1 |
Measurements by using an automatic pressure control and predictions of isobaric VLE at 1.5 MPa for binary mixtures of methyl acetate, ethyl acetate, 1-propanol and 1-butanol Susial P, Vera DG, Montesdeoca I, Susial R, Stevenson SD, Melian NP Chemical Engineering Research & Design, 152, 242, 2019 |
2 |
Measurement and modelization of VLE of binary mixtures of propyl acetate, butyl acetate or isobutyl acetate with methanol at pressure of 0.6 MPa Susial P, Garcia D, Susial R, Clavijo YC, Martin A Chinese Journal of Chemical Engineering, 24(5), 630, 2016 |
3 |
Determination and thermodynamic evaluation of isobaric VLE of methyl acetate or ethyl acetate with 2-propanol at 0.3 and 0.6 MPa Susial P, Susial R, Estupinan EJ, Castillo VD, Rodriguez-Henriquez JJ, Apolinario JC Fluid Phase Equilibria, 375, 1, 2014 |
4 |
Vapor Pressure and VLE Data Measurements on Ethyl Acetate/Ethanol Binary System at 0.1, 0.5, and 0.7 MPa Susial P, Sosa-Rosario A, Rodriguez-Henriquez JJ, Rios-Santana R Journal of Chemical Engineering of Japan, 44(3), 155, 2011 |
5 |
VLE Data of Methyl Acetate plus Methanol at 1.0, 3.0 and 7.0 Bar with a New Ebulliometer Susial P, Rios-Santana R, Sosa-Rosario A Journal of Chemical Engineering of Japan, 43(8), 650, 2010 |
6 |
Isobaric vapour-liquid equilibrium of binary and ternary mixtures containing cyclohexane, n-hexane, 1,3-dioxolane and 1-butanol at 40.0 and 101.3 kPa Gascon I, Martin S, Artigas H, Lopez MC, Lafuente C Chemical Engineering Journal, 88(1-3), 1, 2002 |