[1] Cheng, Chen-His, Chen, Yan-Ping, Vapor-Liquid Equilibria of Carbon Dioxide with Isopropyl Acetate, Diethyl Carbonate and Ethyl Butyrate at Elevated Pressures, Fluid Phase Equilibria, 234, 77 (2005).
[2] Bamberger, A., Sieder, G., Maurer, G., High-Pressure Phase Equilibrium of the Ternary System Carbon Dioxide + Water + Acetic Acid at Temperatures from 313 to 353 K, J. of Supercritical Fluids, 32, 15 (2004).
[3] Kodama, D., Miyazaki, J., Kato, M., Sako, T., High Pressure Phase Equilibrium for Ethylene + 1-Propanol System at 283.65 K, Fluid Phase Equilibria, 219, 19 (2004).
[4] Stryjek, R., Vera, J. H., PRSV: An Improved Peng-Robinson Equation of State with New Mixing Rule for Strongly Nonideal Mixtures, The Canadian Journal of Chemical Engineering, 64, 334 (1986).
[5] Huron, M. J., Vidal, J., New Mixing Rules in Simple Equations of State for Representing Vapor-Liquid Equilibria of Strongly Nonideal Mixtures, Fluid Phase Equilibria, 3, 255, (1979).
[6] Dahl, S., Michelsen, M. L., High-Pressure Vapor-Liquid Equilibrium with a UNIFAC-Based Equation of State, AIChE J., 36, 12, 1829 (1990).
[7] Heidemann, R. A., Kokal, S. L., Combined Excess Free Energy Models and Equations of State, Fluid Phase Equilibrium, 56, 17 (1990).
[8] Holderbaum, T., Gmehling, J., PRSK: A Group Contribution Equation of State Based on UNIFAC, Fluid Phase Equilibrium, 70, 251 (1990).
[9] Wong, S. H., Sandler, S.I., A Theoretically Correct Mixing Rule for Cubic Equations of State, AIChE J., 38, 5, 671 (1992).
[10] Orbey, H., Sandler, S.I., Reformulation of Wong-Sandler Mixing Rule for Cubic Equations of State, AIChE J., 41, 3, 683 (1995).
[11] Twu, C., Coon, J. E., Mixing Rules Constrained by vdW Mixing Rule and Second Virial Coefficient, AIChE J., 42, 3212 (1996).
[12] Renon, H. and Prausnitz, J. M., Local Compositions in Thermodynamic Excess Functions for Liquid Mixtures, AIChE J., 14, 135 (1965).
[13] Van Laar, J. J., Z. Phys. Chem., 72, 723 (1910).
[14] Larsen, Bent L., Rasmussen, P., Fredenslund, A., A Modified UNIFAC Group-Contribution Model for Prediction of Phase Equilibria and Heats of Mixing, Ind. Eng. Chem. Res., 26, 2274 (1987).
[15] Abrams, D. S. and Prausnitz, J. M., Statistical Thermodynamics of Liquid Mixtures: A New Expression for the Excess Gibbs Energy of Partly or Completely Miscible Systems, AIChE J., 21, 116 (1975).
[16] Khodakarami, B., Modarress, H. and Lotfollahi, M. N., Study of the High-Pressure Vapor-Liquid Equilibria for Strongly Non-Ideal Binary and Ternary Mixtures, Canadian Journal of Chemical Engineering, 83, 354 (2005).
[17] Ruivo, R., Paiva, A. and Simoes, P., Phase Equilibria of the Ternary System Methyl Oleate / Squalene / Carbon Dioxide at High Pressure Conditions, J. of Supercritical Fluids, 29, 77 (2004).
[18] Rudolph, E. S. J., Langeveld, J. H., de Loos, Th. W. and Swaan Arons, J. de, Phase Behavior of Water + Nonionic Surfactant Systems: Experiments and Modeling Applying the Peng-Robinson Equation of State with the Wong-Sandler Mixing Rules and the UNIQUAC gE-model , Fluid Phase Equilibria, 173, 1 (2000).
[19] Keshtkar, A., Jalali, F. and Moshfeghian, M., Evaluation of Vapor-Liquid Equilibrium of CO2 Binary Systems Using UNIQUAC- Based Huron-Vidal Mixing Rules, Fluid Phase Equilibria, 140,
1-2, 107, (1997).
[20] Panagiotopoulos, A. Z., and Reid, R.C., "New Mixing Rules for Cubic Equation of State for Highly Polar Assymetric Mixtures", ACS symposium Series 300, American Chemical Society, Washington, D.C., 571-582 (1986).
[21] Adachi, Y., and Sugie, H., A New Mixing Rule- Modified Conventional Mixing Rule, Fluid Phase Equilibria, 23, 103 (1986).
[22] Sandoval, R., Wilseck-Vera, G., and Vera, I. H., Prediction of the Ternary Vapor-Liquid Equilibria with the PRSV Equation of State, Fluid Phase Equilibria, 52, 119 (1989).
[23] Smith, J. M., Van Ness, H. C. and Abbott, M. M., “Introduction to Chemical Engineering Thermo-dynamics”, Sixth Edition, McGrow-Hill (2001).
[24] Elbaccouch, M. M., Raymond, M. B. and Elliot, J.Richard, J. Chem. Eng. Data., 45, 280 (2000).
[25] Gmehling, J., Onken, V., Vapor-Liquid Equilibrium for Mixture of Low Boiling Substances, Dechema, Vol I, Part 2a (1986).
[26] Wu, H. S., Hagewiesche, D., and Sandler, S. I., Vapor - Liquid Equilibria of 2-Propanol + Water + N,N-dimethyl Formamide, Fluid Phase Equilibria, 43, 77 (1988).