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Author:Sandler, S.I.

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93 matching references were found.

Sandler, S.I., Infinite dilution activity coefficients in chemical, environmental and biochemical engineering, Fluid Phase Equilib., 1996, 116, 343-53. [all data]

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]

Tavares, F.W.; Chang, J.; Sandler, S.I., Equation of state for the square-well chain fluid based on the dimer version of Wertheim's perturbation theory, Mol. Phys., 1995, 86, 1451-71. [all data]

Steinhagen, V.; Sandler, S.I., Liquid-vapor equilibrium. tert-Butyl ethyl ether - 2-methylbutane system, Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1995, 23, 36-41. [all data]

Semar, S.; Sandler, S.I.; Antosik, M., Total Pressure Measurements of Binary Mixtures Containing tert-Amyl Methyl Ether and tert-Amyl Alcohol, J. Chem. Eng. Data, 1995, 40, 712-18. [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]

Haines, R.I.S.; Sandler, S.I., Aqueous Solubilities and Infinite Dilution Activity Coefficients of Several Polycyclic Aromatic Hydrocarbons, J. Chem.Eng. Data, 1995, 40, 833-6. [all data]

Hellinger, S.; Sandler, S.I., Liquid-Liquid Equilibria of Fuel Oxygenate + Water + Hydrocarbon Mixtures. 2, J. Chem. Eng. Data, 1995, 40, 321-5. [all data]

Fu, Y.-H.; Sandler, S.I., A Simplified SAFT Equation of State for Associating Compounds and Mixtures, Ind. Eng. Chem. Res., 1995, 34, 1897-909. [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]

Chang, J.; Sandler, S.I., The Wertheim integral equation theory with the ideal chain approximation and a dimer equation of state: generalization to mixtures of hard-sphere chain fluids, J. Chem. Phys., 1995, 103, 3196-212. [all data]

Bhatia, S.R.; Sandler, S.I., Temperature Dependence of Infinite Dilution Activity Coefficients in Octanol and Octanol/Water Partition Coefficients of Some Volatile Halogenated Organic Compounds, J. Chem. Eng. Data, 1995, 40, 1196-8. [all data]

Antosik, M.; Sandler, S.I., Liquid-vapor equilibrium. 1,1-Dimethylpropyl methyl ether - 2,2,4- trimethylpentane system, Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1995, 23, 42-50. [all data]

Tse, G.; Sandler, S.I., Determination of Infinite Dilution Activity Coefficients and 1-Octanol/ Water Partition Coefficients of Volatile Organic Pollutants, J. Chem. Eng. Data, 1994, 39, 354-7. [all data]

Steinhagen, V.; Sandler, S.I., Vapor-Liquid Equilibria of Binary Mixtures with Ethyl tert-Butyl Ether, J. Chem. Eng. Data, 1994, 39, 588-90. [all data]

Sandler, S.I., Thermophysical properties: what have we learned recently, and what do we still need to know?, Int. J. Thermophys., 1994, 15, 1013-35. [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]

Hartounian, H.; Koetitz, J.A.; Kaler, E.W.; Sandler, S.I., A continuous dilution method for phase diagram determination, AIChE J., 1994, 40, 1574-9. [all data]

Antosik, M.; Sandler, S.I., Vapor-Liquid Equilibria of Hydrocarbons and tert-Amyl Methyl Ether, J. Chem. Eng. Data, 1994, 39, 584-7. [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]

Huang, H.; Sandler, S.I., Prediction of vapor-liquid equilibria at high pressures using activity coefficient parameters obtained from low-pressure data: a comparison of two equation of state mixing rules, Ind. Eng. Chem. Res., 1993, 32, 1498-503. [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]

Wong, D.S.H.; Sandler, S.I., A theoretically correct mixing rule for cubic equations of state, AIChE J., 1992, 38, 671-80. [all data]

Wright, D.A.; Sandler, S.I.; DeVoll, D., Environ. Sci. Technol., 1992, 26, 1828. [all data]

Wu, H.S.; Hagewiesche, D.; Sandler, S.I., Liquid-vapor equilibrium. N,N-dimethylmethanamide - 2-propanol system, Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1992, No. 1, 4-6. [all data]

Pividal, K.A.; Birtigh, A.; Sandler, S.I., Infinite dilution activity coefficients for oxygenate systems determined using a differential static cell, J. Chem. Eng. Data, 1992, 37, 484-7. [all data]

Wu, H.S.; Locke, W.E.; Sandler, S.I., Isothermal Vapor-Liquid Equil. of Binary Mixtures Containing Morpholine morpholine, J. Chem. Eng. Data, 1991, 36, 127. [all data]

Wu, H.S.; Pividal, K.A.; Sandler, S.I., Vapor-liquid equilibria of hydrocarbons and fuel oxygenates, J. Chem. Eng. Data, 1991, 36, 418-21. [all data]

Wu, H.S.; Plvldal, K.A.; Sandler, S.I., Vapor-liquid equilibria of hydrocarbons and fuel oxygenates., J. Chem. Eng. Data, 1991, 36, 418. [all data]

Sowers, G.M.; Sandler, S.I., Equations of state from generalized perturbation theory. Part 1. The hard- core Lennard-Jones fluid, Fluid Phase Equilib., 1991, 63, 1-25. [all data]

Sowers, G.M.; Sandler, S.I., Equations of state from generalized perturbation theory. Part II. Lennard- Jones fluid, Fluid Phase Equilib., 1991, 67, 127-50. [all data]

Shealy, G.S.; Bauer, T.J.; Hauschild, T.; Sandler, S.I.; Kassmann, K.D.; Knapp, H., Liquid vapor equilibrium. N,N-Dimethylmethanamide-ethyl ethanoate systemm, Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1991, No. 1, 65. [all data]

Shealy, G.S.; Bauer, T.J.; Hauschild, T.; Sandler, S.I.; Kassmann, K.D.; Knapp, H., Liquid vapor equilibrium. N,N-Dimethylmethanamide-ethyl ethanoate system, Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1991, No. 1, 66. [all data]

Shealy, G.S.; Bauer, T.J.; Hauschild, T.; Sandler, S.I.; Kassmann, K.D.; Knapp, H., Liquid vapor equilibrium. N,N-Dimethylmethanamide-2-methylpropanal system, Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1991, No. 1, 68. [all data]

Shealy, G.S.; Bauer, T.J.; Hauschild, T.; Sandler, S.I.; Kassmann, K.D.; Knapp, H., Liquid vapor equilibrium. N,N-Dimethylmethanamide-2-methylpropanal system, Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1991, No. 1, 69. [all data]

Shealy, G.S.; Bauer, T.J.; Hauschild, T.; Sandler, S.I.; Kassmann, K.D.; Knapp, H., Ethyl ethanoate - 2-methylpropanal system, Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1991, No. 1, 71. [all data]

Shealy, G.S.; Bauer, T.J.; Hauschild, T.; Sandler, S.I.; Kassmann, K.D.; Knapp, H., Ethyl ethanoate - 2-methylpropanal system, Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1991, No. 1, 72. [all data]

Shealy, G.S.; Bauer, T.J.; Hauschild, T.; Sandler, S.I.; Kassmann, K.D.; Knapp, H., Excess free energy. N,N-Dimethylmethanamide-2-methylpropanal system, Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1991, No. 1, 70. [all data]

Shealy, G.S.; Bauer, T.J.; Hauschild, T.; Sandler, S.I.; Kassmann, K.D.; Knapp, H., Excess free energy. Ethyl ethanoate-2-methylpropanal system, Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1991, No. 1, 73. [all data]

Shealy, G.S.; Buaer, T.J.; Hauschild, T.; Sandler, S.I.; Kassmann, K.D.; Knapp, H., Excess free energy. N,N-Dimethylmethanamide-ethyl ethanoate system, Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1991, No. 1, 67. [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]

Marathe, P.; Sandler, S.I., High-pressure vapor-liquid equilibrium of some binary mixtures of cyclopentane, argon, nitrogen, N-butane, and neopentane, J. Chem. Eng. Data, 1991, 36, 192. [all data]

Dodd, L.R.; Sandler, S.I., A study of the Buckingham exponential-six fluid mixtures, Fluid Phase Equilib., 1991, 63, 279-315. [all data]

Dodd, L.R.; Sandler, S.I., Practical equation of state and activity coefficient models based on the exp-6 fluid, Fluid Phase Equilib., 1991, 69, 99-139. [all data]

Wu, H.S.; Locke, W.E.; Sandler, S.I., Liquid-vapor equilibrium. Pyrrolidine-cyclohexane system, Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1990, No. 2, 111. [all data]

Wu, H.S.; Locke, W.E.; Sandler, S.I., Liquid-vapor equilibrium. Pyrrolidine-cyclohexane system, Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1990, No. 2, 112. [all data]

Wu, H.S.; Locke, W.E.; Sandler, S.I., Liquid-vapor equilibrium. Pyrrolidine-oxolane system, Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1990, No. 2, 114. [all data]

Wu, H.S.; Locke, W.E.; Sandler, S.I., Liquid-vapor equilibrium. Pyrrolidine-oxolane system, Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1990, No. 2, 115. [all data]

Wu, H.S.; Locke, W.E.; Sandler, S.I., Liquid-vapor equilibrium. Pyrrolidine-ethanol system, Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1990, No. 2, 117. [all data]

Wu, H.S.; Locke, W.E.; Sandler, S.I., Liquid-vapor equilibrium. Pyrrolidine-ethanol system, Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1990, No. 2, 118. [all data]

Wu, H.S.; Locke, W.E.; Sandler, S.I., Excess Gibbs energy. Pyrrolidine-cyclohexane system, Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1990, No. 2, 113. [all data]

Wu, H.S.; Locke, W.E.; Sandler, S.I., Excess Gibbs energy. Pyrrolidine-oxolane system, Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1990, No. 2, 116. [all data]

Wu, H.S.; Locke, W.E.; Sandler, S.I., Excess Gibbs energy. Pyrrolidine-ethanol system, Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1990, No. 2, 119. [all data]

Wu, H.S.; Locke, W.E.; Sandler, S.I., Liquid-vapor equilibrium. Morpholine-octane system, Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1990, No. 3, 207. [all data]

Wu, H.S.; Locke, W.E.; Sandler, S.I., Liquid-vapor equilibrium. Morpholine-octane system, Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1990, No. 3, 208. [all data]

Wu, H.S.; Locke, W.E.; Sandler, S.I., Liquid-vapor equilibrium. Morpholine-cyclooctane system, Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1990, No. 3, 210. [all data]

Wu, H.S.; Locke, W.E.; Sandler, S.I., Liquid-vapor equilibrium. Morpholine-cyclooctane system, Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1990, No. 3, 211. [all data]

Wu, H.S.; Locke, W.E.; Sandler, S.I., Liquid-vapor equilibrium. Morpholine - 1-butanol system, Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1990, No. 3, 213. [all data]

Wu, H.S.; Locke, W.E.; Sandler, S.I., Liquid-vapor equilibrium. Morpholine - 1-butanol system, Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1990, No. 3, 214. [all data]

Wu, H.S.; Locke, W.E.; Sandler, S.I., Excess Gibbs energy. Morpholine-octane system, Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1990, No. 3, 209. [all data]

Wu, H.S.; Locke, W.E.; Sandler, S.I., Excess Gibbs energy. Morpholine-cyclooctane system, Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1990, No. 3, 212. [all data]

Wu, H.S.; Locke, W.E.; Sandler, S.I., Excess Gibbs energy. Morpholine - 1-butanol system, Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1990, No. 3, 215. [all data]

Wu, H.S.; Locke, W.E.; Sandler, S.I., Isothermal Vapor-Liquid Equilibrium of Binary Mixt. Containing Pyrrolidine, J. Chem. Eng. Data, 1990, 35, 169. [all data]

Sandler, S.I.; Shibata, S.K., The measurement and correlation of high pressure phase equilibria composition and density data in Proc. Thermodyn. Fluids: Meas. Correl. Summer Sch. Exp. Methods Thermodyn. Fluids, Meet dt. 1988, World Sci.: Singapore, 3-22, 1990. [all data]

Pividal, K.A.; Sandler, S.I., Neighbor effects on the group contribution method: infinite dilution activity coefficients of binary systems containing primary amines and alcohols, J. Chem. Eng. Data, 1990, 35, 53. [all data]

Wu, H.S.; Sandler, S.I., Vapor-Liquid Equilibrium of 1,3-dioxolane Systems, J. Chem. Eng. Data, 1989, 34, 209. [all data]

Shibata, S.K.; Sandler, S.I., High-Pressure Vapor-Liquid Equilibria of Mixtures of Nitrogen, Carbon Dioxide, and Cyclohexane, J. Chem. Eng. Data, 1989, 34, 419. [all data]

Shibata, S.K.; Sandler, S.I., High-pressure vapor-liquid equilibria involving mixtures of nitrogen, carbon dioxide, and n-butane, J. Chem. Eng. Data, 1989, 34, 291. [all data]

Shibata, S.K.; Sandler, S.I., Critical evaluation of equation of state mixing rules for the prediction of high-pressure phase equilibria, Ind. Eng. Chem. Res., 1989, 28, 1893. [all data]

Sandler, S.I.; Fischer, J.; Reschke, F., Free energies of mixing, Fluid Phase Equilib., 1989, 45, 251. [all data]

Malewski, M.K.F.; Sandler, S.I., High-Pressure Vapor-Liquid Equilibria of the Binary Mixtures Nitrogen + n-Butane and Argon + n-Butane, J. Chem. Eng. Data, 1989, 34, 424. [all data]

Wu, H.S.; Hagewiesche, D.; Sandler, S.I., Vapor-liquid equilibria of 2-propanol + water + N,N-dimethyl formamide, Fluid Phase Equilib., 1988, 43, 77. [all data]

Wu, H.S.; Sandler, S.I., Vapor-Liquid Equilibria of Tetrahydrofuran Systems, J. Chem. Eng. Data, 1988, 33, 157. [all data]

Wu, H.S.; Sandler, S.I., Vapor-Liquid Equilibria for Binary Mistures of Butyl Ether with 2-Furaldehyde and with 2-, 3-, and 4-Heptanone, J. Chem. Eng. Data, 1988, 33, 316. [all data]

Shealy, G.S.; Sandler, S.I., The excess Gibbs free energy of aqueous nonelectrolyte solutions, AIChE J., 1988, 34, 1065. [all data]

Pividal, K.A.; Sandler, S.I., Ebulliometric method for measuring activity coefficients at infinite dilution: systems with cyclic ethers, J. Chem. Eng. Data, 1988, 33, 438. [all data]

Xu, Z.; Sandler, S.I., Temperature-dependent parameters and the Peng-Robinson equation of state, Ind. Eng. Chem. Res., 1987, 26, 601. [all data]

Shealy, G.S.; Hagewiesche, D.; Sandler, S.I., Vapor-liquid equilibrium of ethanol/water/N,N-dimethylformamide, J. Chem. Eng. Data, 1987, 32, 366. [all data]

Lee, K.H.; Sandler, S.I., The generalized van der Waals partition function. IV. Local composition models for mixtures of unequal size molecules, Fluid Phase Equilib., 1987, 34, 113. [all data]

Hauschild, T.; Wu, H.S.; Sandler, S.I., Vapor-Liquid Equilibrium of the Mixtures 2-Furaldehyde/1-Butanol and 2-Furaldehyde/4-methyl-2-pentanone, J. Chem. Eng. Data, 1987, 32, 226. [all data]

Sandler, S.I.; Lee, K.H.; Kim, H., The generalized van der Waals partition function as a basis for equations of state: mixing rules and activity coefficient models, ACS Symp. Ser., 1986, 300, 180. [all data]

Shealy, G.S.; Bauer, T.J.; Hauschild, T.; Sandler, S.I.; Kassmann, K.D.; Knapp, H., J. Chem. Eng. Data, 1986, 31, 457. [all data]

Kim, C.H.; Vimalchand, P.; Donohue, M.D.; Sandler, S.I., Local composition model for chainlike molecules: a new simplified version of the perturbed hard chain theory, AIChE J., 1986, 32, 1726-34. [all data]

Eckert, C.J.; Sandler, S.I., Vapor-liquid equilibria for the carbon dioxide-cyclopentane system a 37.7, 45.0, and 60.0.degree.C, J. Chem. Eng. Data, 1986, 31, 26. [all data]

Shealy, G.S.; Sandler, S.I., Vapor-Liquid Equilibrium for Four Mixtures Containing N,N-Dimethylformamide, J. Chem. Eng. Data, 1985, 30, 455. [all data]

Shealy, G.S.; Sandler, S.I., Vapor-liquid equilibria of {xCH3CH(CH3)CHO+(1-x)C7H16}(l) and {xCH3CO2C2H5+(1-x)C7H16}(l), J. Chem. Thermodyn., 1985, 17, 143. [all data]

Patel, N.C.; Sandler, S.I., Excess Volumes of the Water/Methanol, n-Heptane/Ethyl Acetate,n-Heptane/n-Butyraldehyde, and n-Heptane/Isobutyraldehyde Systems, J. Chem. Eng. Data, 1985, 30, 218. [all data]

Lee, K.H.; Lombardero, M.; Sandler, S.I., The generalized van der Waals partition function. II. Application to the square-well fluid, Fluid Phase Equilib., 1985, 21, 177. [all data]

Eng, R.; Sandler, S.I., Vapor-liquid equilibria for three aldehyde/hydrocarbon mixtures, J. Chem. Eng. Data, 1984, 29, 156. [all data]

Behrens, P.K.; Sandler, S.I., Vapor-Liquid Equilibria for the Carbon Dioxide-1-Butene System at 37.7 and 45.0 C, J. Chem. Eng. Data, 1983, 28, 52-56. [all data]