Article ID Journal Published Year Pages File Type
203220 Fluid Phase Equilibria 2010 5 Pages PDF
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.

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Physical Sciences and Engineering Chemical Engineering Chemical Engineering (General)
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Phase equilibrium for the systems diisopropyl ether, isopropyl alcohol + 2,2,4-trimethylpentane and +n-heptane at 101.3 kPa
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