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正己烷-碳酸二甲酯系统汽-液平衡研究
引用本文:张江平,王国斌,刘芃,许红云. 正己烷-碳酸二甲酯系统汽-液平衡研究[J]. 天然气化工, 2006, 31(4): 75-78
作者姓名:张江平  王国斌  刘芃  许红云
作者单位:西南化工研究设计院,成都,610025
摘    要:采用双循环式汽液平衡釜测定了正己烷碳酸二甲酯系统于101.325kPa下的汽液平衡数据,并用统计学方法对其进行了热力学一致性检验。该系统存在最低恒沸物:恒沸点65.73℃,正己烷摩尔分率x1=0.755。其数据用Wilson、NRTL和UNIQUAC方程进行了关联,关联结果表明具有很高的精度。

关 键 词:正己烷  碳酸二甲酯  汽-液平衡
文章编号:1001-9219(2006)04-75-04
修稿时间:2005-01-06

Research on the Vapor-Liquid Equilibrium of n-Hmeptane-Dimethyl Carbonate System
ZHANG Jiang-ping,WANG Guo-bin,LIU Peng,XU Hong-yun. Research on the Vapor-Liquid Equilibrium of n-Hmeptane-Dimethyl Carbonate System[J]. Natural Gas Chemical Industry, 2006, 31(4): 75-78
Authors:ZHANG Jiang-ping  WANG Guo-bin  LIU Peng  XU Hong-yun
Affiliation:The Southwest Research and Design Institute of Chemical Industry, Chengdu 610225, China
Abstract:Vapor-liquid equilibrium (VLE) data of n-hexane-DMC system at 101.325kPa has been measured with a modified Rost equilibrium still. This system has lower azeotropic point of 65.73℃ and the azeotropic composition of n-hexane x1 is 0.755. The experimental data were correlated with Wilson, NRTL and UNIQUAC equations and the results had good accuracy.
Keywords:n-hexane  dimethyl carbonate  vapor-liquid equilibrium (VLE)
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