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24 matching references were found.

Coutsikos, P.; Magoulas, K.; Tassios, D., Solubilities of Phenols in Supercritical Carbon Dioxide, J. Chem. Eng. Data, 1995, 40, 953-8. [all data]

Voulgaris, M.; Stamatakis, S.; Magoulas, K.; Tassios, D., Prediction of physical properties for nonpolar compounds, petroleum and coal liquid fractions, Fluid Phase Equilib., 1991, 64, 73-106. [all data]

Magoulas, K.; Tassios, D., Thermophysical properties of n-alkanes from C1 to C20 and their prediction for higher ones, Fluid Phase Equilib., 1990, 56, 119-40. [all data]

Czerwienski, G.J.; Tomasula, P.; Tassios, D., Vapor-liquid equilibria with the vdW - 711 equation of state, Fluid Phase Equilib., 1988, 42, 63. [all data]

Watson, P.; Cascella, M.; May, D.; Salerno, S.; Tassios, D., Prediction of vapor pressures and saturated molar volumes with a simple cubic equation of state: Part II: The van der Waals - 711 EOS, Fluid Phase Equilib., 1986, 27, 35. [all data]

Salerno, S.; Cascella, M.; May, D.; Watson, P.; Tassios, D., Prediction of vapor pressures and saturated volumes with a simple cubic equation of state: Part I: A reliable data base, Fluid Phase Equilib., 1986, 27, 15. [all data]

Yee, D.; Simonetty, J.; Tassios, D., Prediction of vapor-liquid equilibrium from ternary liquid- liquid equilibrium data., Ind. Eng. Chem. Process Des. Dev., 1983, 22, 123. [all data]

Bixon, E.; Guerry, R.; Tassios, D., Salt effect on the vapor pressure of pure solvents: methanol with seven salts at 24.9 c, J. Chem. Eng. Data, 1979, 24, 9. [all data]

Tassios, D., A single parameter equation for isothermal vapor-liquid equilibrium constants, AIChE J., 1971, 17, 1367-71. [all data]

Lindberg, G.W.; Tassios, D., Effect of organic and inorganic salts on relative volatility of nonaqueous systems, J. Chem. Eng. Data, 1971, 16, 52-55. [all data]

Tassios, D.; Van Winkle, M., Prediction of Binary Vapor-Liquid Equilibria, J. Chem. Eng. Data, 1967, 12, 555. [all data]

Voutsas, E.C.; Boukouvalas, C.J.; Kalospiros, N.S.; Tassios, D.P., The performance of EoS/GE models in the prediction of vapor-liquid equilibria in asymmetric systems, Fluid Phase Equilib., 1996, 116, 480-7. [all data]

Voutsas, E.C.; Tassios, D.P., Prediction of Infinite Dilution Activity Coefficients in Binary Mixtures with UNIFAC. A Critical Evaluation, Ind. Eng. Chem. Res., 1996, 35, 1438-45. [all data]

Coutsikos, P.; Kalospiros, N.S.; Tassios, D.P., Capabilities and limitations of the Wong-Sandler mixing rules, Fluid Phase Equilib., 1995, 108, 59-78. [all data]

Kalospiros, N.S.; Misseyannis, G.M.; Androulakis, I.P.; Tassios, D.P., Application of the VdW-711 equation of state to polar mixtures. Correlation of binary and prediction of multicomponent vapor-liquid equilibria, Fluid Phase Equilib., 1991, 64, 173-84. [all data]

Harismiadis, V.I.; Koutras, N.K.; Tassios, D.P.; Panagiotopoulos, A.Z., Gibbs ensemble simulations of binary Lennard-Jones mixtures. How good is conformal solutions theory for phase equilibrium predictions?, Fluid Phase Equilib., 1991, 65, 1-17. [all data]

Androulakis, I.P.; Kalospiros, N.S.; Tassios, D.P., Thermophysical properties of pure polar and nonpolar compounds with a modified VdW-711 equation of state, Fluid Phase Equilib., 1989, 45, 135. [all data]

Spelyng, W.A.; Tassios, D.P., Solvent selectivity for hydrocarbons with close molar volumes, Ind. Eng. Chem. Process Des. Dev., 1974, 13, 328-32. [all data]

Marina, J.M.; Tassios, D.P., Effective local compositions in phase equilibrium correlations., Ind. Eng. Chem. Process Des. Dev., 1973, 12, 67. [all data]

Marina, J.M.; Tassios, D.P., Prediction of ternary liquid-liquid equilibrium from binary data, Ind. Eng. Chem. Process Des. Dev., 1973, 12, 271. [all data]

Bogeatzes, A.S.; Tassios, D.P., Prediction of gas-liquid equilibrium through gas-liquid chromatography, Ind. Eng. Chem. Process Des. Dev., 1973, 12, 274. [all data]

Tassios, D.P., Infinite dilution relative volatilities through gas-liquid chromatography, Ind. Eng. Chem. Process Des. Dev., 1972, 11, 1, 43-6. [all data]

Skamenca, D.G.; Tassios, D.P., An improved redlich-kwong equation of state in the supercritical region, Ind. Eng. Chem. Process Des. Dev., 1971, 10, 59. [all data]

Tassios, D.P., Prediction of binary vapor-liquid equilibria: Members of a homologus series and a common solvent., Ph.D. Thesis, Univ. Tex., Austin, TX, 1967. [all data]