Abstract
This article reports vapour–liquid equilibrium data in three binary systems, namely 2,3-dimethylbutane+diisopropyl ether, 2,3-dimethylbutane+3-methyl-2-butanone, and diisopropyl ether+3-methyl-2-butanone and in one ternary system, 2,3-dimethylbutane+diisopropyl ether+3-methyl-2-butanone. The data were measured isothermally at 313.15, 323.15, and 333.15K covering the pressure range of 13–108kPa. The binary vapour–liquid equilibrium data were correlated using the Wilson and NRTL equations by means of a robust algorithm for processing all isotherms together. The resulting parameters were then used to calculate phase behaviour in the ternary system and to comparison the calculated with experimental data.
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