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一种用离子液体油酸四辛铵从氯化物介质中溶剂萃取第一排过渡金属的机制。

A mechanism for solvent extraction of first row transition metals from chloride media with the ionic liquid tetraoctylammonium oleate.

作者信息

Parmentier Dries, Vander Hoogerstraete Tom, Banerjee Dipanjan, Valia Yash A, Metz Sybrand J, Binnemans Koen, Kroon Maaike C

机构信息

Wetsus, European Centre of Excellence for Sustainable Water Technology, Oostergoweg 9, 8911 MA Leeuwarden, The Netherlands.

出版信息

Dalton Trans. 2016 Jun 21;45(23):9661-8. doi: 10.1039/c6dt00833j. Epub 2016 May 25.

Abstract

Aqueous waste streams of the metallurgical industry often contain considerable concentrations of metal salts. Previous research showed that the metal chloride salts of zinc(ii), manganese(ii) and iron(iii) can be recovered by solvent extraction using a sustainable and renewable fatty acid based ionic liquid as the extractant. In this paper, the extraction mechanism of Zn(ii), Co(ii) and Ni(ii) from chloride media has been studied systematically. The metal extraction performances of the precursors, sodium oleate and tetraoctylammonium chloride, were compared to the extraction performance of the ionic liquid tetraoctylammonium oleate. Slope analysis experiments were performed to determine the number of ionic liquid molecules involved in the extraction. The experimental data showed that Co(ii) and Ni(ii) were extracted in the pH range from 6 to 8 by the formation of negatively charged metal carboxylate complexes with tetraalkylammonium counter ions. In contrast, Zn(ii) gets extracted as a mixed metal chloride carboxylate anionic complex with tetraalkylammonium counter ions. This extraction mechanism was supported by EXAFS measurements.

摘要

冶金工业的含水废物流通常含有相当高浓度的金属盐。先前的研究表明,锌(II)、锰(II)和铁(III)的金属氯化物盐可以通过使用可持续且可再生的脂肪酸基离子液体作为萃取剂进行溶剂萃取来回收。本文系统地研究了从氯化物介质中萃取锌(II)、钴(II)和镍(II)的机理。将前体油酸钠和四辛基氯化铵的金属萃取性能与离子液体油酸四辛基铵的萃取性能进行了比较。进行了斜率分析实验以确定参与萃取的离子液体分子数量。实验数据表明,钴(II)和镍(II)在pH值为6至8的范围内通过与四烷基铵抗衡离子形成带负电荷的金属羧酸盐络合物而被萃取。相比之下,锌(II)作为与四烷基铵抗衡离子形成的混合金属氯化物羧酸盐阴离子络合物被萃取。扩展X射线吸收精细结构(EXAFS)测量支持了这种萃取机理。

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