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高压下CO2异丙醚体系的汽液相平衡
引用本文:朱彩凤,郑丹星,武向红,何伟,荆树宏.高压下CO2异丙醚体系的汽液相平衡[J].北京化工大学学报(自然科学版),2007,34(4):350-353.
作者姓名:朱彩凤  郑丹星  武向红  何伟  荆树宏
作者单位:北京化工大学化学工程学院, 北京 100029
摘    要:采用带有可视石英玻璃窗的高压汽液相平衡装置,测定了压力0.5~25MPa、温度265.15~333.15K条件下CO2异丙醚体系的二元汽液相平衡数据,并通过了热力学一致性检验。用Peng-Robinson(PR)状态方程对CO2-异丙醚体系的汽液相平衡数据进行关联,得到该方程的二元交互作用参数。结果表明,体系的汽液相平衡数据计算值与实验值偏差较小,可采用PR方程对CO2-异丙醚二组分物系的汽液相平衡数据进行预测。

关 键 词:汽液平衡  CO2  异丙醚  Peng-Robinson状态方程  热力学一致性检验  汽液平衡    CO2  异丙醚  Peng-Robinson状态方程    热力学一致性检验
修稿时间:2007-01-24

High pressure vapor-liquid equilibrium for the carbon dioxide-diisopropyl ether binary system
ZHU CaiFeng,ZHENG DanXing,WU XiangHong,HE Wei,JING ShuHong.High pressure vapor-liquid equilibrium for the carbon dioxide-diisopropyl ether binary system[J].Journal of Beijing University of Chemical Technology,2007,34(4):350-353.
Authors:ZHU CaiFeng  ZHENG DanXing  WU XiangHong  HE Wei  JING ShuHong
Institution:College of Chemical Engineering, Beijing University of Chemical Technology, Beijing 100029, China
Abstract:An experimental device incorporating vision windows,for measuring vapor-liquid equilibrium(VLE) data at high-pressures is described.Online-sampling of the vapor and liquid phases can be carried out by gas chromatography.The vapor-liquid equilibrium(VLE) data for the binary system carbon dioxide-diisopropyl ether have been measured at 265.15-333.15 K and 0.5-2.5 MPa.The experimental data set passed the thermodynamic consistency test.An isothermal correlation of the experimental data has been carried out based on the Peng-Robinson(PR) equation and the correlated results accord with the experimental data.The results show that the VLE data for the binary system carbon dioxide-diisopropyl ether can be calculated by the PR equation.
Keywords:vapor-liquid equilibrium  carbon dioxide  diisopropyl ether  Peng-Robinson equation  thermodynamic consistency test
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