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9 matching references were found.
Peres, A.M.; Macedo, E.A., Thermodynamic properties of sugars in aqueous solutions: correlation and prediction using a modified UNIQUAC model, Fluid Phase Equilib., 1996, 123, 71-95. [all data]
Liu, H.; Macedo, E.A., Accurate correlations for the self-diffusion coefficients of CO2, CH4, C2H4 , H2O, and D2O over wide ranges of temperature and pressure, J. Supercrit. Fluids, 1995, 8, 310-17. [all data]
Coutinho, J.P.; Macedo, E.A., Infinite-dilution activity coefficients by comparative ebulliometry. Binary systems containing chloroform and diethylamine, Fluid Phase Equilib., 1994, 95, 149-62. [all data]
Goncalves, A.S.; Macedo, E.A., Infinite-dilution activity coefficients by comparative ebulliometry: five systems containing ethyl formate, Fluid Phase Equilib., 1993, 85, 171-9. [all data]
Goncalves, R.M.C.; Simoes, A.M.N.; Albuquerque, L.M.P.C.; Macedo, E.A., Study of initial- and transition-state solvation in the solvolysis of tert- butyl halides in alcohols from infinite dilution activity coefficients, J. Phys. Org. Chem., 1993, 6, 133-8. [all data]
Dahl, S.; Macedo, E.A., The MHV2 model: a UNIFAC-based equation of state model for vapor-liquid and liquid-liquid equilibria of mixtures with strong electrolytes, Ind. Eng. Chem. Res., 1992, 31, 1195-201. [all data]
Alvarez Gonzales, J.R.; Macedo, E.A.; Soares, M.E.; Medina, A.G., Liquid-liquid equilibria for ternary systems of water-phenol and solvents: Data and representation with models, Fluid Phase Equilib., 1986, 26, 289. [all data]
Macedo, E.A.; Mendonca, J.M.; Medina, A.G., Vapor-liquid equilibrium for the systems ethyl formate + methyl ethyl ketone, ethyl formate + toluene and ethyl formate + methyl ethyl ketone + toluene: new unifac parameters for interactions between, Fluid Phase Equilib., 1984, 18, 197-210. [all data]
Macedo, E.A.; Rasmussen, P., Vapor-Liquid Equilibrium for the Binary Systems Ethyl Acetate-Acetic Acid and Ethyl Propionate-Propionic Acid, J. Chem. Eng. Data, 1982, 27, 463. [all data]