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18 matching references were found.

Plesnar, Z.; Fu, Y.-H.; Sandler, S.I.; Orbey, H., Vapor-Liquid Equilibrium of the Acetic Acid + Octane Binary System at 323.1 5 K and 343.15 K, J. Chem. Eng. Data, 1996, 41, 799-801. [all data]

Orbey, H.; Sandler, S.I., A comparison of various cubic equation of state mixing rules for the simultaneous description of excess enthalpies and vapor-liquid equilibria, Fluid Phase Equilib., 1996, 121, 67-83. [all data]

Orbey, H.; Sandler, S.I., Vapor-liquid equilibria of binary mixtures of alkanols with alkanes from atmospheric pressure to the critical point, Int. J. Thermophys., 1995, 16, 695-704. [all data]

Orbey, H.; Sandler, S.I., On the combination of equation of state and excess free energy models, Fluid Phase Equilib., 1995, 111, 53-70. [all data]

Fu, Y.-H.; Sandler, S.I.; Orbey, H., A Modified UNIQUAC Model That Includes Hydrogen Bonding, Ind. Eng. Chem. Res., 1995, 34, 4351-63. [all data]

Tiryaki, A.; Gueruez, G.; Orbey, H., Liquid-liquid equilibria of ternary systems of water + acetone and C5 and C8 alcohols at 298, 303 and 308 K, Fluid Phase Equilib., 1994, 94, 267-80. [all data]

Huang, H.; Sandler, S.I.; Orbey, H., Vapor-liquid equilibria of some hydrogen + hydrocarbon systems with the Wong-Sandler mixing rule, Fluid Phase Equilib., 1994, 96, 143-53. [all data]

Orbey, H.; Sandler, S.I.; Wong, D.S.H., Accurate equation of state predictions at high temperatures and pressures using the existing UNIFAC model, Fluid Phase Equilib., 1993, 85, 41-54. [all data]

Bennett, A.; Lamm, S.; Orbey, H.; Sandler, S.I., Vapor-liquid equilibria of hydrocarbons and fuel oxygenates. 2, J. Chem. Eng. Data, 1993, 38, 263-9. [all data]

Wong, D.S.H.; Orbey, H.; Sandler, S.I., Equation of state mixing rule for nonideal mixtures using available activity coefficient model parameters and that allows extrapolation over large ranges of temperature and pressure, Ind. Eng. Chem. Res., 1992, 31, 2033-9. [all data]

Orbey, H.; Sandler, S.I., Relative measurements of activity coefficients at infinite dilution by gas chromatography, Ind. Eng. Chem. Res., 1991, 30, 2006-11. [all data]

Orbey, H.; Orbey, N., Evaluation of second virial coefficients from saturation data, Chem. Eng. Commun., 1989, 77, 219-28. [all data]

Orbey, H.; Vera, J.H., An augmented hard core equation of state generalized in terms of Tc Pc, and ω, Pure Appl. Chem., 1989, 61, 1413. [all data]

Kis, K.; Orbey, H., An empirical method for the second viral coefficients of non-standard fluids, Chem. Eng. J. (Lausanne), 1989, 41, 149. [all data]

Orbey, H., A Four Parameter Pitzer-Curl Type Correlation of Second Virial Coefficients, Chem. Eng. Commun., 1988, 65, 1-19. [all data]

Vera, J.H.; Orbey, H., Binary vapor-liquid equilibria of carbon dioxide with 2-methyl-1-pentene, 1 -hexene, 1-heptene, and m-xylene at 303.15, 323.15, and 343.15 k., J. Chem. Eng. Data, 1984, 29, 269. [all data]

Orbey, H.; Vera, J.H., Correlation for the third virial coefficient using t(c), p(c) and omega as parameters., AIChE J. 29, 1983, 107-13 1983. [all data]

Orbey, H.; Orbey, N., Evaluation of second virial coefficients from saturation data, Chem. Eng. Commun., 1989, 77, 219-28. [all data]