Experimental analysis of vapour-liquid phase equilibria for binary systems of diethyl carbonate with methyl, ethyl, isopropyl, n-butyl and isoamyl acetates at 95 kPa

被引:3
作者
Bhoi, Bharat R. [1 ]
Mali, Nilesh A. [1 ]
Joshi, Sunil S. [1 ]
机构
[1] CSIR Natl Chem Lab, Chem Engn & Proc Dev Div, Dr Homi Bhabha Rd, Pune 411008, Maharashtra, India
关键词
Isobaric; VLE; Diethyl carbonate; Methyl acetate; Ethyl acetate; Isopropyl acetate; PLUS DIMETHYL CARBONATE; ACETIC-ACID; TERNARY-SYSTEMS; PROPYL ACETATE; METHANOL; WATER; MIXTURES; ETHANOL; SEPARATION; ALCOHOL;
D O I
10.1016/j.jct.2020.106189
中图分类号
O414.1 [热力学];
学科分类号
摘要
Experimental analysis of vapour-liquid phase equilibrium (VLE) for five binary pairs of diethyl carbonate (DEC) with methyl acetate, ethyl acetate, isopropyl acetate, n-butyl acetate and isoamyl acetate was carried out in this study. VLE data were generated experimentally at local atmospheric pressure of 95 kPa in a glass dynamic recirculation still. Reliability of data was checked with the thermodynamic consistency tests by Van Ness, infinite dilution, pure component and mean absolute deviation test. Experimental data was found to be thermodynamically consistent with all tests and data was regressed with Wilson, NRTL and UNIQUAC activity coefficient models to determine binary interaction parameters. Binary pair of DEC with n-butyl acetate has shown azeotropic behaviour with minimum boiling azeotrope and a close boiling behaviour through-out the composition range. No azeotropic behaviour was observed for the rest of the binary pairs. (c) 2020 Elsevier Ltd.
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页数:8
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