Study on the Vapor-Liquid Equilibrium of Electrolyte Solutions

博士 === 國立臺灣科技大學 === 化學工程研究所 === 81 === The objective of this study is to develop a model describing the behavior of vapor-liquid equilibrium of electrolyte solutions. Three major parts are included in this study. The first part is accomplished by applying...

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Bibliographic Details
Main Authors: Lin Cheng Long, 林振隆
Other Authors: Tseng Hsieng Cheng
Format: Others
Language:zh-TW
Published: 1993
Online Access:http://ndltd.ncl.edu.tw/handle/26043967175220210208
Description
Summary:博士 === 國立臺灣科技大學 === 化學工程研究所 === 81 === The objective of this study is to develop a model describing the behavior of vapor-liquid equilibrium of electrolyte solutions. Three major parts are included in this study. The first part is accomplished by applying the Poisson-Boltzmann equation to describe the ion-ion long-range interaction and the concept of solvation to describe the ion-molecule short-range interaction. The developed model contains three characteristic parameters and is able to estimate mean activity coefficients and osmotic coefficients fairly well for 144 aqueous electrolyte solutions at 25.degree.C. In addition, the proposed model has been also satisfactorily applied to non-aqueous electrolyte solutions and systems with temperatures other than 25.degree.C. The only disadvantage of this model is the necessity of solving an ordinary differential equation, thus to overcome this, a much simpler model is proposed. The new model is similar to the first proposed one containing three characteristic parameters. It is as good as the original model, although a slightly larger average deviations appear for some systems, and has the major advantage of fewer parameters comparing to the models available in the literature. The second part of this study is the experiments of vapor- liquid- equilibrium of electrolyte solutions. The experimental data collected are vapor-liquid-equilibrium and vapor-liquid- liquid- equilibrium. The later is important for the processes such as distillation and extraction, and is seldom published in the literature. The last part of this study is to develop a predictive model for the vapor-liquid-equilibrium of electrolyte solutions (one electrolyte, two solvents). The parameters used in this model are directly obtained from the binary systems, no additional parameters are needed. So this model is simple and requires less computation effort. It predicts well for both isothermal and isobaric systems.