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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  ( SCI-EXPANDED收录 EI收录)  

文献类型:期刊文献

英文题名:Isobaric vapour-liquid equilibrium for binary systems of ethyl iodide with ethanol, propionic acid and ethyl propionate at 101.3 kPa

作者:Pan, Jiahao[1];Li, Xiangjun[1];Zhang, Wujie[1];Cui, Wei[2];Zhou, Zhihong[2];Liu, Dianhua[1]

机构:[1]East China Univ Sci & Technol, State Key Lab Chem Engn, Shanghai 200237, Peoples R China;[2]Shanghai Huayi Energy Chem Co Ltd, Shanghai 200241, Peoples R China

年份:2019

卷号:132

起止页码:23

外文期刊名:JOURNAL OF CHEMICAL THERMODYNAMICS

收录:;EI(收录号:20185106269170);WOS:【SCI-EXPANDED(收录号:WOS:000459914300003)】;

语种:英文

外文关键词:Vapour-liquid equilibrium; Ethyl iodide; Ethanol; Propionic acid; Ethyl propionate; Correlation

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.

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