| 1 |
Liquid-Liquid Equilibria for Monoethylene Glycol plus Hexane and 2,2,4-Trimethylpentane, Water plus Hexane and 2,2,4-Trimethylpentane, Monoethylene Glycol plus Water plus Hexane, and Monoethylene Glycol + Water+2,2,4-Trimethylpentane in the Temperature Range between T=283.15 K and T=323.15 K
Razzouk A, Naccoul R, Mokbel I, Duchet-Suchaux P, Jose J, Rauzy E, Berro C
Journal of Chemical and Engineering Data, 55(4), 1468, 2010 |
| 2 |
Liquid-Liquid Equilibria for Monoethylene Glycol + Water + Alkane Systems in the Range (273 to 313) K and Atmospheric Pressure (vol 131, pg 1577, 2004)
Sentenac P, Berro C, Rauzy E, Mokbel I, Jose J
Journal of Chemical and Engineering Data, 55(4), 1755, 2010 |
| 3 |
Dew points of binary propane or n-butane plus carbon dioxide, ternary propane or n-butane plus carbon dioxide plus water, and quaternary propane or n-butane plus carbon dioxide plus water plus methanol mixtures: Measurement and modeling
Gil L, Avila S, Garcia-Gimenez P, Blanco ST, Berro C, Otin S, Velasco I
Industrial & Engineering Chemistry Research, 45(11), 3974, 2006 |
| 4 |
Dew-point curves of natural gas. Measurement and modeling
Avila S, Benito A, Berro C, Blanco ST, Otin S, Velasco I
Industrial & Engineering Chemistry Research, 45(14), 5179, 2006 |
| 5 |
Experimental vapor pressures of six n-alkanes (C-21, C-23, C-25, C-27, C-29, C-30) in the temperature range between 350 K and 460 K
Sawaya T, Mokbel I, Ainous N, Rauzy E, Berro C, Jose J
Journal of Chemical and Engineering Data, 51(3), 854, 2006 |
| 6 |
Experimental vapor pressures of alkyl and aryl sulfides - Prediction by a group contribution method
Sawaya T, Mokbel I, Rauzyb E, Saab J, Berro C, Jose J
Fluid Phase Equilibria, 226, 283, 2004 |
| 7 |
Liquid-liquid equilibria for monoethylene glycol plus water plus alkane systems in the range (273 to 313) K and atmospheric pressure
Sentenac P, Berro C, Rauzy E, Mokbel I, Jose J
Journal of Chemical and Engineering Data, 49(6), 1577, 2004 |
| 8 |
Representation for binary mixtures of n-alcohols plus sub and supercritical CO2 by a group-contribution method
Artal M, Embid JM, Velasco I, Berro C, Rauzy E
Fluid Phase Equilibria, 178(1-2), 119, 2001 |
| 9 |
Experimental vapour pressures of 13 secondary and tertiary alcohols - Correlation and prediction by a group contribution method
N'Guimbi J, Berro C, Mobkel I, Rauzy E, Jose J
Fluid Phase Equilibria, 162(1-2), 143, 1999 |
| 10 |
Density of methanol+water between 250K and 440K and up to 40MPa and vapor-liquid equilibria from 363K to 440K
Sentenac P, Bur Y, Rauzy E, Berro C
Journal of Chemical and Engineering Data, 43(4), 592, 1998 |
