VAPOR-LIQUID-EQUILIBRIA AT 1-ATM FOR TERNARY AND QUATERNARY SYSTEMS COMPOSED OF ACETONE, METHANOL, 2-PROPANOL, AND 1-PROPANOL

被引：15

作者：

GULTEKIN, N

机构：

[1] Faculty of Arts and Sciences, Karadeniz Technical University

来源：

JOURNAL OF CHEMICAL AND ENGINEERING DATA | 1990年 / 35卷 / 02期

关键词：

Alcohols--Phase Equilibria - Methanol--Mixing - Mixtures--Phase Equilibria - Thermodynamics--Calculations;

D O I：

10.1021/je00060a010

中图分类号：

O414.1 [热力学];

学科分类号：

摘要：

The vapor-liquid equilibrium data for each system composed of acetone, methanol, 2-propanol, and 1-propanol at the isobarlc condition of 1 atm are presented. The experimental data of the binary systems were used to calculate the binary parameters of the Wilson equation. These binary parameters have been used to calculate vapor-phase compositions and boiling points of related ternary and quarternary systems. Calculated vapor-phase compositions and boiling points have been obtained very close to the experimental data for each system investigated. © 1990, American Chemical Society. All rights reserved.

引用

页码：132 / 136

页数：5

共 20 条

[1] STATISTICAL THERMODYNAMICS OF LIQUID-MIXTURES - NEW EXPRESSION FOR EXCESS GIBBS ENERGY OF PARTLY OR COMPLETELY MISCIBLE SYSTEMS [J].