Title of article
Vapour–liquid equilibrium for the systems diethyl sulphide + 1-butene, +cis-2-butene, +2-methylpropane, +2-methylpropene, +n-butane, +trans-2-butene
Author/Authors
Dell’Era، نويسنده , , Claudia and Pokki، نويسنده , , Juha-Pekka and Uusi-Kyyny، نويسنده , , Petri and Pakkanen، نويسنده , , Minna and Alopaeus، نويسنده , , Ville، نويسنده ,
Issue Information
روزنامه با شماره پیاپی سال 2010
Pages
8
From page
180
To page
187
Abstract
Isothermal vapour–liquid equilibrium was measured for the systems of diethyl sulphide + 1-butene, +cis-2-butene, and +2-methylpropene at 312.6 K, diethyl sulphide + n-butane was measured at 317.6 K, diethyl sulphide + trans-2-butene at 317.5 K, and diethyl sulphide + 2-methylpropane at 308.0 K. The pressure–temperature–total composition data were converted into pressure–temperature–liquid–vapour composition data using the method of Barker. Error estimates are provided for each variable. The isothermal parameters for the Wilson, NRTL and UNIQUAC activity coefficient models were regressed. The measurements were compared with the predictions by COSMO segment activity coefficient (COSMO-SAC) and UNIFAC.
Keywords
Vapour–liquid equilibrium , UNIFAC , COSMO-SAC , C4-hydrocarbon , Diethyl sulphide
Journal title
Fluid Phase Equilibria
Serial Year
2010
Journal title
Fluid Phase Equilibria
Record number
1987850
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