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Kraehenbuehl, M.A.; Gmehling, J., Vapor Pressures of Methyl tert-Butyl Ether, Ethyl tert-Butyl Ether, Isopropyl tert-Butyl Ether, tert-Amyl Methyl Ether, and tert-Amyl Ethyl Ether, J. Chem. Eng. Data, 1994, 39, 4, 759-762, https://doi.org/10.1021/je00016a026 . [all data]

Fiege, C.; Joh, R.; Petri, M.; Gmehling, J., Solid-Liquid Equilibria for Different Heptanones with Benzene, Cyclohexane, and Ethanol, J. Chem. Eng. Data, 1996, 41, 6, 1431-1433, https://doi.org/10.1021/je960140h . [all data]

Lohmann, J.; Joh, R.; Gmehling, J., Solid-Liquid Equilibria of Viscous Binary Mixtures with Alcohols, J. Chem. Eng. Data, 1997, 42, 6, 1170-1175, https://doi.org/10.1021/je9700683 . [all data]

Heine, A.; Fischer, K.; Gmehling, J., Various Thermodynamic Properties for Binary Systems with Tertiary Ethers, J. Chem. Eng. Data, 1999, 44, 3, 373-378, https://doi.org/10.1021/je980203r . [all data]

Fiege, C.; Joh, R.; Petri, M.; Gmehling, J., Solid-Liquid Equilibria for Different Heptanones with Benzene, Cyclohexane, and Ethanol, J. Chem. Eng. Data, 1996, 41, 6, 1431, https://doi.org/10.1021/je960140h . [all data]

Lohmann, J.; Joh, R.; Gmehling, J., Solid-Liquid Equilibria of Viscous Binary Mixtures with Alcohols, J. Chem. Eng. Data, 1997, 42, 6, 1170, https://doi.org/10.1021/je9700683 . [all data]

Ihmels, E.C.; Lemmon, E.W.; Gmehling, J., An Equation of State and Compressed Liquid and Supercritical Densities for Sulfur Dioxide, Fluid Phase Equilib., 2003, 207, 1-2, 111-130, https://doi.org/10.1016/S0378-3812(03)00004-9 . [all data]

Abbas, R.; Ihmels, E.C.; Enders, S.; Gmehling, J., Measurement of Transport Properties for Selected Siloxanes and Their Mixtures Used as Working Fluids for Organic Rankine Cycles, Ind. Eng. Chem. Res., 2011, 50, 14, 8756-8763, https://doi.org/10.1021/ie2002632 . [all data]

Moellmann, C.; Gmehling, J., Measurement of Activity Coefficients at Infinite Dilution Using Gas-Liquid Chromatography. 5. Results for N-Methylacetamide, N,N-Dimethylacetamide, N,N-Dibutylformamide, and Sulfolane as Stationary P, J. Chem. Eng. Data, 1997, 42, 35-40. [all data]

Noll, O.; Fischer, K.; Gmehling, J., Vapor-Liquid Equilibria and Enthalpies of Mixing for the Binary System Water + N-Methyl-2-pyrrolidone in the Temperature Range 80-140 .degree.C, J. Chem. Eng. Data, 1996, 41, 1434-1438. [all data]

Gmehling, J.; Boelts, R., Azeotropic Data for Binary and Ternary Systems at Moderate Pressures, J. Chem. Eng. Data, 1996, 41, 202-9. [all data]

Fischer, K.; Gmehling, J., Vapor-liquid equilibria, activity coefficients at infinite dilution and heats of mixing for mixtures of N-methyl pyrrolidone-2 with C5 or C6 hydrocarbons and for hydrocarbon mixtures, Fluid Phase Equilib., 1996, 119, 113-130. [all data]

Fischer, K.; Gmehling, J., Further development, status and results of the PSRK method for the prediction of vapor-liquid equilibria and gas solubilities, Fluid Phase Equilib., 1996, 121, 185-206. [all data]

Fischer, K.; Shulgin, I.; Rarey, J.; Gmehling, J., Vapor-liquid equilibria for the system water + tert.-pentanol at 4 temperatures, Fluid Phase Equilib., 1996, 120, 143-165. [all data]

deHaan, A.B.; Boelts, R.; Gmehling, J., Vapor-Liquid Equilibria and Excess Enthalpies for Binary Mixtures of Acrylonitrile with Hexane, Cyclohexane, Benzene, Toluene, 2-Butanone, and Acetonitrile, J. Chem. Eng. Data, 1996, 41, 1155-1159. [all data]

deHaan, A.B.; Gmehling, J., Excess Enthalpies for Various Binary Mixtures with N-Methylacetamide or Acetic Anhydride, J. Chem. Eng. Data, 1996, 41, 474-8. [all data]

Park, S.J.; Gmehling, J., Excess molar volumes at the 308.15 K for constituent binaries of n-decane, n-dodecane, 1-decanol and 1-dodecanol, Korean J. Chem. Eng., 1995, 12, 152-5. [all data]

Krahenbuhl, M.A.; Gmehling, J., The vapor pressures of 2-methyl-1-butanol and 3-methyl-1-butanol, Braz. J. Chem. Eng., 1995, 12, 228-34. [all data]

Jakob, A.; Joh, R.; Rose, C.; Gmehling, J., Solid-liquid equilibria in binary mixtures of organic compounds, Fluid Phase Equilib., 1995, 113, 117-26. [all data]

Gmehling, J., From UNIFAC to modified UNIFAC to PSRK with the help of DDB, Fluid Phase Equilib., 1995, 107, 1-29. [all data]

Gmehling, J.; Krentscher, B., Excess enthalpies of 12 binary liquid mixtures containing cyclohexane at elevated temperatures and pressures (up to 416 K and 1.9 MPa), ELDATA Int. Electron. J. Phys.-Chem. Data, 1995, 1, 181-90. [all data]

Gmehling, J.; Krentscher, B., The excess enthalpy of tetrahydrofuran (oxolane) + water, a binary liquid mixture with closed limiting miscibility curve, below (343.15 K), between ( 383.15 K), and above (416.29 K) the consolute tem, ELDATA Int. Electron. J. Phys.-Chem. Data, 1995, 1, 291-295. [all data]

Fischer, K.; Shulgin, I.; Gmehling, J., Direct calculation of SRK parameters from experimental PvT data in the saturation state, Fluid Phase Equilib., 1995, 103, 1-10. [all data]

deHaan, A.B.; Heine, A.; Fischer, K.; Gmehling, J., Vapor-Liquid Equilibria and Excess Enthalpies for Octane + N- Methylacetamide, Cyclooctane + N-Methylacetamide, and Octane + Acetic Anhydride at 125 .degree.C, J. Chem. Eng. Data, 1995, 40, 1228-32. [all data]

Atik, Z.; Gmehling, J., Activity coefficients at infinite dilution of fluorobenzene, 1', 1', 1'- trifluorotoluene and iodoethane in toluene, J. Soc. Alger. Chim., 1995, 5, 81-7. [all data]

Avedis, G.; Meents, B.; Gmehling, J., Excess enthalpies of (aniline + an alkane or an alkene) at the temperature 363.15 K, J. Chem. Thermodyn., 1995, 27, 939-44. [all data]

Park, S.J.; Fischer, K.; Gmehling, J., Excess Volumes for Alkanol + Morpholine Systems at 298.15 and 308.15 K, J. Chem. Eng. Data, 1994, 39, 859-62. [all data]

Kraehenbuehl, M.A.; Gmehling, J., Vapor Pressures of Methyl tert-Butyl Ether, Ethyl tert-Butyl Ether, Isopropyl tert-Butyl Ether, tert-Amyl Methyl Ether, and tert-Amyl Ethyl Ether, J. Chem. Eng. Data, 1994, 39, 759-62. [all data]

Fischer, K.; Gmehling, J., P-x and γ.infin. Data for the Different Binary Butanol-Water Systems at 50.degree.C, J. Chem. Eng. Data, 1994, 39, 309-15. [all data]

Rarey, J.R.; Gmehling, J., Computer-operated differential static apparatus for the measurement of vapor-liquid equilibrium data, Fluid Phase Equilib., 1993, 83, 279-87. [all data]

Gmehling, J., Excess enthalpies for 1,1,1-trichloroethane with alkanes, ketones, and esters, J. Chem. Eng. Data, 1993, 38, 143-6. [all data]

Dallinga, L.; Schiller, M.; Gmehling, J., Measurement of activity coefficients at infinite dilution using differential ebulliometry and non-steady-state gas-liquid chromatography, J. Chem. Eng. Data, 1993, 38, 147-55. [all data]

Atik, Z.; Meents, B.; Gmehling, J., Excess molar enthalpies of (fluorobenzene or trifluoromethylbenzene or iodoethane + methanol or toluene) at the temperature 313.15 K and pressure 0.7 MPa, J. Chem. Thermodyn., 1993, 25, 905-7. [all data]

Schiller, M.; Gmehling, J., Measurement of Activity Coefficients at Infinite Dilution Using Gas-Liquid Phases, J. Chem. Eng. Data, 1992, 37, 503-8. [all data]

Gmehling, J.; Meents, B., Excess enthalpy of cyclohexane +hexane & of 2,5,8,11,14-pentaoxapentadecane + benzene, Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1992, No. 3, 144-5. [all data]

Gmehling, J.; Meents, B., Excess enthalpy of some alkanone (c3-c7) + alkene (c6, c8) 2-methylpropane, Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1992, No. 3, 161-8. [all data]

Gmehling, J.; Meents, B., Excess enthalpy of some alkanol (c1-c4) +alkane(c5-c8) or 1-alkene(c6,c8) mixtures., Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1992, No. 3, 153-60. [all data]

Gmehling, J.; Meents, B., Excess enthalpy of some alkyl ethanoates (c4, c6, c8) + hexene or + 1-octene mixtures, Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1992, No. 3, 169-76. [all data]

Gmehling, J.; Meents, B., Excess enthalpy of some alkyl ethanoates (c4,c6,c8) + toluene or + 1,4-dimethylbenzene mixtures, Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1992, No. 3, 177-84. [all data]

Gmehling, J.; Meents, B., Excess enthalpy of propyl ethanoate + 2-butanone or + 1-butanol & of methyl dodecanoate + toulene or + methanol mixtures, Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1992, No. 3, 185-8. [all data]

Gmehling, J.; Meents, B., Excess enthalpy of some mixtures containing chloroalkanes (c1-c3), Int. DATA Ser., SEl. Data Mixtures, Ser. A, 1992, No. 3, 189-209. [all data]

Gmehling, J.; Meents, B., Excess enthalpy of ethanenitrile + 1-alkenes (c6, c8) or + 2-alkanones (c4, C7) & of hexane + nitroalkanes (c1, c2), Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1992, No. 3, 204-9. [all data]

Gmehling, J.; Meents, B., Excess enthalpy of 1-methyl-2-pyrrolidinone + cyclohexane, + benzene, + toluene, or + 1,4-dimethylbenzene, Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1992, No. 3, 210-3. [all data]

Gmehling, J.; Park, S.J.; Fischer, K.; Meents, B., Excess enthalpy of t-butyl methyl ether, methanol, or ethanol + butane or + 2-methylpropene, Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1992, No. 3, 146-52. [all data]

Nagata, I.; Meyer, T.; Gmehling, J., Correlation of binary liquid-liquid equilibrium data over a wide temperature range using UNIQUAC and extended UNIQUAC models, Fluid Phase Equilib., 1991, 65, 19-39. [all data]

Meyer, T.; Gmehling, J., Temperature dependence of binary liquid/liquid equilibria with the aid of gE-models, Chem.-Ing.-Tech., 1991, 63, 486-8. [all data]

Meyer, T.; Polka, H.M.; Gmehling, J., Low-pressure isobaric vapor-liquid equilibria of ethanol/water mixtures containing electrolytes, J. Chem. Eng. Data, 1991, 36, 340-2. [all data]

Holderbaum, T.; Gmehling, J., PSRK: a group contribution equation of state based on UNIFAC, Fluid Phase Equilib., 1991, 70, 251-65. [all data]

Holderbaum, T.; Utzig, A.; Gmehling, J., Vapor-liquid equilibria for the system butane/ethanol at 25.3, 50.6 and 72. 5.degree.C, Fluid Phase Equilib., 1991, 63, 219-26. [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]

Gmehling, J.; Matovu, A.; Naumann, D.; Wagner, H.G., Vapor-liquid equilibrium for the 2-butanone-cyclohexane system between 323 and 343 K, Chem.-Ing.-Tech., 1991, 63, 764-5. [all data]

Gmehling, J., Unpublished data, 1700, Dechema Chem. Data Ser. 1700. [all data]

Gmehling, J.; Onken, U.; Arlt, W.; Grenzheuser, P.; Weidlich, U.; Kolbe, B.; Rarey-Nies, J., Organic Hydroxy Compounds: Supplement 4. in Vapor-Liquid Equilibrium Data Collection, DECHEMA Chemis- try Data Series, Vol. 1, Part 2f, DECHEMA: Frankfurt, Ger., 1990. [all data]

Gmehling, J.; Tiegs, D.; Knipp, U., A comparison of the predictive capability of different group contribution methods, Fluid Phase Equilib., 1990, 54, 147. [all data]

Gmehling, J.; Tiegs, D.; Knipp, U., A comparison of the predictive capability of different group contribution methods [Erratum to document cited in CA112(24):224359t], Fluid Phase Equilib., 1990, 59, 337. [all data]

Park, S.J.; Gmehling, J., Isobaric Vapor-Liquid Equilibrium Data for the Binary Systems 1,3,5-Tri- methylbenzene/N-Formylmorpholine and m-Xylene/N-Formylmorpholine, J. Chem. Eng. Data, 1989, 34, 399. [all data]

Onken, U.; Rarey-Nies, J.; Gmehling, J., The Dortmund data bank: A computerized system for retrieval, correlation, and prediction of thermodynamic properties of mixtures, Int. J. Thermophys., 1989, 10, 739. [all data]

Knoop, C.; Tiegs, D.; Gmehling, J., Measurement of γ Using Gas-Liquid Chromatography 3. Results for the Stationary Phases 10-Nonadecanone, N-Formylmorpholine, 1-Pentanol, m-Xylene, and Toluene, J. Chem. Eng. Data, 1989, 34, 240. [all data]

Molnar-Jobbagy, M.; Rarey-Nies, J.; Gmehling, J., Gas solubility data bank for further development of phase equilibriu models, Fluid Phase Equilib., 1988, 42, 185. [all data]

Gaulhofer, A.; Kolbe, B.; Gmehling, J., Thermodynamic properties of ethanol and water- III. Description of the different excess functions using an empirical model, Fluid Phase Equilib., 1988, 39, 193. [all data]

Gmehling, J.; Onken, U.; Arlt, W.; Grenzheuser, P.; Weidlich, U.; Kolbe, B.; Rarey-Nies, J., Aqueous systems: Supplement 2. in Vapor-Liquid Equilibrium Data Collection, DECHEMA Chemis- try Data Series, Vol. 1, Part 1b, DECHEMA: Frankfurt, Ger., 1988. [all data]

Weidlich, U.; Gmehling, J., A modified UNIFAC model. 1. Prediction of VLE, hE, and γ.infin., Ind. Eng. Chem. Res., 1987, 26, 1372. [all data]

Weidlich, U.; Gmehling, J., Measurement of gamma(infinite) using gas-liquid chromatography. 1. Results for the stationary phases n-octacosane, 1-docosanal, 10-nonadecanone, and 1-eicosene, J. Chem. Eng. Data, 1987, 32, 138-42. [all data]

Weidlich, U.; Roehm, H.; Gmehling, J., Measurement of γ Using GLC. 2. Results for the stationary phases N-formylmorpholine and N-methylpyrrolidone, J. Chem. Eng. Data, 1987, 32, 450-3. [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]

Weidlich, U.; Berg, J.; Gmehling, J., Extension of Unifac by Headspace Gas Chromatography, J. Chem. Eng. Data, 1986, 31, 313. [all data]

Grenzheuser, P.; Gmehling, J., An Equation of State for the Description of Phase Equilibria and Caloric Quantities on the Basis of the "Chemical Theory", Fluid Phase Equilib., 1986, 25, 1. [all data]

Gmehling, J.; Tiegs, D.; Medina, A.; Soares, M.; Bastos, J.; Alessi, P.; Kikic, I., Activity Coefficients at Infinite Dilution, DECHEMA Chem- istry Data Series, Vol. IX, Part 1, DECHEMA: Frankfurt, Ger., 1986. [all data]

Weidlich, U.; Gmehling, J., Extension of UNIFAC by Headspace Gas Chromatography, J. Chem. Eng. Data, 1985, 30, 95. [all data]

Kolbe, B.; Gmehling, J., Thermodynamic Properties of Ethanol + Water. I. Vapour-Liquid Equil. Measurements from 90 to 150 deg. C by the Static Method, Fluid Phase Equilib., 1985, 23, 213. [all data]

Kolbe, B.; Gmehling, J., Thermodynamic properties of ethanol + water. II. Potentials and limits of GE models, Fluid Phase Equilib., 1985, 23, 227. [all data]

Gmehling, J., VLE Data for the Design of Separation Processes, AIChE Symp. Ser., 1985, 81, 244, 121-9. [all data]

Gmehling, J.; Onken, U.; Arlt, W.; Grenzheuser, P.; Weidlich, U.; Kolbe, B.; Rarey-Nies, J., Organic Hydroxy Compounds: Alcohols. in Vapor-Liquid Equilibrium Data Collection, DECHEMA Chemis- try Data Series, Vol. I, Part 2a, DECHEMA: Frankfurt, Ger., 1985. [all data]

Gmehling, J.; Onken, U.; Arlt, W.; Grenzheuser, P.; Weidlich, U.; Kolbe, B.; Rarey-Nies, J., Aliphatic Hydrocarbons: Supplement 1. in Vapor-Liquid Equilibrium Data Collection, DECHEMA Chemis- try Data Series, Vol. I, Part 6c, DECHEMA: Frankfurt, Ger., 1984. [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]

Gmehling, J., Isothermal vapor-liquid equilibria in binary systems formed by esters with alkenes., J. Chem. Eng. Data, 1983, 28, 27. [all data]

Gmehling, J., Phase Equilibria in Binary Systems FOrmed by Phenol with Benzene, n-Octane and n-Decane, J. Chem. Eng. Data, 1982, 27, 371. [all data]

Gmehling, J.; Onken, U.; Arlt, W.; Grenzheuser, P.; Weidlich, U.; Kolbe, B.; Rarey-Nies, J., Organic Hydroxy Compounds: Supplement 1. in Vapor-Liquid Equilibrium Data Collection, DECHEMA Chemis- try Data Series, Vol. I, Part 2c, DECHEMA: Frankfurt, Ger., 1982. [all data]

Gmehling, J.; Onken, U.; Arlt, W.; Grenzheuser, P.; Weidlich, U.; Kolbe, B.; Rarey-Nies, J.; Weidlich, U.; Kolbe, B., Aqueous systems: Supplement 1. in Vapor-Liquid Equilibrium Data Collection, DECHEMA Chemis- try Data Series, Vol. I, Part 1a, DECHEMA: Frankfurt, Ger., 1981. [all data]

Gmehling, J.; Onken, U.; Schulte, H.W., Vapor-Liquid Equilibrioa for the Binary Systems Diethyl Ether-Halothane (1,1,1-Trifluoro-2-bromo-2-chloroethane), Halothane-Methanol, and Diethyl Ether-Methanol, J. Chem. Eng. Data, 1980, 25, 29. [all data]

Gmehling, J.; Onken, U.; Arlt, W.; Grenzheuser, P.; Weidlich, U.; Kolbe, B.; Rarey-Nies, J., Aqueous systems. in Vapor-Liquid Equilibrium Data Collection, DECHEMA Chemis- try Data Series, Vol. I, Part 1, DECHEMA: Frankfurt, Ger., 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]

Gmehling, J.; Onken, U.; Arlt, W.; Grenzheuser, P.; Weidlich, U.; Kolbe, B.; Rarey-Nies, J., Aldehydes, ketones, ethers in Vapor-Liquid Equilibrium Data Collection, DECHEMA Chemis- try Data Series, Vol. I, Part 3/4, DECHEMA: Frankfurt, Ger., 1979. [all data]

Gmehling, J.; Onken, U.; Arlt, W.; Grenzheuser, P.; Weidlich, U.; Kolbe, B.; Rarey-Nies, J., Organic Hydroxy Compounds: Alcohols and Phenols. in Vapor-Liquid Equilibrium Data Collection, DECHEMA Chemis- try Data Series, Vol. 1, Part 2b, DECHEMA: Frankfurt, Ger., 1978. [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]

Horstman, S.; Gardeler, H.; Bolts, R.; Zudkevitch, D.; Gmehling, J., Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary Systems 2-Methyltetrahydrofuran with 2,2,4-Trimethylpentane (Isooctane), Ethanol, Toluene, Cyclohexane, and Methylcyclohexane, J. Chem. Eng. Data, 1999, 44, 959-64. [all data]

Gmehling, J.G.; Anderson, T.F.; Prausnitz, J.M., Solid-liquid equilibria using unifac, Ind. Eng. Chem. Fundam., 1978, 17, 269. [all data]