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针对二甲醚生产过程中的汽液相平衡问题,本文提出了适于描述含CO2、DME和CH3OH体系的NRTL-PR模型组合,并以此模型计算了大量关于CO2-DME-CH3OH体系的三元VLE数据,绘制出几组等温、等压三元相图.可以认为,此模型得到的数据和相图能准确地反映含二甲醚体系的VLE关系,是实际生产工艺的研究与开发的重要基础.

参考文献

[1] 童景山,梁燕波.新能源-二甲醚(DME)的热物理性质的研究[C].中国工程热物理学会工程热力学与能源利用学术会议论文集,2002:495-499.
[2] Tsang C Y;Streett W B .Vapor-Liquid Equilibrium in the System Carbon Dioxide/Dimethyl Ether[J].Chemical Engineering Data,1981,26(06):155-159.
[3] Jonasson A;Persson O;Fredenslund A .High-Pressure Solubility of Carbon Dioxide and Carbon Monoxide in Dimethyl Ether[J].Chemical Engineering Data,1995,40(01):296-300.
[4] Chang E;Calado J;Streett W .Vapor-Liquid Equilibrium in the System Dimethyl Ether/Methanol from 0 to 180℃and at Pressures to 6 7 MPa[J].Chemical Engineering Data,1982,27(03):293-298.
[5] Mariana Teodorescu;Peter Rasmussen .High-Pressure Vapor-Liquid Equilibria in the Systems Nitrogen + Dimethyl Ether, Methanol + Dimethyl Ether, Carbon Dioxide + Dimethyl Ether + Methanol, and Nitrogen + Dimethyl Ether + Methanol[J].Journal of Chemical and Engineering Data: the ACS Journal for Data,2001(3):640-646.
[6] Hong J H;Kobayashi R .Vapor-Liquid Equilibrium Studies for the Carbon Dioxide-Methanol System[J].Fluid Phase Equilibria,1988,41:269-276.
[7] Suzuki K;Sue H .Isothermal Vapor-Liquid Equilibrium Data for Binary Systems at High Pressures: Carbon Dioxide-Methanol, Carbon Dioxide-Ethanol, Carbon Dioxide-1-Propanol, Methane-Ethanol, Methane-1-Propanol, Ethane-Ethanol, and Ethane-1-Propanol Systems[J].Chemical Engineering Data,1990,35(01):63-66.
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