Na2CO3(aq) as regeneration solution. Over 99% of Co2+ was extracted and using 0.7-1 M Na2CO3(aq) the extracted Co2+ was recovered for 99% in the form of CoCO3(s). Co2+ transfer shifted from ion-pair extraction in the first cycle to ion-exchange in the successive cycles. Thus, the measurement of a single extraction–regeneration cycle is not sufficient to perceive conclusive information about the steady-state conditions of the process. In the context of the feasibility of the technology, four key aspects are addressed: extraction efficiency, recovery of the IL, loss of the IL, and the end product. Synopsis Cobalt extraction from aqueous using ionic liquid [P8888 +][oleate-] and cobalt recovery applying Na2CO3 solution as an efficient and sustainable regeneration strategy since it provides interesting end product for market with high regeneration efficiency.
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