Studies of Salt Effects on the Vapor-Liquid Equilibrium of the Water-Organic Acid and Methyl tert-Butyl Ether-Methanol Systems

碩士 === 國立台灣工業技術學院 === 化學工程技術研究所 === 85 === The objective of this study is to investigate the behavior of vapor-liquid equilibria of electrolyte solutions, including experimental measurements and theoretical calculations. In the experiment part, a static-t...

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Bibliographic Details
Main Authors: Yao, Tian-Si, 姚天賜
Other Authors: Tseng Hsieng-Cheng
Format: Others
Language:zh-TW
Published: 1997
Online Access:http://ndltd.ncl.edu.tw/handle/25589741635503801937
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Summary:碩士 === 國立台灣工業技術學院 === 化學工程技術研究所 === 85 === The objective of this study is to investigate the behavior of vapor-liquid equilibria of electrolyte solutions, including experimental measurements and theoretical calculations. In the experiment part, a static-type vapor-liquid equilibrium (VLE) apparatus was employed to measure the equilibrium data for two systems of electrolyte solutions with salt concentrations varying from zero to saturation: 1. organic acid aqueous solutions system, (1) water-propionic acid , with NaCl as the electrolyte, (2) water-acetic acid, with NaCl or NH4Cl as the electrolyte; 2. MTBE-methanol system, with NaCl, KI, or LiCl as the electrolyte. The experimental data obtained satisfy the thermodynamic consistency tests of both area and point methods. In the theoretical calculation part, either semi-chemical theory model or chemical theory model, combined with the modified Wilson model, was used to predict the VLE of electrolyte solutions for the organic acid aqueous solutions system, where dimerization occurs. As for the MTBE-methanol system, where no dimerization occurs, the Peng-Robinson equation of state was employed together with the modified Wilson activity coefficient model to predict the VLE of the electrolyte solutions of this system. The predicted results for all three systems agree quite well with the experimental data. The parameters of the modified Wilson model was calculated for each system by the method of vapor pressure lowering, and the method of boiling point elevation as well. The parameters obtained by both methods were then used to calculate the temperatures and vapor compositions of the VLE. It was found that the calculated results by both methods agree equally well with the experimental data.