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Jonasson, A.; Persson, O.; Fredenslund, A., High Pressure Solubility of Carbon Dioxide and Carbon Monoxide in Dimethyl Ether, J. Chem. Eng. Data, 1995, 40, 296-300. [all data]

Nielsen, F.; Olsen, E.; Fredenslund, A., Environ. Sci. technol., 1994, 28, 2133. [all data]

Jonsdottir, S.O.; Rasmussen, K.; Fredenslund, A., UNIQUAC parameters determined by molecular mechanics, Fluid Phase Equilib., 1994, 100, 121-38. [all data]

Jonasson, A.; Savoia, M.; Persson, O.; Fredenslund, A., Isothermal vapor-liquid equilibrium data for ether + glycol, chloroalkene + glycol, epoxy ether + alkane, epoxy ether + alkene, and epoxy ether + chloroalkane systems, J. Chem. Eng. Data, 1994, 39, 134-9. [all data]

Voros, N.; Proust, P.; Fredenslund, A., Liquid-liquid phase equilibria of aqueous two-phase systems containing salts and polyethylene glycol, Fluid Phase Equilib., 1993, 90, 333-53. [all data]

Knudsen, K.; Stenby, E.H.; Fredenslund, A., A comprehensive comparison of mixing rules for calculation of phase equilibria in complex systems, Fluid Phase Equilib., 1993, 82, 361-8. [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]

Wolff, S.R.; Danner, R.P.; Fredenslund, A., Extension of the group contribution equation of state for the calculation of gas solubilities, Fluid Phase Equilib., 1992, 81, 109-27. [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]

Viktorov, A.I.; Fredenslund, A., Application of the hole quasi-chemical group contribution equation of state for phase equilibrium calculation in systems with association, Fluid Phase Equilib., 1991, 66, 77-101. [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]

Aasberg-Petersen, K.; Stenby, E.; Fredenslund, A., Prediction of high-pressure gas solubilities in aqueous mixtures of electrolytes, Ind. Eng. Chem. Res., 1991, 30, 2180-5. [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]

Pedersen, K.S.; Thomassen, P.; Fredenslund, A., On the dangers of "tuning" equation of state parameters, Chem. Eng. Sci., 1988, 43, 269. [all data]

Heidemann, R.A.; Fredenslund, A., Vapor-liquid equilibria in complex mixtures, Inst. Chem. Eng. Symp. Ser., 1988, No. 104, A291-A322. [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]

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]

Pedersen, K.S.; Lund, T.; Fredenslund, A., Surface Tension of Petroleum Mixtures in Phase Equil. Sep. Proc. Sept 8713, 1987. [all data]

Tochigi, K.; Kojima, K.; Fredenslund, A., Prediction of Vapor-Liquid-Liquid Equilibria Using the UNIFAC, Modified UNIFAC, and GC-EOS Models, Fluid Phase Equilib., 1986, 25, 231. [all data]

Fredenslund, A.; Pedersen, K.S., Prediction of Transport and Surface Properties in Phase Equil. Sep. Proc. Sept 8626, 1986. [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]

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]

Fredenslund, A., Thermodynamic Consistency of High-Pressure Vapor-Liquid Equilibrium Data in Intern. Symp. Vapor-Liquid Equil. Multicomp. Systems, Warszawa-Jablonna, Nov. 2-6, 1975, p 87, 1980. [all data]

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

Christensen, P.L.; Fredenslund, A., Thermal Conductivity of Gaseous Mixtures of Methane with Nitrogen and Carbon Dioxide, J. Chem. Eng. Data, 1979, 24, 281-83. [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]

Grauso, L.; Fredenslund, A.; Mollerup, J.M., Vapour-liquid equilibrium data for the systems c(2)h(6) + n(2), c(2)h(4) + n(2), c(3)h(8) + n(2), and c(3)h(6) + n(2)., Fluid Phase Equilib., 1977, 1, 13. [all data]

Grauso, L.; Fredenslund, A., Measurement and correlation of high-pressure vapor-liquid equilibrium data, Ber. Bunsen-Ges. Phys. Chem., 1977, 81, 1088. [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]

Mollerup, J.M.; Fredenslund, A., Vapor-liquid equilibria in the freon 12 + freon 13 system, J. Chem. Eng. Data, 1976, 21, 299. [all data]

Fredenslund, A.; Mollerup, J.M.; Hall, K.R., Vapor-liquid equilibrium data for the systems c(2)h(4) + c(2)h(6) and co(2) + c(2)h(4) + c(2)h(6), J. Chem. Eng. Data, 1976, 21, 301. [all data]

Fredenslund, A.; Jones, R.L.; Prausnitz, J.M., Group Contribution Estimation of Activity Coeff. in Nonideal Mixtures mixtures, AIChE J., 1975, 21, 1086. [all data]

Fredenslund, A.; Mollerup, J.M., Gas-liquid equilibrium of hydrogen sulphide + carbon monoxide, J. Chem. Thermodyn., 1975, 7, 677. [all data]

Christiansen, L.J.; Fredenslund, A., Thermodynamic consistency using orthogonal collocation or computation of equilibrium vapor compositions at high pressures, AIChE J., 1975, 21, 49. [all data]

Fredenslund, A.; Mollerup, J.M., Measurement and prediction of equilibrium ratios for the ethane + carbon dioxide system, J. Chem. Soc., Faraday Trans. 1, 1974, 70, 1653. [all data]

Christiansen, L.J.; Fredenslund, A., Vapor-liquid equilibria of the methane + argon + carbon monoxide system, Cryogenics, 1974, 14, 10. [all data]

Christiansen, L.J.; Fredenslund, A.; Gardner, N., Gas-liquid equilibria of the co(2) + co and co(2) + ch(4) + co systems, Adv. Cryog. Eng., 1974, 19, 309. [all data]

Mollerup, J.M.; Fredenslund, A., Molecular thermodynamics of solutions in the normal and critical regions: II activity coefficients for the ar + n(2), c(2)h(6) + c(2)h(4) and c(3)h(6 ) + co(2) systems, Chem. Eng. Sci., 1973, 28, 1295-302. [all data]

Fredenslund, A.; Mollerup, J.M.; Christiansen, L.J., Apparatus for Accurate Determination of Vapor-Liquid Equilibrium Properties and Gas PVT[pressure-volume-temperature] Properties, Cryogenics, 1973, 13, 414-9. [all data]

Christiansen, L.J.; Fredenslund, A.; Mollerup, J.M., Vapor-liquid equilibrium of the methane - argon, methane - carbon monoxide, and argon - carbon monoxide systems at elevated pressures, Cryogenics, 1973, 13, 405. [all data]

Fredenslund, A.; Mollerup, J.M.; Persson, O., Gas-liquid equilibrium of oxygen + carbon dioxide system, J. Chem. Eng. Data, 1972, 17, 440. [all data]

Fredenslund, A.; Sather, G.A., Gas-liquid equilibrium of the oxygen + carbon dioxide system, J. Chem. Eng. Data, 1970, 15, 17. [all data]

Fredenslund, A.; Sather, G.A., Molecular thermodynamics of solutions at moderately high pressures, Ind. Eng. Chem. Fundam., 1969, 8, 718. [all data]

Fredenslund, A., High pressure vapor-liquid equilibria, Ph.D. Dissertation, University of Wisconsin, Ann Arbor, MI, 1968. [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]