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首页> 外文期刊>The Journal of Chemical Thermodynamics >Isobaric vapour-liquid equilibrium for binary systems of ethyl iodide with ethanol, propionic acid and ethyl propionate at 101.3 kPa
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Isobaric vapour-liquid equilibrium for binary systems of ethyl iodide with ethanol, propionic acid and ethyl propionate at 101.3 kPa

机译:用乙醇,丙酸和丙酸乙酯在101.3kPa下乙酸乙酯和乙基乙基乙基乙酸乙酯的异蒸气液平衡

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摘要

Isobaric vapour-liquid equilibrium (VLE) data for the binary systems of ethyl iodide with ethanol, propionic acid and ethyl propionate at 101.3 kPa were measured in an Ellis equilibrium still, and the thermodynamic consistency of the experimental data was checked by the Herington area method and Van Ness method. The non-random two-liquid (NRTL), universal quasichemical (UNIQUAC), and Wilson models were applied to correlate the measured VLE data. All three models represent the experimental values quite well. The system (ethyl iodide + ethanol) presents a minimum azeotropic boiling point at 101.3 kPa, in which the azeotropic temperature and composition are 336.08 K and 63.445 mol% (ethyl iodide). The azeotropic behavior was not found in the other two systems. (C) 2018 Elsevier Ltd.
机译:在Ellis平衡静止的情况下测量用于乙醇,丙酸和丙酸乙酯的二元体系的异蒸气液平衡(VLE)数据,并在埃利斯平衡中测量了赫林顿地区方法的实验数据的热力学稠度 和van ness方法。 应用非随机的双液(NRTL),通用QuAsiChical(Uniquac)和Wilson模型来关联测量的VLE数据。 所有三种模型都代表了实验值。 该系统(乙基碘+乙醇)在101.3kPa处呈现最低共沸沸点,其中共沸温度和组合物为336.08k和63.445mol%(乙基碘)。 在其他两个系统中未发现共沸行为。 (c)2018年elestvier有限公司

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