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.