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氯化物盐析剂对过渡金属离子水合作用及碱性萃取剂氯化甲基三辛基铵溶剂萃取的阳离子效应

Cation Effect of Chloride Salting Agents on Transition Metal Ion Hydration and Solvent Extraction by the Basic Extractant Methyltrioctylammonium Chloride.

作者信息

Lommelen Rayco, Onghena Bieke, Binnemans Koen

机构信息

Department of Chemistry, KU Leuven, Celestijnenlaan 200F, P.O. Box 2404, B-3001 Leuven, Belgium.

出版信息

Inorg Chem. 2020 Sep 21;59(18):13442-13452. doi: 10.1021/acs.inorgchem.0c01821. Epub 2020 Aug 28.

Abstract

The addition of a nonextractable salt has an important influence on the solvent extraction of metal ions, but the underlying principles are not completely understood yet. However, relating solute hydration mechanisms to solvent extraction equilibria is key to understanding the mechanism of solvent extraction of metal ions as a whole. We have studied the speciation of Co(II), Zn(II), and Cu(II) in aqueous solutions containing different chloride salts to understand their extraction to the basic extractant methyltrioctylammonium chloride (TOMAC). This includes the first speciation profile of Zn(II) in chloride media with the three Zn(II) species [Zn(HO)], [ZnClHO], and [ZnCl]. The observed differences in extraction efficiency for a given transition metal ion can be explained by transition metal ion hydration due to ion-solvent interactions, rather than by ion-solute interactions or by differences in speciation. Chloride salting agents bearing a cation with a larger hydration Gibbs free energy reduce the free water content more, resulting in a lower hydration for the transition metal ion. This destabilizes the transition metal chloro complex in the aqueous phase and increases the extraction efficiency. Salting agents with di- and trivalent cations reduce the transition metal chloro complex hydration less than expected, resulting in a lower extraction efficiency. The cations of these salting agents have a very large hydration Gibbs free energy, but the overall hydration of these salts is reduced due to significant salt ion pair formation. The general order of salting-out strength for the extraction of metal ions from chloride salt solutions is Cs < Rb < NH ≈ K < Al ≈ Mg ≈ Ca ≈ Na < Li. These findings can help in predicting the optimal conditions for metal separation by solvent extraction and also contribute to a broader understanding of the effects of dissolved salts on solutes.

摘要

添加不可萃取盐对金属离子的溶剂萃取有重要影响,但其基本原理尚未完全明确。然而,将溶质水合机制与溶剂萃取平衡联系起来是理解整个金属离子溶剂萃取机制的关键。我们研究了含有不同氯化物盐的水溶液中Co(II)、Zn(II)和Cu(II)的形态,以了解它们被碱性萃取剂甲基三辛基氯化铵(TOMAC)萃取的情况。这包括在氯化物介质中Zn(II)的首个形态分布,其中有三种Zn(II)物种:[Zn(HO)]、[ZnClHO]和[ZnCl]。对于给定的过渡金属离子,观察到的萃取效率差异可以用离子 - 溶剂相互作用导致的过渡金属离子水合来解释,而不是离子 - 溶质相互作用或形态差异。具有较大水合吉布斯自由能阳离子的氯化盐析剂会更多地降低自由水含量,导致过渡金属离子的水合程度降低。这会使水相中过渡金属氯配合物不稳定,并提高萃取效率。含有二价和三价阳离子的盐析剂对过渡金属氯配合物水合的降低程度低于预期,导致萃取效率较低。这些盐析剂的阳离子具有非常大的水合吉布斯自由能,但由于显著的盐离子对形成,这些盐的整体水合程度降低。从氯化物盐溶液中萃取金属离子的盐析强度一般顺序为Cs < Rb < NH ≈ K < Al ≈ Mg ≈ Ca ≈ Na < Li。这些发现有助于预测通过溶剂萃取进行金属分离的最佳条件,也有助于更广泛地理解溶解盐对溶质的影响。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/191a/7529323/48accc0bcc34/ic0c01821_0001.jpg

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