10.1021/acs.jced.8b00855.s001 Akash Patel Akash Patel Chintan Modi Chintan Modi Milind Joshipura Milind Joshipura Nitin Bhate Nitin Bhate Measurement and Correlation of Isobaric Vapor Liquid Equilibrium Data for Cyclopentyl Methyl Ether and Cyclopentanol American Chemical Society 2019 Isobaric Vapor Liquid Equilibrium Data Deviation plots 101.79 kPa CP UNIQUAC models Antoine equation NRTL model predictions equilibrium CPME components cyclopentyl methyl ether literature data Pure component Wilson model Cyclopentyl Methyl Ether vapor 2019-01-28 22:04:25 Journal contribution https://acs.figshare.com/articles/journal_contribution/Measurement_and_Correlation_of_Isobaric_Vapor_Liquid_Equilibrium_Data_for_Cyclopentyl_Methyl_Ether_and_Cyclopentanol/7640264 Isobaric vapor–liquid equilibrium data for pure components cyclopentyl methyl ether (CPME) and cyclopentanol (CP) and their binary mixtures was generated using a modified ebulliometer. This data has been reported for five different pressures in the range of 71.50 to 101.79 kPa. Pure component boiling points were correlated using the Antoine equation and compared with the literature data. Binary vapor–liquid equilibrium data was modeled using Wilson, NRTL, and UNIQUAC models. Deviation plots for experimental and predicted temperatures are given. UNIQUAC and NRTL model predictions showed a better fit with the experimental values relative to the Wilson model.