KU Leuven , Department of Chemistry , Celestijnenlaan 200F , P.O. Box 2404, B-3001 Leuven , Belgium.
Univ. Grenoble Alpes, Univ. Savoie Mont Blanc , CNRS, Grenoble INP (Institute of Engineering Univ. Grenoble Alpes), LEPMI , 38000 Grenoble , France.
Inorg Chem. 2019 Sep 16;58(18):12289-12301. doi: 10.1021/acs.inorgchem.9b01782. Epub 2019 Aug 27.
The metal extraction mechanism of basic extractants is typically described as an anion exchange process, but this mechanism does not correctly explain all observations. This paper introduces a novel model for the extraction of metals by basic extractants from chloride media supported by experimental data on methyltrioctylammonium chloride and Aliquat 336 chloride systems. This model relies on the hypothesis that the metal species least stabilized in the aqueous phase by hydration (i.e., the metal species with the lowest charge density) is extracted more efficiently than the more water stabilized species (i.e., species with higher charge densities). Once it is transferred to the organic phase, the extracted species can undergo further Lewis acid-base adduct formation reactions with the chloride anions available in the organic phase to form negatively charged chloro complexes, which than associate with the organic cations. Salting-out agents influence the extraction, most likely by decreasing the concentration of free water molecules, which destabilizes the metal complex in the aqueous phase. The evidence provided includes (1) the link between extraction and transition-metal speciation, (2) the trend in extraction efficiency as a function of the concentration of different salting-out agents, and (3) the behavior of HCl in the extraction system. The proposed extraction model better explains the experimental observations in comparison to the anion exchange model and allows the prediction of optimal conditions for metal extractions and separations a priori, by selecting the most suitable salting-out agent and its concentration.
碱性萃取剂的金属萃取机理通常被描述为阴离子交换过程,但该机理并不能正确解释所有观察结果。本文提出了一个新的模型,用于从氯化物介质中提取金属的碱性萃取剂,该模型得到了甲基三辛基氯化铵和 Aliquat 336 氯化物体系的实验数据的支持。该模型基于以下假设:在水相中被水合作用稳定化程度最低的金属物种(即电荷密度最低的金属物种)比更稳定化的水合物种(即电荷密度更高的物种)更容易被萃取。一旦被转移到有机相中,萃取的物种就可以与有机相中可用的氯离子发生进一步的路易斯酸碱加合反应,形成带负电荷的氯络合物,这些络合物与有机阳离子结合。盐析剂会影响萃取,最可能的原因是降低了自由水分子的浓度,从而使水相中金属络合物的稳定性降低。提供的证据包括(1)萃取与过渡金属形态之间的关系,(2)不同盐析剂浓度对萃取效率的影响趋势,以及(3)HCl 在萃取体系中的行为。与阴离子交换模型相比,所提出的萃取模型更好地解释了实验观察结果,并允许通过选择最合适的盐析剂及其浓度,事先预测金属萃取和分离的最佳条件。