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38 matching references were found.
Wilson, L.C.; Wilding, W.V.; Wilson, G.M.; Rowley, R.L.; Felix, V.M.; Chilsom-Carter, T., Thermophysical Properties of HFC-125, Fluid Phase Equilib., 1992, 80, 167-177, https://doi.org/10.1016/0378-3812(92)87065-U . [all data]
Rowley, R.L.; Powell, R.H., Vapor-Liquid Equilibrium Measurements on Mixtures Important to Industrial Design in Experimental Results for DIPPR 1990-91 Projects on Phase Equilibria and Pure Component Properties, DIPPR Data Series No. 2, 1994. [all data]
Tolley, W.K.; Izatt, R.M.; Oscarson, J.L.; Rowley, R.L.; Giles, N.F., Comparison of the thermodynamics of mixing of titanium tetrachloride and tin tetrachloride with supercritical carbon dioxide, Sep. Sci. Technol., 1993, 28, 615-23. [all data]
Wilson, L.C.; Wilding, W.V.; Wilson, G.M.; Rowley, R.L.; Felix, V.M.; Chisolm-Carter, T., Thermophysical properties of HFC-125, Fluid Phase Equilib., 1992, 80, 167-77. [all data]
Giles, N.F.; Oscarson, J.L.; Rowley, R.L.; Tolley, W.K.; Izatt, R.M., Thermodynamic properties of mixing for tin tetrachloride dissolved in supercritical carbon dioxide: a combined experimental and molecular dynamics study, Fluid Phase Equilib., 1992, 73, 267-84. [all data]
Rowley, R.L.; Ely, J.F., Nonequilibrium molecular dynamics simulations of structured molecules. Part I. Isomeric effects on the viscosity of butanes, Mol. Phys., 1991, 72, 831-46. [all data]
Rowley, R.L.; Ely, J.F., Nonequilibrium molecular-dynamics simulations of n-butane and isobutane viscosity, Mol. Simul., 1991, 7, 5-6, 303-23. [all data]
Rowley, R.L.; Powell, R.H., Vapor-liquid equilibrium measurements on mixtures important to industrial design: phenol + dimethylether, phenol + propylamine, ethylformate + dimethylether, ethylbenzene + propylamine, methylamin in Experimental Results for Phase Equilibria and Pure Component Properties, DIPPR DATA Series No. 1, 1991. [all data]
Rowley, R.L.; Stoker. J.M.; Giles, N.F., Molecular-Dynamics Simulation of Mutual Diffusion in Nonideal Liquid Mixtures., Int. J. Thermophys., 1991, 12, 500. [all data]
Rowley, R.L.; Stoker. J.M.; Giles, N.F., Molecular-dynamics simulation of mutual diffusion in nonideal liquid mixtures, Int. J. Thermophys., 1991, 12, 501-13. [all data]
Okeson, K.J.; Rowley, R.L., A four-parameter corresponding-states method for prediction of newtonian, pure-component viscosity., Int. J. Thermophys., 1991, 12, 119. [all data]
Rowley, R.L.; Hoffman, G.L., Vapor-liquid equilibrium measurements on mixtures important to industrial design: triethylene glycol + n-hexane, triethylene glycol + cyclohexane, and furfural + isoprene, AICHE Symp. Ser., 1990, 86, 279, 6-19. [all data]
Rowley, R.L.; Oscarson, J.L.; Giles, N.F.; Tolley, W.K.; Izatt, R.M., Experimental and molecular-dynamics simulated excess enthalpies and solubilities of neopentane in supercritical carbon dioxide, Fluid Phase Equilib., 1990, 60, 143-56. [all data]
Battler, J.R.; Rowley, R.L., Excess enthalpy of four partially miscible binary liquid mixtures near their critical solution temperatures, J. Chem. Eng. Data, 1990, 35, 334-8. [all data]
Rowley, R.L.; Oscarson, J.L.; Slater, P.N.; Giles, N.F.; Izatt, R.M.; Tolley, W.K., Molecular-dynamics simulations of excess enthalpies in mixtures of supercritical carbon dioxide and neopentane, Fluid Phase Equilib., 1989, 53, 167. [all data]
Johnson, J.K.; Rowley, R.L., Application of an extended Lee-Kesler corresponding-states techniqu to prediction of vapor-liquid equilibria in multicomponent mixtures containing polar components, Int. J. Thermophys., 1989, 10, 479. [all data]
Rowley, R.L.; White, G.L.; Chiu, M., Ternary Liquid Mixture Thermal Conductivities, Chem. Eng. Sci., 1988, 43, 361. [all data]
Rowley, R.L.; Yi, S.-C.; Gubler, D.V.; Stoker. J.M., Mutual Diffusivity, Thermal Conductivity, and Heat of Transport in Binary Liquid Mixtures of Alkanes in Chloroform, J. Chem. Eng. Data, 1988, 33, 362. [all data]
Rowley, R.L.; Gubler, V., Thermal Conductivities in Seven Ternary Liquid Mixtures at 40 deg C and 1 Atm, J. Chem. Eng. Data, 1988, 33, 5. [all data]
Christensen, J.J.; Rowley, R.L.; Izatt, R.M., Handbook of Heats of Mixing, 1988. [all data]
Wilding, W.V.; Johnson, J.K.; Rowley, R.L., Thermodynamic Properties and Vapor Pressures of Polar Fluids from A Four-Parameter Corresponding States Method, Int. J. Thermophys., 1987, 8, 717. [all data]
Rowley, R.L.; Li, S.C.; Gubler, V.; Stoker. J.M., Mutual Diffusivity, Thermal Conductivity, and Heat of Transport in Binary Liquid Mixtures of Alkanes in Carbon Tetrachloride, Fluid Phase Equilib., 1987, 36, 219-233. [all data]
Rowley, R.L.; White, G.L., Thermal conductivities of ternary liquid mixtures, J. Chem. Eng. Data, 1987, 32, 63. [all data]
Rowley, R.L.; Yi, S.-C.; Gubler, V.; Stoker. J.M., Mutual Diffusivity, Thermal COnductivity, and Heat of Transport in Binary Liquid Mixtures of Alkanes in Carbon Tetrachloride, Fluid Phase Equilib., 1987, 36, 219. [all data]
Wilding, W.V.; Rowley, R.L., A Four-Parameter Corresponding States Method for the Prediction of Thermodynamic Properties of Polar and Nonpolar Fluids, Int. J. Thermophys., 1986, 7, 525. [all data]
Rowley, R.L.; Hall, M.D., Heats of Transport from the Diffusion Thermoeffect in Binary Liquid Mixtures of Toluene, Chlorobenzene, and Bromobenzene, J. Chem. Phys., 1986, 85, 3550. [all data]
Clark, W.M.; Rowley, R.L., The Mutual Diffusion Coefficient of Methanol-n-Hexane Near the Consolute Point., AIChE J., 1986, 32, 1125. [all data]
Battler, J.R.; Rowley, R.L., Prediction of Ternary Liquid-Liquid Equilibria from Excess Enthalpies, Fluid Phase Equilib., 1986, 25, 129. [all data]
Wei, I.C.; Rowley, R.L., A Local composition model for multicomponent liquid mixture shear viscosity, Chem. Eng. Sci., 1985, 40, 401. [all data]
Clark, W.M.; Rowley, R.L., Ternary Liquid Diffusion Coefficients Near Plait Points, Int. J. Thermophys., 1985, 1985, 631-642. [all data]
Battler, J.R.; Clark, W.M.; Rowley, R.L., Excess enthalpy and liquid-liquid equilibrium surfaces for the cyclohexane-2-propanol-water system from 293.15 to 323.15 K, J. Chem. Eng. Data, 1985, 30, 254. [all data]
Battler, J.R.; Rowley, R.L., Excess enthalpies between 293 and 323 K for constituent binaries of ternary mixtures exhibiting partial miscibility, J. Chem. Thermodyn., 1985, 17, 719-32. [all data]
Wei, I.C.; Rowley, R.L., Binary liquid mixture viscosities and densities, J. Chem. Eng. Data, 1984, 29, 332. [all data]
Wei, I.C.; Rowley, R.L., Ternary liquid mixture viscosities and densities., J. Chem. Eng. Data, 1984, 29, 336. [all data]
Wel, I.; Rowley, R.L., Ternary Liquid Mixture Viscosities and Densities, J. Chem. Eng. Data, 1984, 29, 336-340. [all data]
Rowley, R.L., Measurement and Prediction of Liquid Mixture Thermal Conductivity and Viscosity, U. S. Dept. Energy Rep. DOE/ER/13008--9 1984, 1984. [all data]
Peterson, E.R.; Vongvanich, T.; Rowley, R.L., Thermal diffusion factors near the azeotrope conditions of ethanol-water mixtures, J. Chem. Eng. Data, 1984, 29, 6. [all data]
Rowley, R.L.; Horne, F.H., The Dufor effect. III. Direct Experimental Determination of the Heat of Transport of Carbon Tetrachloride-Cyclohexane Liquid Mixtures, J. Chem. Phys., 1980, 72, 131-139. [all data]