Title of article
Phase equilibrium for the systems diisopropyl ether, isopropyl alcohol + 2,2,4-trimethylpentane and +n-heptane at 101.3 kPa
Author/Authors
Lladosa، نويسنده , , Estela and Montَn، نويسنده , , Juan B. and Burguet، نويسنده , , MھCruz، نويسنده ,
Issue Information
روزنامه با شماره پیاپی سال 2010
Pages
5
From page
135
To page
139
Abstract
Consistent vapour–liquid equilibrium data for the ternary systems diisopropyl ether + isopropyl alcohol + 2,2,4-trimethylpentane and diisopropyl ether + isopropyl alcohol + n-heptane are reported at 101.3 kPa. The vapour–liquid equilibrium data have been correlated by Wilson, NRTL and UNIQUAC equations. The ternary systems do not present ternary azeotropes.
Keywords
diisopropyl ether , Isopropyl alcohol , n-Heptane , Activity-coefficient models , Vapour–liquid equilibrium , 2 , 4-Trimethylpentane , 2
Journal title
Fluid Phase Equilibria
Serial Year
2010
Journal title
Fluid Phase Equilibria
Record number
1987752
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