New
isothermal binary vapor–liquid equilibrium (VLE) systems
of 1-pentanol + 2,2,4-trimethylpentane at 350.2, 360.2, and 370.2
K, methyl-tert-butyl-ether + 2,2,4-trimethylpentane
at 307.2, 317.2, and 327.2 K, and methyl-tert-butyl-ether
+ 1-pentanol at 317.2 and 327.2 K were measured. The vapor–liquid
equilibrium data were measured using a dynamic low pressure glass
still. The experimental data were regressed using the γ–Φ
approach (combined method) with the Wilson, NRTL, and UNIQUAC activity
coefficient models for description of the liquid phase nonideality.
The virial equation of state with the Hayden and O’Connell
correlation for the second virial coefficient was used to describe
the vapor phase nonideality. The system of 2,2,4- trimethylpentane
+ 1-pentanol exhibited a minimum boiling azeotrope. The methyl-tert-butyl-ether + (2,2,4-trimethylpentane/1-pentanol) systems
showed positive deviation from Raoult’s law. The aforementioned
activity coefficient models correlated the experimental data well.
The thermodynamic consistency of the experimental data was determined
using the point test of Van Ness and the Herrington area test.