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33 matching references were found.

Emmerling, U.; Figurski, G.; Rasmussen, P., Densities and Kinematic Viscosities for the Systems Benzene + Methyl Formate, Benzene + Ethyl FOrmate, Benzene + Propyl Formate, and Benzen + Butyl Formate, J. Chem. Eng. Data, 1998, 43, 289-92. [all data]

Jonasson, A.; Persson, O.; Rasmussen, P., High-Pressure Solubility of Hydrogen in Dimethyl Ether, J. Chem. Eng. Data, 1995, 40, 1209-10. [all data]

Skovborg, P.; Rasmussen, P., Comments on: Hydrate dissociation enthalpy and guest size, Fluid Phase Equilib., 1994, 96, 223-31. [all data]

Cao, W.; Knudsen, K.; Fredenslund, A.; Rasmussen, P., Group-contribution viscosity predictions of liquid mixtures using UNIFAC- VLE parameters, Ind. Eng. Chem. Res., 1993, 32, 2088-92. [all data]

Chiavone-Filho, O.; Proust, P.; Rasmussen, P., Vapor-liquid equilibria for glycol ether + water systems, J. Chem. Eng. Data, 1993, 38, 128-31. [all data]

Chiavone-Filho, O.; Rasmussen, P., Solubilities of salts in mixed solvents, J. Chem. Eng. Data, 1993, 38, 367-9. [all data]

Dahl, S.; Dunalewicz, A.; Fredenslund, A.; Rasmussen, P., The MHV2 model: prediction of phase equilibria at sub- and supercritical conditions, J. Supercrit. Fluids, 1992, 5, 42-7. [all data]

Cao, W.; Fredenslund, A.; Rasmussen, P., Statistical thermodynamic model for viscosity of pure liquids and liquid mixtures, Ind. Eng. Chem. Res., 1992, 31, 2603-19. [all data]

Mueller, E.A.; Rasmussen, P., Density & excess vol. in aq. poly(ethylene glycol) sol., J. Chem. Eng. Data, 1991, 36, 214-17. [all data]

Lencka, M.; Persson, O.; Rasmussen, P., J. Chem. Thermodyn., 1991, 23, 851-58. [all data]

Kikic, I.; Fermeglia, M.; Rasmussen, P., UNIFAC prediction of vapor-liquid equilibria in mixed solvent-salt systems, Chem. Eng. Sci., 1991, 46, 2775-80. [all data]

Hansen, H.K.; Rasmussen, P.; Fredenslund, A.; Schiller, M.; Gmehling, J., Vapor-liquid equilibria by UNIFAC group contribution. 5. Revision and extension, Ind. Eng. Chem. Res., 1991, 30, 2352-5. [all data]

Dahl, S.; Fredenslund, A.; Rasmussen, P., The MHV2 model: a UNIFAC-based equation of state model for prediction of gas solubility and vapor-liquid equilibria at low and high pressuress, Ind. Eng. Chem. Res., 1991, 30, 1936-45. [all data]

Suarez, J.T.; Torres-Marchal, C.; Rasmussen, P., Prediction of surface tensions of nonelectrolyte solutions, Chem. Eng. Sci., 1989, 44, 782. [all data]

Fogh, F.; Rasmussen, P., Detection of High-Pressure Dew and Bubble Points Using a Microwave Technique, Ind. Eng. Chem. Res., 1989, 28, 371. [all data]

Froerup, M.D.; Jepsen, J.T.; Fredenslund, A.; Rasmussen, P., High pressure dew and bubble points from microwave measurements, Fluid Phase Equilib., 1989, 52, 229. [all data]

Gani, R.; Tzouvaras, N.; Rasmussen, P.; Fredenslund, A., Prediction of gas solubility and vapor-liquid equilibria by group contribution, Fluid Phase Equilib., 1989, 47, 133. [all data]

Urlic, L.; Rasmussen, P.; Fredenslund, A., Prediction of Viscosities of Liquid Mixtures by Unifac Method Preliminary Version in Phase Equil. Sep. Proc. Sept 8815, 1988. [all data]

Tiegs, D.; Gmehling, J.; Rasmussen, P.; Fredenslund, A., Vapor-Liquid Equilibria by UNIVAC Group Contribution 4. Revision and Extension, Ind. Eng. Chem. Res., 1987, 26, 159. [all data]

Suarez, J.T.; Torres-Marchal, C.; Rasmussen, P., Prediction of Surface Tensions of Nonelectrolyte Solutions in Phase Equil. Sep. Proc. Sept 8712, 1987. [all data]

Radnai, G.; Rasmussen, P.; Fredenslund, A., Vapor-liquid equilibrium data for binary mixtures containing aldehydes and esters and for the mixture 1,1,2-trichloro-1,2,2-trifluoroethane plus n-hexane, AIChE Symp. Ser., 1987, 83, 256, 70-79. [all data]

Radnai, G.; Bottini, S.; Rasmussen, P.; Fredenslund, A., Vapor-liquid equilibrium for binary systems with alkyl bromides, AIChE Symp. Ser., 1985, 81, 244, 102-20. [all data]

Christensen, C.; Gmehling, J.; Rasmussen, P.; Weidlich, U., Heats of Mixing Data Collection, DECHEMA Chemistry Data Series, Vol. III, DECHEMA: Frankfurt, Ger., 1984. [all data]

Macedo, E.A.; Rasmussen, P., Vapor-Liquid Equilibrium for the Binary Systems Ethyl Acetate-Acetic Acid and Ethyl Propionate-Propionic Acid, J. Chem. Eng. Data, 1982, 27, 463. [all data]

Magnussen, T.; Rasmussen, P.; Fredenslund, A., UNIFAC Parameter Table for Prediction of Liquid-Liquid Equilibria, Ind. Eng. Chem. Process Des. Dev., 1981, 20, 331. [all data]

Jensen, T.; Fredenslund, A.; Rasmussen, P., Pure-Component Vapor Pressures Using UNIFAC Group Contribution, Ind. Eng. Chem. Fundam., 1981, 20, 239. [all data]

Rasmussen, P., Recent Progress in the UNIFAC Group-Contribution Estimation of Activity Coefficients in Intern. Symp. Vapor-Liquid Equil. Multicomp. Systems, Warszawa-Jablonna, Nov. 2-6, 1975, p 107, 1980. [all data]

Skjold-Jorgensen, S.; Kolbe, B.; Gmehling, J.; Rasmussen, P., Vapor-Liquid Equilibria by UNIFAC Group Contribution - Revision and Extension, Ind. Eng. Chem. Process Des. Dev., 1979, 18, 714. [all data]

Fredenslund, A.; Rasmussen, P., Correlation of pure component gibbs energy using unifac group contribution, AIChE J., 1979, 25, 203. [all data]

Rasmussen, P.; Kierkegaard, L.; Fredenslund, A., Chemical Engineering with per Soltoft, Oesergaard, K.; Fredenslund, Aa., Eds., Teknisk Forlag: Copenhagen, p 129, 1977. [all data]

Fredenslund, A.; Gmehling, J.; Michelsen, M.L.; Rasmussen, P.; Prausnitz, J.M., Computerized design of multicomponent distillation columns using the unifac group contribution method for calculation of activity coefficients, Ind. Eng. Chem. Process Des. Dev., 1977, 16, 450. [all data]

Gmehling, J.; Rasmussen, P.; Fredenslund, A., Vapor-Liquid Equilibrium bu UNIFAC Group Contribution. Revision and Extension 2., Ind. Eng. Chem., Process Des. Dev., 1982, 21, 118-27. [all data]

Rasmussen, P., Identification of Volatile Components of Jacjfruit by Gas Chromatography / MAss Spectrometry with Two Different Columns, Anal. Chem., 1983, 55, 8, 1331-1335, https://doi.org/10.1021/ac00259a033 . [all data]