| 1 |
Introduction of the amine group at cycloaliphatic hydrocarbon (c-CHNH2) for the modified UNIFAC (Dortmund) model and validation in multicomponent systems containing cyclohexylamine
Klauck M, Silbermann R, Metasch R, Unger S, Schmelzer J
Fluid Phase Equilibria, 314, 169, 2012 |
| 2 |
Phase equilibrium properties of the ternary mixture dibutyl ether plus toluene plus heptane at 313.15 K
Alonso-Tristan C, Segovia JJ, Chamorro CR, Martin MC, Villamanan MA
Fluid Phase Equilibria, 317, 84, 2012 |
| 3 |
Vapor pressures and activity coefficients of binary mixtures of 1-ethyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide with acetonitrile and tetrahydrofuran
Safarov J, Geppert-Rybczynska M, Hassel E, Heintz A
Journal of Chemical Thermodynamics, 47, 56, 2012 |
| 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 |
Vapor-liquid equilibria for the ternary system of carbon dioxide plus ethanol plus ethyl acetate at elevated pressures
Cheng CH, Chen YP
Fluid Phase Equilibria, 242(2), 169, 2006 |
| 6 |
Vapour-liquid equilibrium of octane enhancing additives in gasolines 7: Total pressure data and g(E) for the ternary mixture tert-amyl methyl ether (TAME), methanol and hexane at 313.15 K
Alonso-Tristan C, Segovia JJ, Chamorro CR, Montero EA, Villamanan MA
Fluid Phase Equilibria, 245(1), 52, 2006 |
| 7 |
Experimental investigation of the vapour-liquid equilibrium of binary and ternary mixtures containing dibutyl ether (DBE), cyclohexane and toluene at 313.15 K
Alonso-Tristan C, Segovia JJ, Chamorro CR, Villamanan MA
Fluid Phase Equilibria, 245(1), 57, 2006 |
| 8 |
Vapor-liquid equilibria for the ternary mixture of carbon dioxide plus 1-propanol plus propyl acetate at elevated pressures
Cheng CH, Tang M, Chen YP
Fluid Phase Equilibria, 248(1), 89, 2006 |
| 9 |
Vapor-liquid equilibrium of octane-enhancing additives in gasolines -6. Total pressure data and G(E) for binary and ternary mixtures containing 1, 1-dimethlethyl methyl ether (MTBE), methanol and n-hexane at 313.15 K
Alonso C, Montero EA, Chamorro CR, Segovia JJ, Martin MC, Villamanan MA
Fluid Phase Equilibria, 217(2), 157, 2004 |
| 10 |
Influence of water on the vapor-liquid equilibria, activity coefficients at infinite dilution and enthalpies of mixing for mixtures of N-methyl-2-pyrrolidone with C5 or C6 hydrocarbons
Fischer K, Gmehling J
Fluid Phase Equilibria, 218(1), 69, 2004 |
