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首页> 外文期刊>Journal of Chemical and Engineering Data: the ACS Journal for Data >Isothermal Vapor-Liquid Equilibria for Methyl-2,2-dimethylethyl Ether + 2-Methylpropan-2-ol, Diethyl Ether + Ethyl-2,2-dimethyletyle Ether, 2-Methyl-2-butene + (2-Methylbutan-2-ol), and Diisopropyl Ether + Octane
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Isothermal Vapor-Liquid Equilibria for Methyl-2,2-dimethylethyl Ether + 2-Methylpropan-2-ol, Diethyl Ether + Ethyl-2,2-dimethyletyle Ether, 2-Methyl-2-butene + (2-Methylbutan-2-ol), and Diisopropyl Ether + Octane

机译:甲基-2,2-二甲基乙基醚+ 2-甲基丙烷-2-醇,二乙基醚+乙基-2,2-二甲基乙基醚,2-甲基-2-丁烯+(2-甲基丁-2-的等温蒸气-液体平衡醇)和二异丙醚+辛烷

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摘要

Isothermal vapor-liquid equilibrium data for four binary systems methyl-2,2-dimethylethyl ether + 2-methylpropan-2-ol, diethyl ether + ethyl-2,2-dimethylethyl ether, 2-methyl-2-butene + 2-methylbutan-2-ol, and diisopropyl ether + octane were collected at two temperatures using a modified Malanowski still. The vivial equation truncated at the second virial coefficient was used to calculate the vapor-phase fugacity coefficients. The liquid-phase activity coefficient data were fitted to the van Laar, Wilson, and NRTL equations.
机译:四个二元体系甲基-2,2-二甲基乙基醚+ 2-甲基丙烷-2-醇,乙醚+乙基-2,2-二甲基乙基醚,2-甲基-2-丁烯+ 2-甲基丁烷的等温气液平衡数据使用改良的Malanowski蒸馏器在两个温度下收集-2-ol和二异丙基醚+辛烷。用第二维里系数截断的维特方程来计算气相逸度系数。将液相活度系数数据拟合到van Laar,Wilson和NRTL方程。

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