首页> 外文期刊>Journal of Chemical and Engineering Data: the ACS Journal for Data >Vapor-Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing 2-Ethoxy-2-methylpropane or 2-Ethoxy-2-methylbutane and Acetonitrile or Propanenitrile
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Vapor-Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing 2-Ethoxy-2-methylpropane or 2-Ethoxy-2-methylbutane and Acetonitrile or Propanenitrile

机译:包含2-乙氧基-2-甲基丙烷或2-乙氧基-2-甲基丁烷和乙腈或丙腈的二元混合物的汽液平衡,过量摩尔焓和过量摩尔体积

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摘要

Vapor-liquid equilibrium (VLE), excess molar enthalpies (H~E), and excess molar volumes (Vs) provide complementary data for thermodynamic models. In this work, new data of binary mixtures of acetonitrile (ACN) or propanenitrile (PPN) with 2-ethoxy-2-methylpropane (ETBE) or 2-ethoxy-2-mefhylbutane (TAEE) are reported. Isothermal VLE data were measured by using a circulation still at 333 K for ETBE + ACN, at 343 K for TAEE + ACN, and at 363 K for TAEE + PPN. H~E were measured by using a SETARAM C80 calorimeter equipped with a flow mixing cell at 298 K for all four binary systems. V~E were measured by using an Anton Paar DMA 5I2P densimeter at 298 K for all four binary systems. H~E data and measured VLE data, or literature VLE data for the binary system of ETBE and PPN, were used for the optimization of Wilson model parameters by using VLEFIT software. Redlich-Kister equation parameters were separately regressed for the V~E data.
机译:汽液平衡(VLE),过量的摩尔焓(H〜E)和过量的摩尔体积(Vs)为热力学模型提供了补充数据。在这项工作中,报告了乙腈(ACN)或丙腈(PPN)与2-乙氧基-2-甲基丙烷(ETBE)或2-乙氧基-2-甲基丁烷(TAEE)的二元混合物的新数据。等温VLE数据是通过使用ETBE + ACN在333 K,TAEE + ACN在343 K和TAEE + PPN在363 K的循环测量的。通过使用SETARAM C80量热计(对于所有四个二元系统,均配备有在298 K的混流池)测量H〜E。通过使用Anton Paar DMA 5I2P密度计在所有四个二进制系统中在298 K下测量V〜E。使用VLEFIT软件,使用H〜E数据和测得的VLE数据,或ETBE和PPN二元系统的文献VLE数据来优化Wilson模型参数。对V〜E数据分别回归Redlich-Kister方程参数。

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