Isobaric vapor−liquid equilibrium data for pure components as well as binary mixtures of 2-ethoxyethanol−2-ethoxyethyl acetate was generated using a modified ebulliometer. Measurements are reported for five different pressures in the range of (53 to 101) kPa. Pure component vapor pressures were correlated using the Antoine correlation and compared with the literature data. Binary mixture isobaric data was modeled using the Margules 2-suffix, Margules 3-suffix, van Laar, Wilson, nonrandom two-liquid (NRTL), and universal quasichemical (UNIQUAC) equations. Deviation plots for experimental and predicted temperatures are given.

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