C. Duarte et al., Correlation of vapor-liquid equilibrium for carbon dioxide plus ethanol plus water at temperatures from 35 to 70 degrees C, SEP SCI TEC, 35(14), 2000, pp. 2187-2201
A simple mathematical model, based on polynomial functions, was used to cor
relate experimental vapor-liquid equilibrium (VLE) data for the CO2 + ethan
ol + water system. The data were collected from the literature for temperat
ures 35, 40, 50, 60, and 70 degreesC and pressures from 10 MPa to 18.5 MPa.
This model is able to reproduce the equilibrium compositions of the two ph
ases within the experimental error given in the group of selected publicati
ons.