Title of article
Vapour–liquid equilibrium of octane enhancing additives in gasolines 7: Total pressure data and gE for the ternary mixture tert-amyl methyl ether (TAME), methanol and hexane at 313.15 K
Author/Authors
Alonso-Tristلn، نويسنده , , C. and Segovia-Martيnez، نويسنده , , J.J. and Chamorro، نويسنده , , C.R. and Montero، نويسنده , , E.A. and Villamaٌلn، نويسنده , , M.A.، نويسنده ,
Issue Information
روزنامه با شماره پیاپی سال 2006
Pages
5
From page
52
To page
56
Abstract
Experimental VLE data at 313.15 K for the ternary system TAME + methanol + hexane are reported. A static method using an isothermal total pressure cell (Van Ness’ technique) has been employed. Reduction of the experimental data has been done by Barkerʹs method using Wohl expansion, NRTL, Wilson and UNIQUAC equations. Moreover, experimental results have been compared to predictions for the ternary system obtained from its corresponding binaries from Wilson, NRTL and UNIQUAC models.
Keywords
Data , VLE , Methanol , TAME , Excess Gibbs energy
Journal title
Fluid Phase Equilibria
Serial Year
2006
Journal title
Fluid Phase Equilibria
Record number
1985981
Link To Document