Search Results

Search criteria:

Author:Robinson, R.L.

You may also wish to search for items by Robinson, R. and Robinson.

45 matching references were found.

Robinson, R.L.; Edmister, W.C.; Dullien, F.A.L., Diffusion Coefficients for Four Homomorphic Binary Liquid Systems, Ind. Eng. Chem. Fundam., 1966, 5, 74-9. [all data]

Srivatsan, S.; Gao, W.; Gasem, K.A.M.; Robinson, R.L., Solubility of Methane in Toluene at Temperatures from 313 to 423 K at Pressures to 8.9 MPa, J. Chem. Eng. Data, 1998, 43, 623-5. [all data]

Park, J.; Robinson, R.L.; Gasem, K.A.M., Solubilities of Hydrogen in Aromatic Hydrocarbons from 323 to 433 K and Pressures to 21.7 MPa, J. Chem. Eng. Data, 1996, 41, 70-3. [all data]

Srivatsan, S.; Yi, X.; Robinson, R.L.; Gasem, K.A.M., Solubilities of Carbon Monoxide in Heavy Normal Paraffins at Temperatures from 311 to 423 K and Pressures to 10.2 MPa, J. Chem. Eng. Data, 1995, 40, 237-40. [all data]

Shaver, R.D.; Robinson, R.L.; Gasem, K.A.M., Modified SPHCT equation of state for improved predictions of equilibrium and volumetric properties of pure fluids, Fluid Phase Equilib., 1995, 112, 223-48. [all data]

Park, J.; Robinson, R.L.; Gasem, K.A.M., Solubilities of Hydrogen in Heavy Normal Paraffins at Temperatures from 323 .2 to 423.2 K and Pressures to 17.4 MPa, J. Chem. Eng. Data, 1995, 40, 241-4. [all data]

Park, J.; Yi, X.; Gasem, K.A.M.; Robinson, R.L., Solubilities of Carbon Monoxide in Aromatic Hydrocarbons at Temperatures from 323 to 433 K and Pressures to 23.3 MPa, J. Chem. Eng. Data, 1995, 40, 245-7. [all data]

Darwish, N.A.; Gasem, K.A.M.; Robinson, R.L., Solubility of Methane in Benzene, Naphthalene, Phenanthrene, and Pyrene at Temperatures from 323 to 433 K and Pressures to 11.3 MPa, J. Chem. Eng. Data, 1994, 39, 781-4. [all data]

Srivastan, S.; Darwish, N.A.; Gasem, K.A.M.; Robinson, R.L., Solubility of methane in hexane, decane, and dodecane at temperatures from 311 to 423 K and pressures to 10.4 MPa, J. Chem. Eng. Data, 1992, 37, 516-20. [all data]

Shaver, R.; Robinson, R.L.; Gasem, K.A.M., A framework for the prediction of saturation properties: vapor pressuress, Fluid Phase Equilib., 1991, 64, 141-63. [all data]

Nagarajan, N.; Gasem, K.A.M.; Robinson, R.L., Equilibrium Phase Compoistions, Phase Densities, and Interfacial Tensions for CO2 + Hydrocarbon Systems. 6. CO2 + n-Butane + n-Decane, J. Chem. Eng. Data, 1990, 35, 228. [all data]

Robinson, R.L.; Jacoby, R.H., Better Compressibility Factors, Hydrocarbon Process. Pet. Refin., 1965, 44, 4, 141-5. [all data]

Edmister, W.C.; Robinson, R.L., Thermodynamic consistency tests for vapor-liquid equilibria data, Chem. Eng. Prog., Symp. Ser., 1963, 59, 11. [all data]

Gasem, K.A.M.; Bufkin, B.A.; Raff, A.M.; Robinson, R.L., Solubilities of Ethane in Heavy Normal Paraffins at Pressures to 7.8 MPa and Temperatures from 348 to 423 K, J. Chem. Eng. Data, 1989, 34, 187. [all data]

Gasem, K.A.M.; Dickson, K.B.; Dulcamara. P.B.; Nagarajan, N.; Robinson, R.L., Equilibrium Phase Compositions, Phase Densities, and Interfacial Tensions for CO2 + Hydrocarbon Systems 5. CO2 + n-Tetradecane, J. Chem. Eng. Data, 1989, 34, 191. [all data]

Gasem, K.A.M.; Raff, A.M.; Darwish, N.; Robinson, R.L., Solubility of Ethane in n-Hexane at Pressures to 5.4 MPa and Temperatures from 311 to 394 K, J. Chem. Eng. Data, 1989, 34, 397. [all data]

Nagarajan, N.; Robinson, R.L., Equilibrium Phase Composition, Phase Densities, and Interfacial Tensions for CO2 + Hydrocarbon Systems 3. CO2 + Cyclohexane. 4. CO2 + Benzene, J. Chem. Eng. Data, 1987, 32, 369. [all data]

Nagarajan, N.; Robinson, R.L., Equil. Phase Comp., Phase Dernsities, and Interfacial Tensionss for CO2 + Hydrocarbon Systems 2. CO2 + n-Decane, J. Chem. Eng. Data, 1986, 31, 168. [all data]

Bufkin, B.A.; Robinson, R.L.; Estrera, S.S.; Luks, K.D., Solubility of ethane in n-decane at pressures to 8.2 MPa and temperatures from 278 to 411 K, J. Chem. Eng. Data, 1986, 31, 421. [all data]

Anderson, J.M.; Barrick, M.W.; Robinson, R.L., Solubilities of Carbon Dioxide in Cyclohexane and trans-Decalin at Pressures to 10.7 MPa and Temperatures from 323 to 423 K, J. Chem. Eng. Data, 1986, 31, 172. [all data]

Hsu, J.; Nagarajan, N.; Robinson, R.L., Equilibrium Phase Compositions, Phase Densities and Interfacial Tensions for CO2 + Hydrocarbon Systems. 1. CO2 + n-Butane, J. Chem. Eng. Data, 1985, 30, 485. [all data]

Gasem, K.A.M.; Robinson, R.L., Solubilities of Carbon Dioxide in Heavy Normal Paraffins (C20-C44) at Pressures to 9.6 MPa and Temperatures from 323 to 423 K, J. Chem. Eng. Data, 1985, 30, 53-56. [all data]

Gupta, M.K.; Li, Y.-H.; Hulsey, B.J.; Robinson, R.L., Phase equilibrium for carbon dioxide + benzene at 313.2, 353.2, and 393.2 k., J. Chem. Eng. Data, 1982, 27, 55-7. [all data]

Li, Y.-H.; Dillard, K.H.; Robinson, R.L., Vapor-Liquid Phase Equilibrium for Carbon Dioxide-n-Hexane at 40, 80 and 120 deg C, J. Chem. Eng. Data, 1981, 26, 53-5. [all data]

Li, Y.-H.; Dillard, K.H.; Robinson, R.L., Vapor-liquid phase equilibrium in the methane + ethane + propane + toluene + 1-methylnaphthalene system at 220-400 f and 200-2000 psia, J. Chem. Eng. Data, 1981, 26, 200-204. [all data]

Dillard, D.D.; Waxman, M.; Robinson, R.L., Volumetric Data and Virial Coefficients for Helium, Krypton and Helium-Krypton Mixtures, J. Chem. Eng. Data, 1978, 23, 269-74. [all data]

Mundis, C.J.; Yarborough, L.; Robinson, R.L., Vaporization equilibrium ratios for co(2) and h(2)s in paraffinic, naphthenic and aromatic solvents, Ind. Eng. Chem. Process Des. Dev., 1977, 16, 254-9. [all data]

Hwang, S.-C.; Robinson, R.L., Vapor-Liquid Equilibria at 25 deg C for None Alcohol-Hydrocarbon Binary Systems, J. Chem. Eng. Data, 1977, 22, 319-25. [all data]

Robinson, R.L.; Hiza, M.J., Solid-vapor equilibrium - a survey, Adv. Cryog. Eng., 1975, 20, 218-238. [all data]

Kate, F.H.; Robinson, R.L., Vapor + solid equilibrium for helium + krypton, J. Chem. Thermodyn., 1973, 5, 259-71. [all data]

Kate, F.H.; Robinson, R.L., Vapor + solid equilibrium for helium + xenon, J. Chem. Thermodyn., 1973, 5, 273-81. [all data]

Yodovich, A.; Robinson, R.L.; Chao, K.-C., AIChE J., 1971, 17, 1152. [all data]

Yudovich, A.; Robinson, R.L.; Chao, K.-C., Phase equilibrium of carbon dioxide in the methane + carbon dioxide + n- decane system, AIChE J., 1971, 17, 1152-9. [all data]

Spear, R.R.; Robinson, R.L.; Chao, K.-C., Critical states of ternary mixtures and equations of state, Ind. Eng. Chem. Fundam., 1971, 10, 588-92. [all data]

Robinson, R.L.; Chao, K.-C., A correlation of vaporization equilibrium ratios for gas processing systems, Ind. Eng. Chem. Process Des. Dev., 1971, 10, 221. [all data]

Lin, H.-M.; Robinson, R.L., Test of combination rules for prediction of interaction second virial coefficients, J. Chem. Phys., 1971, 54, 52. [all data]

Smith, V.C.; Robinson, R.L., Vapor-Liquid Equilibria at 25 deg C in the Binary Mixtures Formed by Hexane, Benzene, and Ethanol, J. Chem. Eng. Data, 1970, 15, 391-5. [all data]

Lin, H.-M.; Robinson, R.L., Uncertainties in intermolecular pair potential parameters determined from macroscopic property data: I virial coefficients, J. Chem. Phys., 1970, 52, 3727-3731. [all data]

Kuo, C.-M.; Robinson, R.L.; Chao, K.-C., Quasilattice theory and paraffin - alcohol systems, Ind. Eng. Chem. Fundam., 1970, 9, 564-568. [all data]

Spear, R.R.; Robinson, R.L.; Chao, K.-C., Critical states of mixtures and equations of state, Ind. Eng. Chem. Fundam., 1969, 8, 2-8. [all data]

Yudovich, A.; Robinson, R.L.; Chao, K.-C., Mixture volumetric properties from infinite dilution studies: part I methane - carbon dioxide, Chem. Eng. Prog., Symp. Ser., 1968, 64, 85-91. [all data]

Kate, F.H.; Robinson, R.L.; Chao, K.C., Mixture volumetric properties from infinite dilution studies II methane - hydrogen sulfide, Chem. Eng. Prog., Symp. Ser., 1968, 64, 91-94. [all data]

Dillard, D.D.; Edmister, W.C.; Erbar, J.H.; Robinson, R.L., Calorimetric Determination of the Isothermal Effect of Pressure on the Enthalpy of Methane and Two Methane Propane Mixtures, AIChE J., 1968, 14, 923-28. [all data]

Gao, W.; Gasem, K.A.M.; Robinson, R.L., Solubilities of nitrogen in selected naphthenic and aromatic hydrocarbons at temperatures from 344 to 433 K and pressures to 22.8 MPa, J. Chem. Eng. Data, 1999, 44, 185-9. [all data]

Chao, K.-C.; Robinson, R.L.; Smith, M.L.; Kuo, C.-M., A Group Interaction Theory of Heat of Mixing and Application to Alcohol-paraffin Solutions in Chem. Eng. Progr., Symp. Soer. 61, 1967. [all data]