Title of article
Isothermal vapour–liquid equilibria and excess molar enthalpies of hex-2-yne + methyl butyl ether and hex-3-yne + dibutyl ether mixtures
Author/Authors
Boukais-Belaribi، نويسنده , , Ghénima and Belaribi، نويسنده , , Brahim Farid and Lohmann، نويسنده , , Juergën and Jose، نويسنده , , Jacques، نويسنده ,
Issue Information
روزنامه با شماره پیاپی سال 2007
Pages
7
From page
180
To page
186
Abstract
The vapour pressures of liquid hex-2-yne + methyl butyl ether (MBE) and hex-3-yne + dibutyl ether (DBE) binary mixtures and of the four pure components are measured by a static method in the temperature range from 263 to 354 K. The isoplethal T–P data are reported and correlated with the Antoine equation. Interpolated data are also reported. Excess molar Gibbs energies, GE, are calculated for several constant temperatures, taking into account the vapour-phase imperfection in terms of the second virial coefficients, and were fitted to the Redlich–Kister equation. Calorimetric excess enthalpy, HE, measurements for these binary mixtures are also reported at 298.15 K. The experimental VLE and HE data were used, examining the binary mixtures hex-2-yne + MBE and hex-3-yne + DBE in the framework of the DISQUAC and modified UNIFAC (Do) models.
Keywords
The modified UNIFAC (Do) model , The DISQUAC model , Excess enthalpy , Methyl butyl ether , Vapour–liquid equilibria , Hex-2-yne , dibutyl ether , Hex-3-yne
Journal title
Fluid Phase Equilibria
Serial Year
2007
Journal title
Fluid Phase Equilibria
Record number
1986724
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