Title of article :
Total pressure and excess Gibbs energy for the ternary mixture di-isopropyl ether + 1-propanol + benzene and its corresponding binary systems at 313.15 K
Author/Authors :
Marيa C. and Villamaٌلn، نويسنده , , R.M. and Chamorro، نويسنده , , C.R. and Villamaٌلn، نويسنده , , M.A. and Segovia، نويسنده , , J.J.، نويسنده ,
Issue Information :
روزنامه با شماره پیاپی سال 2006
Abstract :
Total pressure measurements are reported for the ternary system ‘di-isopropyl ether + 1-propanol + benzene’ and two of the binary systems involved ‘di-isopropyl ether + 1-propanol’ and ‘1-propanol + benzene’ at 313.15 K. Data reduction by Barkerʹs method provides correlations for GE using the Margules equation for the binary systems and the Wohl expansion for the ternary system. Wilson, NRTL and UNIQUAC models have been applied successfully to both the binary and the ternary systems.
Keywords :
ternary mixtures , Di-isopropyl ether (DIPE) , 1-propanol , Benzene , VLE data
Journal title :
Fluid Phase Equilibria
Journal title :
Fluid Phase Equilibria