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相关溶液的热化学研究:通过溶解度测量计算溶质 - 溶剂平衡常数

Thermochemical investigations of associated solutions: calculation of solute--solvent equilibrium constants from solubility measurements.

作者信息

Acree W E, McHan D R, Rytting J H

出版信息

J Pharm Sci. 1983 Aug;72(8):929-34. doi: 10.1002/jps.2600720822.

Abstract

A simple solution model that has lead to successful predictive equations for the partial molar excess properties of a solute in simple binary solvent mixtures containing only nonspecific interactions is extended to include association between the solute and one of the solvent components. An expression is derived and tested for its ability to describe anthracene solubilities in binary solvent mixtures containing benzene. The best description of the experimental solubilities requires the formation of a 1:1 anthracene-benzene complex, with a molarity-based equilibrium constant of KcAC approximately equal to 0.107 M-1. In comparison, a stoichiometric complexation model which attributes all solubility enhancement to the formation of anthracene-benzene complexes requires a somewhat larger equilibrium constant (KcAC approximately equal to 0.228 M-1) to describe the solubility behavior of anthracene in the benzene-n-heptane system. The results of these calculations illustrate that the determination of solute-solvent equilibrium constants from solubility data depends on the theoretical model used and the manner in which nonspecific interactions are incorporated into the model.

摘要

一个简单的溶液模型已被扩展,该模型曾得出了仅包含非特异性相互作用的简单二元溶剂混合物中溶质偏摩尔过量性质的成功预测方程,扩展后包括溶质与一种溶剂成分之间的缔合。推导了一个表达式,并测试了其描述蒽在含苯二元溶剂混合物中溶解度的能力。对实验溶解度的最佳描述需要形成1:1的蒽 - 苯络合物,基于摩尔浓度的平衡常数KcAC约等于0.107 M-1。相比之下,一个将所有溶解度增强归因于蒽 - 苯络合物形成的化学计量络合模型需要稍大的平衡常数(KcAC约等于0.228 M-1)来描述蒽在苯 - 正庚烷体系中的溶解度行为。这些计算结果表明,根据溶解度数据确定溶质 - 溶剂平衡常数取决于所使用的理论模型以及将非特异性相互作用纳入模型的方式。

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