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23 matching references were found.

Borch-Jensen, C.; Staby, A.; Mollerup, J.M., Mutual solubility of 1-butanol and carbon dioxide, ethene, ethane, or propane at a reduced supercritical solvent temperature of 1.03, J. Supercrit. Fluids, 1994, 7, 231-44. [all data]

Staby, A.; Mollerup, J.M., Measurement of mutual solubilities of 1-pentanol and supercritical carbon dioxide, J. Supercrit. Fluids, 1993, 6, 15-19. [all data]

Staby, A.; Mollerup, J.M., Mutual solubilities of mono-alcohols and carbon dioxide: A review of experimental data, Fluid Phase Equilib., 1993, 89, 351-81. [all data]

Lundgaard, L.; Mollerup, J.M., Calculation of phase diagrams of gas-hydrates, Fluid Phase Equilib., 1992, 76, 141-50. [all data]

Staby, A.; Mollerup, J.M., Measurement of the Volumetric Properties of A Nitrogen-Methane-Ethane Mixture at 275, 310, and 345 K at Pressures To 60 MPa, J. Chem. Eng. Data, 1991, 36, 89. [all data]

Staby, A.; Mollerup, J.M., Measurement of solubilities of 1-pentanol in supercritical ethene, J. Supercrit. Fluids, 1991, 4, 4, 233-7. [all data]

Lundgaard, L.; Mollerup, J.M., The influence of gas phase fugacity and solubility on correlation of gas- hydrate formation pressure, Fluid Phase Equilib., 1991, 70, 199-213. [all data]

Mollerup, J.M., Simultaneous correlation of hard sphere diameters and second virial coefficients, Fluid Phase Equilib., 1989, 52, 59-65. [all data]

Mollerup, J.M.; Clark, W.M., Correlation of solubilities of gases and hydrocarbons in water, Fluid Phase Equilib., 1989, 51, 257. [all data]

Mollerup, J.M., Derivation of mixing rules from excess Gibbs energy models, Fluid Phase Equilib., 1986, 25, 323. [all data]

Mollerup, J.M., Measurement of the volumetric properties of sulfur hexafluorid from 260 to 340 K at pressures to 2.5 MPa, J. Chem. Eng. Data, 1985, 30, 21-3. [all data]

Mollerup, J.M., Measurement of the volumetric properties of methane and ethene at 310 K at pressures to 70 MPa and of propene from 270 to 345 K at pressures to 3 MPa by the Burnett method, J. Chem. Thermodyn., 1985, 17, 489. [all data]

Mollerup, J.M., Thermodynamic Properties of LNH and LPG Mixtutres in Intern. Symp. Vapor-Liquid Equil. Multicomp. Systems, Warszawa-Jablonna, Nov. 2-6, 1975, p 133, 1980. [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]

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]

Mollerup, J.M., Vapour-liquid equilibrium in ethylene + carbon dioxide and ethane + carbon dioxide, J. Chem. Soc., Faraday Trans. 1, 1975, 71, 2351-60. [all data]

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

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]