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18 matching references were found.

Hwang, C.-A.; Holste, J.C.; Hall, K.R.; Gammon, B.E.; Marsh, K.N.; Parrish, W.R., PVT Properties and Bubble Point Pressures for Compositionally Characterized Commercial Grade Butane, 2-Methylpropane, and Natural Gasoline, J. Chem. Eng. Data, 1996, 41, 1517-1521. [all data]

Pinnick, H.R.; Falling, C.L.; Allred, G.C.; Parrish, W.R., Densities of Mixtures of Heptane + Methyl 1,1-Dimethylethyl Ether at Temperatures between 243.16 and 333.14 K, J. Chem. Eng. Data, 1995, 40, 950-2. [all data]

Allred, G.C.; Beets, J.W.; Parrish, W.R., Excess Properties for 1-Butanethiol + Heptane, + Cyclohexane, + Benzene, and + Toluene. 2. Excess Molar Enthalpies at 283.15, 298.15, and 333.15 K, J. Chem. Eng. Data, 1995, 40, 1062-6. [all data]

Jangkamolkulchai, A.; Allred, G.C.; Parrish, W.R., Densities and excess molar volumes of methyl tert-butyl ether and ethyl tert-butyl ether with hydrocarbons from 255.4 to 333.2 K, J. Chem. Eng. Data, 1991, 36, 481-4. [all data]

Heiser, R.F.; Parrish, W.R., Using rational functions to fit experimental data in Proc. Thermodyn. Fluids: Meas. Correl. Summer Sch. Exp. Methods Thermodyn. Fluids, Meet dt. 1988, World Sci.: Singapore, 337-51, 1990. [all data]

Allred, G.C.; Beets, J.W.; Parrish, W.R., Excess Properties for 1-Butanethiol + n-Heptane, Cyclohexane, Benzene, and Toluene. 1. Excess Molar Volumes at 283.15 and 298.15 K, J. Chem. Eng. Data, 1990, 35, 328. [all data]

Heiser, R.F.; Parrish, W.R., Representing Physical Data With Rational Functions, Ind. Eng. Chem. Res., 1989, 28, 484-9. [all data]

Parrish, W.R., Compressed Liquid Propene Densities between 5 and 73 deg C at Pressures to 9.6 MPa, J. Chem. Eng. Data, 1987, 32, 311-313. [all data]

Parrish, W.R., Compressed liquid densities of propane-normal butane mixtures betwee 10 and 60.degree.C at pressures up to 9.6 MPa, Fluid Phase Equilib., 1986, 25, 65. [all data]

Parrish, W.R., Compressed liquid densities of propane-normal butane mixtures between 50F and 140F at pressures up to 1400 psia in Proc., Annu. Conv. - Gas Process. Assoc. 64, 1985. [all data]

Parrish, W.R., Calculation of compressed liquid ethane-propane mixture densities fo custody transfer at pressures up to 14 MPa, Fluid Phase Equilib., 1985, 23, 193. [all data]

Parrish, W.R., Compressed liquid densities of ethane-propane mixtures between 10 an 49.degree.C at pressures up to 9.6 MPa, Fluid Phase Equilib., 1984, 18, 279-97. [all data]

Parrish, W.R.; Sitton, D.M., Vapor-liquid equilibrium data for the propane +, n-butane +, isobutane +, and propylene + isopropyl fluoride systems at 30 and 50 c., J. Chem. Eng. Data, 1982, 27, 303-6. [all data]

Hiza, M.J.; Haynes, W.M.; Parrish, W.R., Orthobaric liquid densities and excess volumes for binary mixtures of low molar-mass alkanes and nitrogen between 105 and 140 k, J. Chem. Thermodyn., 1977, 9, 873-96. [all data]

Parrish, W.R.; Hiza, M.J., On the consistency of liquid-vapor equilibria data for binary mixtures of methane with the light paraffin hydrocarbons, Adv. Cryog. Eng., 1976, 21, 485. [all data]

Parrish, W.R.; Steward, W.G., Vapor-liquid equilibria data for helium + carbon monoxide and helium + nitrous oxide systems, J. Chem. Eng. Data, 1975, 20, 412-6. [all data]

Kidnay, A.J.; Miller, R.C.; Parrish, W.R.; Hiza, M.J., Liquid-vapour phase equilibria in the nitrogen + methane system from 130 to 180 k, Cryogenics, 1975, 15, 531-40. [all data]

Parrish, W.R.; Hiza, M.J., Liquid-vapor equilibria in the nitrogen + methane system between 95 and 120 k., Adv. Cryog. Eng., 1974, 19, 300-8. [all data]