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Recovery of Fe and Mn from aqueous solution with solvent extraction and liquid membrane permeation using ionic liquids

机译:溶剂萃取和离子液体液膜渗透法从水溶液中回收铁和锰

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摘要

In the hydrometallurgical recovery process of Fe(III) and Mn(II) from ores and scrap, solvent extraction and liquid membrane processes, which combine extraction and stripping into a single stage, are one of the promising separation process. In this study, ionic liquid such as Aliquat 336, Cyphos IL 101, and Cyphos IL 102 were used as complexing reagents to recover be(III) and Mn(II) in the solvent extraction and liquid membrane permeation. In the solvent extraction, the anionic chlorocomplexes, FeCl4- and MnCl3- formed in the presence of excess hydrochloric acid were extracted with all ionic liquids via anion exchange reaction. Cyphos IL 101 among the ionic liquids investigated was the large extractability for the recovery of Fe(III) and Mn(II). In the liquid membrane permeation with ionic liquids, the combination of Aliquat 336 as a carrier and 0.1 M Na2SO4 as a stripping phase gave a largest permeability of Le(III) (approximately 80%). In the case of Cyphos IL 101, the stripping rate was found to be considerably slow. The permeation rate of Mn(II) in membrane permeation using Aliquat 336 was smaller than that of Fe(III). This suggest that the kinetic separation of Fe(III) and Mn(II) is possible.
机译:在从矿石和废料中回收Fe(III)和Mn(II)的湿法冶金工艺中,将萃取和汽提结合在一起的溶剂萃取和液膜工艺是很有前途的分离工艺之一。在这项研究中,使用离子液体(例如Aliquat 336,Cyphos IL 101和Cyphos IL 102)作为络合剂在溶剂萃取和液膜渗透中回收be(III)和Mn(II)。在溶剂萃取中,通过所有的离子液体通过阴离子交换反应萃取在过量盐酸存在下形成的阴离子氯配合物FeCl4-和MnCl3-。在所研究的离子液体中,Cyphos IL 101具有很高的可萃取性,可用于回收Fe(III)和Mn(II)。在用离子液体渗透液膜中,作为载体的Aliquat 336和作为汽提相的0.1 M Na2SO4的组合产生最大的Le(III)渗透率(约80%)。对于Cyphos IL 101,发现其剥离速度相当慢。使用Aliquat 336进行膜渗透时,Mn(II)的渗透速率小于Fe(III)。这表明Fe(III)和Mn(II)的动力学分离是可能的。

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