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2013

  • T. Hector, L. Uhlig, J. Gmehling
    Prediction of Different Thermodynamic Properties for Systems of Alcohols and Sulfate-based Anion Ionic Liquids Using modified UNIFAC
    Fluid Phase Equilib. 338, 135-140 (2013).

2012

  • P. Belting, J. Rarey, J. Gmehling, R. Ceriani, O. Chavone-Filho, A.J.A. Meirelles
    Activity Coefficient at Infinite Dilution Measurements for Organic Solutes (polar and non-polar) in Fatty Compounds: Saturated Fatty Acids
    J. Chem. Thermodyn. 55, 42-49 (2012).
  • M. Kleiber, J. Gmehling
    Funktionen und Nutzen der Chemischen Industrie, p. 249 - 282
    "Die Modernität der Industrie", Eds. B. P. Priddat, K.-W. West
    Metropolis-Verlag, Marburg 2012.
  • A. Mohs, J. Gmehling
    A revised LIQUAC and LIFAC model (LIQUAC*/LIFAC*) for the prediction of properties
    of electrolyte solutions
    Fluid Phase Equilib. (2012)
  • V.M.T.M. Silva, C.S.M. Pereira, A.E. Rodrigues, S.P. Verevkin, V.N. Emel'Yanenko, I.V. Garist, J. Gmehling
    Experimental and Theoretical Study of Chemical Equilibria in the Reactive Systems of Acetal Synthesis
    Ind. Eng. Chem. Res. 51, 12723-12729 (2012).
  • Z. Xue, T. Mu, J. Gmehling
    Comparison of the a priori COSMO-RS models and Group Contribution Methods: Original UNIFAC, Modified UNIFAC(Do) as well as Modified UNIFAC(Do) Consortium
    Ind. Eng. Chem. Research 51, 11809-11817 (2012)
  • R. D. Chirico, T. W. de Loos, J. Gmehling, A. R. H. Goodwin, S. Gupta, W. H. Haynes, K. N. Marsh, V. Rives, J. D. Olson, C. Spencer, J. F. Brenecke, J. P. Trusler
    Guidelines for Reporting of Phase Equilibrium Measurements
    Pure Appl. Chem. 84 (8) 1785-1813 (2012).
  • D. Montaño, I. Gascón, B. Schmid, J. Gmehling, C. Lafuente
    Experimental and Predicted Properties of the Binary Mixtures Containing an Isomeric Chlorobutane and Butyl Ethyl Ether
    J. Chem. Thermodyn. 51, 150-158 (2012).
  • H. Matsuda, M. Fukano, S. Kikkawa, D. Constantinescu, K. Kurihara, K. Tochigi, K. Ochi, J. Gmehling
    Ebulliometric Determination and Prediction of (vapour-liquid) Equilibria for Binary and Ternary Mixtures Containing Alcohols (C1-C4) and Dimethylcarbonate
    J. Chem. Thermodyn. 44, 84-96 (2012).
  • B. Schmid, J. Gmehling
    Revised Parameters and Typical Results for the VTPR Group Contribution Equation of State
    Fluid Phase Equilib. 317, 110-126 (2012)

2011

  • D. Montaño, I. Gascón, B. Schmid, J. Gmehling, C. Lafuente
    Simultaneous Prediction of Densities and Vapor-Liquid Equilibria of Mixtures Containing an Isomeric Chlorobutane and Methyl tert.-Butyl Ether Using the VTPR Model
    Ind. Eng. Chem. Res. 50, 14193-14202 (2011).
  • Mi-Yi Li, Li-Sheng Wang, J. Gmehling
    Thermodynamics of Phase Equilibria in Aqueous Strong Electrolyte Systems. Ind. Eng. Chem. Res. 50(6): 3621-3631 (2011)
  • Mi-Yi Li, Li-Sheng Wang, Bo Jiang, J. Gmehling
    Generalized LIQUAC Model for the Single- and Mixed-Solvent Strong Electrolyte Systems, AIChE J. 57(9): 2535-2546 (2011).
  • K. Tochigi, J. Gmehling
    Determination of ASOG Parameters - Extension and Revision
    J. Chem. Eng. Japan 44(5) 304-306 (2011)
  • H.Matsuda, H. Takahara, S. Fujino, D. Constantinescu, K. Kurihara, K. Tochigi, K. Ochi, J. Gmehling
    Selection of entrainers for the separation of the binary azeotropic system methanol + dimethyl carbonate by extractive distillation
    Fluid Phase Equilib. 310, 166-181 (2011).
  • D. Montaño, I. Gascón, R. Bölts, J. Gmehling, C. Lafuente
    Isothermal Vapour-Liquid Equilibria and Excess Enthalpies at 298.15 K for the Binary Mixtures Containing an Isothermal Chlorobutane and Diisopropylether
    Fluid Phase Equilib. 308, 8-14 (2011)
  • A. Mohs, S. Decker, J. Gmehling
    The Solid-Liquid Equililibrium of the Binary System H2O-DMSO and the Influence of a Salt (NaCl, KCl) on the Thermodynamic Behavior - Correlations Using a Revised LIQUAC Model
    Fluid Phase Equilib. 304, 11-20 (2011)
  • R. Abbas, E. C. Ihmels, S. Enders, J. Gmehling
    Measurement of Transport Properties for Selected Siloxanes and their Mixtures Used as Working Fluids for Organic Rankine Cycles
    Ind. Eng. Chem. Research 50, 8756-8763 (2011).
  • R. Abbas, A. Schedemann, C. Ihmels, S. Enders, J. Gmehling
    Measurement of Thermophysical Pure Component Properties for a few Siloxanes Used as Working Fluids for Organic Rankine Cycles
    Ind. Eng. Chem. Research 50, 9748-9757 (2011).
  • J. Berje, A. Schedemann, J. Gmehling
    Liquid Densities of Acetone and n-Heptane and Excess Volumes of the Binary System in a Wide Temperature and Pressure Range
    Fluid Phase Equilib. 300, 10-115 (2011).
  • S. Nebig, J. Gmehling
    Prediction of Phase Equilibria and Excess Properties for Systems with Ionic Liquids Using modified UNIFAC: Typical Results and Present Status of the modified UNIFAC Matrix for Ionic Liquids
    Fluid Phase Equilib. 302, 220-225 (2011).
  • A. Diedrichs, J. Gmehling
    Solubility Prediction of Active Pharmaceutical Ingredients in Pure Solvents (Alkanes, Alcohols, Water) with Various Activity Coefficient Models
    Ind. Eng. Chem. Res. 50, 1757-1769 (2011).
  • B. Schmid, J. Gmehling
    The Universal Group Contribution Equation of State - Present Status and Potential for Process Development
    Fluid Phase Equilib. 302, 213-219 (2011).
  • Mi-Yi Li, Li-Sheng Wang, Kun-Peng Wang, B. Jiang, J. Gmehling
    Experimental measurement and modeling of solubility of LiBr and LiNO3 in methanol, ethanol, 1-propanol, 2-propanol and 1-butanol.
    Fluid Phase Equilib. 307, 104-109 (2011).
  • R. Abbas, C. Ihmels, S. Enders, J. Gmehling
    Joule-Thomson Coefficients and Joule-Thomson Inversion Curves for Pure Compounds and Binary Systems Predicted with the Group Contribution Equation of State VTPR
    Fluid Phase Equilib. 306, 181-189 (2011).
  • H. Matsuda, K. Tochigi, V- Liebert, J. Gmehling
    Vapor-Liquid Equilibria of Ternary Systems with 1-Ethyl-3-methylimidazolium ethylsulfate Using Headspace Gas Chromatography
    Fluid Phase Equilib. 307, 197-201 (2011).
  • A. Mohs, S. Decker, J. Gmehling
    The Solid-Liquid Equililibrium of the Binary System H2O-DMSO and the Influence of a Salt (NaCl, KCl) on the Thermodynamic Behavior - Correlations Using a Revised LIQUAC Model
    Fluid Phase Equilib. 304, 11-20 (2011).
  • 2010


    • I. Hahnenkamp, G. Graubner, J. Gmehling
      Measurement and prediction of solubilities of active pharmaceutical ingredients
      Int. J. of Pharmaceutics 388, 73-81 (2010)
    • S. Thiede, S. Horstmann, T. Meisel, J. Gmehling
      Experimental determination of vapor-liquid equilibria and excess enthalpy data for the binary system 2-methyl-1-butanol + 3-methyl-1-butanol as a test mixture for distillation columns
      Ind. Eng. Chem. Res., 49, 1844-1847 (2010)
    • L. Brandt, O. Elizalde-Solis, L.A. Galicia-Luna, J. Gmehling
      Solubility and Density Measurements of Palmitic Acid in Supercritical Carbon Dioxide + Alcohol Mixture
      Fluid Phase Equilib. 289, 72-79 (2010)
    • V. Liebert, T. Hector, J. Gmehling
      Chemical Equilibrium Conversion of tert.-Amyl-methyl-ether Synthesis in the Presence of n-Pentane, Tetrahydrofuran or Benzene
      Ind. Eng. Chem. Research 49, 4412-4419 (2010)
    • S. Nebig, J. Gmehling
      Measurements of different thermodynamic properties of systems containing ionic liquids and prediction of these properties using modified UNIFAC (Dortmund)
      Fluid Phase Equilib. 294, 206-212 (2010).
    • B. Mokhtarani, J. Gmehling
      Measurement of Vapor - Liquid Equilibria of Ionic Liquids with Aromatic or Alkanes Using Headspace Gas Chromatography
      J. Chem. Thermodyn. 42, 1036-1038 (2010).
    • S. Cehreli, J. Gmehling
      Phase Equilibria for Benzene-Cyclohexene and Activity Coefficients at Infinite Dilution for the Ternary Systems with Ionic Liquids
      Fluid Phase Equilib. 295, 125-129 (2010).
    • Miyi Li, D. Constantinescu, L. Wang, A. Mohs, J. Gmehling
      Solubilities of NaCl, KCl, LiCl, and LiBr in Methanol, Ethanol, Acetone, and Mixed Solvents and Correlation Using the LIQUAC Model
      Ind. Eng. Chem. Research 49, 4981-4988 (2010).
    • S. Thiede, S. Horstmann, J. Gmehling
      Vapor-Liquid Equilibrium Data, Excess Enthalpy Data, and Azeotropic Data for the Binary System Dibutyl Ether + o-Xylene
      J. Chem. Eng. Data 55, 3155-3159 (2010).
    • A. Schedemann, C. Ihmels, J. Gmehling
      Liquid Densities of THF and Excess Volumes for the Mixture with Water in a Wide Pressure and Temperature Range
      Fluid Phase Equilib. 295, 201-207 (2010).
    • B. Schmid, J. Gmehling
      From van der Waals to VTPR: The systematic improvement of the van der Waals equation of state
      J. of Supercritical Fluids 55, 438-447 (2010).

    2009

    • J. Huang, J. Li, J. Gmehling
      Prediction of solubilities of Salts, Osmotic Coefficients and Vapor-Liquid Equilibria for Single and Mixed Solvent Electrolyte Systems Using the LIQUAC model
      Fluid Phase Equilib., 275, 8-20 (2009)
    • S. Nebig, V. Liebert, J. Gmehling
      Measurement and prediction of activity coefficients at infinite dilution, vapor-liquid equilibria, and excess enthalpies of binary systems with 1,1-dialkylpyrrolidinium bis(trifluoromethylsulfonyl)- imide using mod. UNIFAC (Dortmund)
      Fluid Phase Equilib., 277, 61-67 (2009)
    • J. J. B. Machado, T. W. de Loos, E. C. Ihmels, K. Fischer, J. Gmehling
      Erratum to "High Pressure Solid-Solid and Solid-Liquid Transition Data for Long Chain Alkanes"
      [J. Chem. Thermodyn., 1632-1637 (2008)]
      J. Chem. Thermodyn. 41, 716 (2009)
    • J. Gmehling
      Present Status and Potential of Group Contribution Methods for Process Development
      J. Chem. Thermodyn. 41, 731-747 (2009)
    • A. Mohs, A. Jakob, J. Gmehling
      Analysis of a concept for predicting missing group interaction parameters for the UNIFAC model using connectivity indices
      AIChE J., 55, 1614-1625 (2009)
    • A. Westerholt, V. Liebert, J. Gmehling
      Influence of Ionic Liquids on the Separation Factor of three Standard Separation Problems
      Fluid Phase Equilib., 280, 56-60 (2009)
    • M. Bahlmann, S. Nebig, J. Gmehling
      Measurement of activity coefficients at infinite dilution of aliphatics and olefins in 1-alkyl-3-methylimidazolium tetrafluoroborate
      Fluid Phase Equilib., 282, 113-116 (2009)
    • K. Tochigi, J. Rarey, J. Gmehling
      Recommended NRTL Parameters by Simultaneous Correlation of VLE, Infinite Dilution Activity Coefficients and Excess Enthalpy Data
      J. Chem. Eng. Japan 42 (6), 376-380 (2009)
    • L. Negadi, I. Mokbel, A. Negadi, A. Ait Kaci, J. Jose, J. Gmehling
      Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butryric Acid + Toluene)
      J. Chem. Eng. Data, 54, 2045-2048 (2009)
    • Y. Nannoolal, J. Rarey, D. Ramjugernath
      Estimation of Pure Component Properties, Part 4: Estimation of the Saturated Liquid Viscosity of Non-Electrolyte Organic Compounds via Group Contributions and Group Interactions
      Fluid Phase Equilib., 281 (2), 97-119 (2009)
    • D. Constantinescu, J. Rarey, J. Gmehling
      Application of COSMO-RS Type Models to the prediction of Excess Enthalpies
      Ind. Eng. Chem. Res., 48 (18), 8710-8725 (2009)
    • J. Gmehling, A. Jakob
      Letter to the Editor about "Phase equilibria on four binary systems containing 3-methylthophene"by E. Sapei, et al. [Fluid Phase Equilib. 279 (2009) 81-86]"
      Fluid Phase Equilib. 286, 101-102 (2009)
    • T. Teutenberg, P. Wagner, J. Gmehling
      Development of a Concept for High-Temperature Liquid Chromatography.
      Part I: Determination of the Vapour Pressures of Binary Solvent Mixtures - Implications for Liquid Chromatographic Separations
      J. of Chromatography A 1216, 6471-6480 (2009)
    • T. Teutenberg, P. Wagner, J. Gmehling
      Development of a Concept for High-Temperature Liquid Chromatography.
      Part II: Determination of the Viscosities of Binary Solvent Mixtures - Implications for Liquid Chromatographic Separations
      J. of Chromatography A 1216, 8470-8479 (2009)
    • T. Teutenberg, P. Wagner, J. Gmehling
      Development of a Concept for High-Temperature Liquid Chromatography.
      Part III: Determination of the Static Permittivities of Pure Solvents and Binary Solvent Mixtures - Implications for Liquid Chromatographic Separations
      J. of Chromatography A 1216, 8480-8487 (2009)
    • T. Mu, J. Rarey, J. Gmehling
      Development of a group contribution method to predict the surface charge density distribution of molecules for COSMO-SAC
      AIChE J. 5 (12) 3298-3300 (2009)

    2008

    • B. Schmid, M. Döker, J. Gmehling
      Esterification of Ethyleneglycol with Acetic Acid Catalyzed by Amberlyst 36
      Ind. Eng. Chem. Res. 47, 698-703 (2008)

    • T. Mu, J. Rarey, J. Gmehling
      Reply to "Comments on `Performance of COSMO-RS with Sigma Profiles from Different Model Chemistries`"
      Ind. Eng. Chem. Res. 47, 989 (2008)

    • T. Sanz, J. Gmehling
      Isothermal Vapor-Liquid Equilibria for Different Binary Mixtures Involved in Alcoholic Distillation
      Fluid Phase Equilib. 267, 158-162 (2008).

    • V. Liebert, S. Nebig, J. Gmehling
      Measurement of Vapor-Liquid Equilibria, Excess Enthalpies, and Activity Coefficients at Infinite Dilution for Systems with Ionic Liquids and Prediction of these Properties Using mod. UNIFAC (Dortmund)
      Fluid Phase Equilib. 268/1-2, 14-20 (2008).

    • R. Abbas, J. Gmehling
      Vapor-Liquid Equilibria, Azeotropic Data, Excess Enthalpies, Activity Coefficients at Infinite Dilution, and Solid-Liquid Equilibria for Binary Alcohol-Ketone Systems
      Fluid Phase Equilib. 267, 119-126 (2008).

    • T. Brinkmann, H. Pingel, T. Wolff, M. Döker, E. Bozek-Winkler, J. Gmehling
      Verhalten verschiedener Membranmaterialien für die Aufbereitung organischer Produktströme aus Reaktivrektifikationskolonnen
      Chem.-Ing.-Tech. 80, 157 (2008)

    • M. Grigiante, P. Stringari, G. Scalabrin, E. C. Ihmels, K. Fischer, J. Gmehling
      Vapor-Liquid-Liquid Equilibria and Excess Molar Enthalpies of Binary and Ternary Mixtures of 2-Propanol, Water and Propylene.
      J. Chem. Thermodyn. 40, 537-548 (2008).
    • R. Abbas, J. Gmehling
      Corrigendum to " Vapor-Liquid Equilibria, Azeotropic Data, Excess Enthalpies, Activity Coefficients at Infinite Dilution, and Solid-Liquid Equilibria for Binary Alcohol-Ketone Systems" [Fluid Phase Equilib. 267, 119-126 (2008)]
      Fluid Phase Equilib. 274, 105-107 (2008).

    • J.J.B. Machado, T.W. de Loos, E. C. Ihmels, K. Fischer, J. Gmehling
      High Pressure Solid-Solid and Solid-Liquid Transition Data for Long Chain Alkanes
      J. Chem. Thermodyn. 40, 1632-1637 (2008)

    • T. Mu, J. Gmehling
      Conductor-Like Screening Model for Real Solvents (COSMO-RS)
      Prog. Chem. (China) 20 (10), 1487-1494 (2008) J. Chem. Thermodyn. 40, 1632-1637 (2008)

    • Y. Nannoolal, J. Rarey, D. Ramjugernath
      Estimation of Pure Component Properties Part 3: Estimation of the Vapor Pressure of Non-Electrolyte Organic Compounds via Group Contributions and Group Interactions
      Fluid Phase Equilib., 269, 117-133 (2008)

    • B. Moller, J. Rarey, D. Ramjugernath
      Estimation of the Vapor Pressure of Non-Electrolyte Organic Compounds via Group Contributions and Group Interactions
      J. Mol. Liqu., 143, 52-63 (2008)

    • F. Amireche-Ziar, G. Boukais-Belaribi, A. Jakob, I. Mokbel, F. Brahim Belaribi
      Isothermal vapour-liquid equilibria of binary systems of 1,2-dichloroethanewith ethers
      Fluid Phase Equilib., 268, 39-44 (2008)

    2007


    • S.-J. Park, K. Han, J. Gmehling
      Isothermal Phase Equilibria and Excess Molar Enthalpies for Binary Systems with Dimethyl Ether at 323.15 K
      J. Chem. Eng. Data 52, 1814-1818 (2007)

    • ­
    • T. Mu, J. Rarey, J. Gmehling
      Development of a Group Contribution Method to Predict the Surface Charge Density Distribution of Molecules for COSMO-RS(Ol)
      AIChE J. 53, 13231-3240 (2007)

    • B. Schmid, M. Döker, J. Gmehling
      Measurement of the Thermodynamic Properties for the Reactive System Ethylenglycol-Acetic Acid
      Fluid Phase Equilib. 258, 115-124 (2007)

    • S. Nebig, R. Bölts, J. Gmehling
      Measurement of Vapor-liquid-Equilibria (VLE) and Excess Enthalpies (HE)of Binary Systems with 1-Alkyl-3-Methylimidazolium bis(trifluoromethylsulfonyl)imide and Prediction of these Properties and γ using mod. UNIFAC (Dortmund)
      Fluid Phase Equilib. 258, 168 (2007)

    • T. Mu, J. Rarey, J. Gmehling
      Performance of COSMO-RS with Sigma Profiles from Different Model Chemistries
      Ind. Eng. Chem. Res. 46, 6612-6629 (2007)­

    • A. Jabloniec, S. Horstmann, J. Gmehling
      Experimental Determination and Calculation of Gas Solubility Data for Nitrogen in Different Solvents
      Ind. Eng. Chem. Res. 46, 4654-4659 (2007)

    • F. Forner, M. Döker, J. Gmehling, J.-U. Repke
      Anfahrstrategien für die Reaktivrektifikation in Boden- und Packungskolonnen
      Chemie Ingenieur Technik 79, 367-376 (2007)

    • So-Jin Park, Kyu-Jin Han, J. Gmehling
      Vapor-Liquid Equilibria and HE for Binary Systems of Dimethyl Ether (DME) with C1-C4 Alkan-1-ols at 323.15 K and Liquid-Liquid Equilibria for Ternary System of DME + Methanol + Water at 313.15 K
      J. Chem. Eng. Data 52, 230-234 (2007)

    • Y. Nannoolal, J. Rarey, D. Ramjugernath
      Estimation of Pure Component Properties Part 2: Estimation of Critical Data by group Contribution
      Fluid Phase Equilib., 252, 1-27 (2007)

    2006


    • P. Marchi, G. Scalabrin, E. C. Ihmels, K. Fischer, J. Gmehling
      Bubble Pressure Measurements for the (1,1,1,2-Tetrafluoroethane + Triethylene Glycol Dimethylether) System
      J. Chem. Thermodyn. 38 (11) 1247-1253 (2006)

    • E. Bozek, J. Gmehling
      Transesterification of Methyl Acetate and n-Butanol Catalyzed by Amberlyst 15
      Ind. Eng. Chem. Res. 45, 6648-6654 (2006)

    • T. Sanz, J. Gmehling
      Esterification of Acetic Acid with Isopropanol Couplet with Pervaporation Part II: Study of a Pervaporation Reactor
      Chem. Eng. J. 123, 9-14 (2006)

    • T. Sanz, J. Gmehling
      Esterification of Acetic Acid with Isopropanol Couplet with Pervaporation Part I: Kinetics and Pervaporation Studies
      Chem. Eng. J. 123, 1-8 (2006)

    • E. Collinet, J. Gmehling
      Prediction of Phase Equilibria with Strong Electrolytes with the Help of the Group Contribution Equation of State VTPR
      Fluid Phase Equilibria 246, 111-118 (2006)

    • J. Gmehling, W. Cordes
      Experimental, Calculated and Predicted Solubilities - Basis for the Synthesis and Design of Thermal Separation Processes, in Development and Applications in Solubility,
      editor: T. M. Letcher, RSC Publishing, Cambridge 2007

    • A. Diedrichs, J. Gmehling
      Prediction of Heat Capacities of Liquids by the Group Contribution Equation of State VTPR
      Fluid Phase Equilibria 248, 56-69 (2006)

    • A. Diedrichs, J. Gmehling
      Measurement of Heat Capacities from Ionic Liquids by Differential Scanning Calorimetry
      Fluid Phase Equilibria 244, 68-77 (2006)

    • L. Negadi, M. Wilken, J. Gmehling
      Solid-Liquid Equilibria for Binary Organic Systems Containing 1-Methoxy-2-propanol and 2-butoxy-1-ethanol
      J. Chem. Eng. Data 51, 1873-1876 (2006)

    • L. Negadi, J. Gmehling
      Azeotropic and Heats of Mixing Data for Several Binary Organic Systems Containing 1-Methoxy-2-propanol and 2-Butoxy-1-ethanol
      J. Chem. Eng. Data 51, 1122-1125 (2006)

    • A. Jakob, H. Grensemann, J. Lohmann, J. Gmehling
      Further Development of the Group Contribution Model Modified UNIFAC (Dortmund)
      Ind. Eng. Chem. Res. 45, 7924-7933 (2006)

    • P. Marchi, G. Scalabrin, E. C. Ihmels, K. Fischer, J. Gmehling
      PρTx-Measurements for (1,1,1,2-Tetrafluoroethane + Triethylene Glycol Dimethyl Ether) at High Haloalkane Content
      J. Chem. Eng. Data 51, 992-996 (2006)

    • J. Kiepe, O. Noll, J. Gmehling
      Modified LIQUAC and Modified LIFAC - A Further Development of Electrolyte Models for the Reliable Prediction of Phase Equilibria with Strong Electrolytes
      Ind. Eng. Chem. Res. 45, 2361-2373 (2006)

    • M. T. Sanz, J. Gmehling
      Study of the dehydration of Iso-Propanol by Pervaporation-Based Hybrid Process
      Chem. Eng. Technol. 29(4) 473-480 (2006)

    • E. C. Ihmels, J. T. Safarov, E. Hassel, J. Gmehling
      (p, ρ, T) properties and apparent molar volumes VF of CaCl2 in methanol at T=(298.15 to 398.15) K and pressures up to 40 MPa
      J. Chem. Thermodyn. 38, 224-229 (2006)

    2005


    • K.-J. Han, S.-J. Park, J. Gmehling
      Excess Molar Volumes and Viscosity Deviations for the Ternary System N,N-Dimethylformamide plus N-Methylformamide plus Water and the binary Sub-systems
      J. Chem. Eng. Data 50, 1951-1955 (2005)

    • S. Steinigeweg, J. Gmehling
      Recent advances in thermal separation processes
      Bunri Gijutsu (Journal of Separation Process Engineering, Japan), 35(4) 14-22 (2005)

    • E. C. Ihmels, J. Safarov, E. Hassel, J. Gmehling
      (p, r, T) properties, and apparent molar volumes VF of ZnBr2 in methanol at T=(298.15 to 398.15) K and pressures up to p = 40 MPa
      J. Chem. Thermodyn. 37, 1318-1326 (2005)

    • R. Kato, J. Gmehling
      Systems With Ionic Liquids: Measurement of VLE and γ∞ Data and Prediction of Their Thermodynamic Behavior Using original UNIFAC, mod. UNIFAC(Do) and COSMO-RS(Ol)
      J. Chem. Thermodyn. 37, 603-619 (2005)

    • R. Kato, J. Gmehling
      Measurement and Correlation of Vapor-Liquid Equilibria of Binary Systems Containing the Ionic Liquids [EMIM][(CF3SO2)2N], [BMIM][(CF3SO2)2N], [MMIM][(CH3)2PO4] and Oxygenated Organic Compounds Respectively Water
      Fluid Phase Equilib. 231, 38-43 (2005)

    • E. Collinet, J. Gmehling
      Activity Coefficients at Infinite Dilution, Azeotropic Data, Excess Enthalpies and Solid-Liquid Equilibria for Binary Systems of Alkanes or Aromatics with Esters
      Fluid Phase Equilib. 230, 131-142 (2005)

    • S. Steinigeweg, J. Gmehling
      Green Separation Processes
      Editors: C.A.M. Afonso, J.P.S.G. Crespo
      Chapter 3.2, Distillation, p. 127-154 Wiley, New York 2005

    • T. Yamaguchi, J. Rarey, J. Ahlers, J. Gmehling
      Approaches for the Development of a Universal Group Contribution Equation of State Proceedings of the 7th Asian Thermophysical Properties Conference, August 23-28,
      2004, Hefei & Huangshan, China

    • E. C. Ihmels, K. Fischer, J. Gmehling
      Thermodynamic Properties of the Butenes, Part I. Experimental Densities, Vapor Pressures, and Critical Constants
      Fluid Phase Equilib.228-229,155-171 (2005)

    • H. Grensemann, J. Gmehling
      Performance of the COSMO-RS Model in Comparison to Classical Group Contribution
      Methods, Ind. Eng. Chem. Res. 44, 1610-1624 (2005)

    • M. Döker, J. Gmehling
      Measurement and Prediction of Vapor-Liquid Equilibria of Ternary Systems Containing Ionic Liquids
      Fluid Phase Equilib. 227, 255-266 (2005)

    • S. Horstmann, A. Jabłoniec, J. Krafczyk, K. Fischer, J. Gmehling
      PSRK group contribution equation of state: comprehensive revision and extension IV, including critical constants and a-function parameters for 1000 components
      Fluid Phase Equilib. 227, 157-164 (2005)

    • Jiding Li, Y, Lin, J. Gmehling
      A gE model for single and mixed solvent electrolyte systems
      3. Prediction of solid-liquid equilibria for aqueous electrolyte systems
      Ind. Eng. Chem. Res. 44, 1602-1609 (2005)

    • T. Sanz, J. Gmehling
      Isothermal Vapor-Liquid Equilibrium, Excess Enthalpy Data and Activity Coefficients at Infinite Dilution for the Binary System Water + Methyl Lactate
      J. Chem. Eng, Data 50, 85-88 (2005)

    • S. Horstmann, K. Fischer, J. Gmehling
      Application of PSRK for Process Design
      Chem. Eng. Commun. 192, 336-350 (2005)

    2004


    • R. Kato, J. Gmehling
      Activity Coefficients at Infinite Dilution of Various Solutes in the Ionic Liquids [MMIM]+ [CH3SO4]-, [MMIM]+ [CH3OC2H4SO4]-, [MMIM]+ [(CH3)2PO4]-, [C5H5NC2H5]+ [(CF3SO2)2N]-and [C5H5NH]+ [C2H5OC2H4OSO3]-
      Fluid Phase Equilib. 226, 37-44 (2004)

    • Z. Atik, D. Gruber, M. Krummen, J. Gmehling
      Measurement of Activity Coefficients at Infinite Dilution of Benzene, Toluene, Ethanol, Esters, Ketones, and Ethers at Various Temperatures in Water Using the Dilutor Technique
      J. Chem. Eng. Data 49, 1429-1432 (2004)

    • R. Kato, M. Krummen, J. Gmehling
      Measurement and Correlation of Vapor-Liquid Equilibria and Excess Enthalpies of Binary Systems Containing Ionic Liquids and Hydrocarbons
      Fluid Phase Equilib. 225, 47-54 (2004)

    • J. Gmehling, J. Menke, J. Krafczyk, K. Fischer, J.-C. Fontaine, and H. V. Kehiaian
      Azeotropic Data for Binary Mixtures, p. 6-180-6-200?, CRC Press, Boca Raton 2004

    • J. Ahlers, T. Yamaguchi, J. Gmehling
      Development of a Universal Group Contribution Equation of State
      5. Prediction of the Solubility of High Boiling Compounds in Supercritical Gases with the Group Contribution Equation of State VTPR
      Ind. Eng. Chem. Res. 43, 6569-6576 (2004)

    • S. Horstmann, H. Gardeler, M. Wilken, K. Fischer, J. Gmehling
      Isothermal Vapor-Liquid-Liquid Equilibrium and Excess Enthalpy Data for the Binary Systems Water + 1,2-Ethanediol and Propene + Acetophenone
      J. Chem. Eng. Data 49, 1508-1511 (2004)

    • S. Horstmann, M. Wilken, K. Fischer, J. Gmehling
      Isothermal Vapor-Liquid-Liquid Equilibrium and Excess Enthalpy Data for the Binary Systems Propylene Oxide + 2-Methylpentane and Difluoromethane (R32) + Pentafluoroethane (R125)
      J. Chem. Eng. Data 49, 1504-1507 (2004)

    • S. Horstmann, K. Fischer, J. Gmehling
      Isothermal Vapor-Liquid Equilibrium and Excess Enthalpy Data for the Binary Systems Water + Sulfolane and Methanol + N-Methyl-2-Pyrrolidone (NMP)
      J. Chem. Eng. Data 49, 1499-1503 (2004)

    • S. Horstmann, K. Fischer, J. Gmehling
      Vapor-Liquid-Liquid Equilibria, Azeotropic, and Excess Enthalpy Data for the Binary System n-Undecane + Propionamide, and Pure Component Vapor Pressure and Density Data for Propionamide
      J. Chem. Eng. Data 49, 1494-1498 (2004)

    • Min Li, Li-Sheng Wang, J. Gmehling
      A modified mixing rule for the PSRK model and application for the prediction of vapor-liquid equilibria of polymer solutions
      Chinese J. Chem. Eng. 12. 454-457 (2004)

    • J. Gmehling
      Ionic Liquids in Separation Processes
      Chemical Thermodynamics for Industry, p. 76-87
      Editor T. Letcher
      The Royal Society of Chemistry, Cambridge 2004

    • J. Kiepe, S. Horstmann, K. Fischer, J. Gmehling
      Application of the PSRK Model for Systems Containing Strong Electrolytes
      Ind. Eng. Chem. Res. 43, 6607-6615 (2004)

    • M. C. Rose, J. Kiepe, J. Gmehling
      Experimental Determination and Prediction of Phase Equilibria in Systems Containing Strong Electrolytes
      Deutsche Forschungsgemeinschaft Research Report "Thermodynamic Properties of Complex Fluid Mixtures", 208-240. Wiley-VCH, Weinheim 2004

    • R. Sidi-Boumedine, S. Horstmann, K. Fischer, E. Provost, W. Fürst, J. Gmehling
      Experimental Determination of Hydrogen Sulfide Solubility Data in Aqueous Alkanolamine Solutions
      Fluid Phase Equilibria 218, 149-155 (2004)

    • R. Sidi-Boumedine, S. Horstmann, K. Fischer, E. Provost, W. Fürst, J. Gmehling
      Experimental Determination of Carbon Dioxide Solubility Data in Aqueous Alkanolamine Solutions
      Fluid Phase Equilibria 218, 85-94 (2004)

    • S. Steinigeweg, J. Gmehling
      Transesterification Processes by Combination of Reactive Distillation and Pervaporation
      Chemical Engineerimg and Processing 43, 447-456 (2004)

    • H. Gardeler, J. Gmehling
      Experimental Determination of Phase Equilibria and Comprehensive Examination of the Predictive Capabilities of Group Contribution Equations of State with a View to the Synthesis of Supercritical Extraction Processes
      Supercritical Fluids as Solvents and Reaction Media, p. 1-38, Editor G. Brunner, Elsevier, Amsterdam 2004

    • K. Fischer, J. Gmehling
      Influence of Water on the Vapor-Liquid Equilibria, Activity Coefficients at Infinite Dilution and Heats of Mixing for Mixtures of N-Methylpyrrolidone-2 with C5 or C6 Hydrocarbons
      Fluid Phase Equilibria 218, 69-76 (2004)

    • M. Krummen, J. Gmehling
      Measurement of Activity Coefficients at Infinite Dilution in N-Methylpyrrolidone and N-Formylmorpholine and their Mixtures with Water Using the Dilutor Technique
      Fluid Phase Equilib. 215, 283-294 (2004)

    • T. Pöpken, J. Gmehling
      A Simple and Reliable Method for Determining the Location of Distillation Border Planes in Quaternary Systems
      Ind. Eng. Chem. Research 43, 777-783 (2004)
    • 2003

      • J. Kiepe, S. Horstmann, K. Fischer, J. Gmehling
        Experimental Determination and Prediction of Gas Solubility Data for Methane + Water Solutions Containing Different Monovalent Electrolytes
        Ind. Eng. Chem. Res. 42, 5392-5398 (2003)

      • L.-S. Wang, J. Ahlers, J. Gmehling
        Development of a Universal Group Contribution Equation of State: IV Prediction of Vapor-Liquid Equilibria of Polymer Solutions with the Volume Translated Group Contribution Equation of State
        Ind. Eng. Chem. Research 42, 6205-6211 (2003)

      • J. Gmehling, J. Ahlers
        Group Contribution Methods - Ideal Tools for the Development of Chemical Processes Proceedings of the International Symposium on Molecular Thermodynamics and Molecular Simulation MTMS '03, Sendai/Japan, May 27-30, 2003

      • J. Kiepe, A. K. de Araujo Rodrigues, S. Horstmann, J. Gmehling
        Experimental Determination and Correlation of Liquid Density Data of Electrolyte Mixtures Containing Water or Methanol
        Ind. Eng. Chem. Res. 42, 2022-2029 (2003)

      • J. Kiepe, S. Horstmann, J. Gmehling
        Experimental Determination and Prediction of Gas Solubility Data for CO2 + H2O Mixtures Containing NaNO3 or KNO3
        Ind. Eng. Chem. Res. 42, 3851-3856 (2003)

      • S. Steinigeweg, J. Gmehling
        Esterification of a Fatty Acid by Reactive Distillation
        Ind: Eng. Chem. Res. 42, 3612-3619 (2003)

      • J. Gmehling
        Potential of Group Contribution Methods for the Prediction of Phase Equilibria and Excess Properties of Complex Mixtures
        Pure Appl. Chem. 75(7) 875-888 (2003)

      • K. Fischer, M. Wilken, J. Gmehling
        The Effect of Gas Pressure on the Melting Behavior of Compounds
        Fluid Phase. Equilib. 210, 161-173 (2003)

      • J. Gmehling
        Potential of Thermodynamic Tools ( Group Contribution Methods, Factual Data Banks ) for the Development of Chemical Processes
        Fluid Phase. Equilib. 210, 161-173 (2003)

      • E. C. Ihmels, E. W. Lemmon, J. Gmehling
        An Equation of State and Compressed Liquid and Supercritical Densities for Sulfur Dioxide
        Fluid Phase Equilib. 207 (1-2), 111-130 (2003)

      • E. C. Ihmels, J. Gmehling
        Extension and Revision of the Group Contribution Method GCVOL for the Prediction of Liquid Densities
        Ind. Eng. Chem. Res. 42, 408-412 (2003)

      • M. Teodorescu, M. Wilken, M. Krummen, J. Gmehling
        Azeotropic and solid-liquid equilibrium data for several binary organic systems containing one acetal compound
        Fluid Phase Equilib. 204, 267-280 (2003)

      • M. Teodorescu, M. Krummen, J. Gmehling
        Excess Molar Enthalpies for the Binary Systems of Benzene or Cyclohexane with 1,1-Diethoxyethane at 323.15 K or with 2,2-Dimethoxybutane at 303.15 K and infinite Dilution Activity Coefficients in 1,1-Diethoxyethane
        J. Chem. Eng. Data 48, 435-439 (2003)

      • R. Wittig, J. Lohmann, J. Gmehling
        Prediction of Phase Equilibria and Excess Properties for Systems Containing Sulfones Using the Group Contribution Method modified UNIFAC (Dortmund)
        AIChE J. 49(2), 530-537 (2003)

      • R. Wittig, J. Lohmann, J. Gmehling
        Vapor-Liquid Equilibria by UNIFAC Group Contribution. 6. Revision and Extension
        Ind. Eng. Chem. Res. 42, 183-188 (2003)

      • R. A. Harris, R. Wittig, J. Gmehling, T.M. Letcher, D. Ramjugernath, J.D. Raal
        Vapor-Liquid Equilibria for Four Binary Systems at 363.15 K: N-Methylformamide + Hexane, + Benzene, + Chlorobenzene and + Acetonitrile
        J. Chem. Eng. Data 48, 341-343 (2003)

      2002


      • J. Gmehling, S. Steinigeweg
        Thermodynamik: Vom brennenden Eis und Chemieanlagen Einblicke - Forschungsmagazin der Carl von Ossietzky
        Universität Oldenburg 36, 24-28 (2002)

      • E. C. Ihmels, J. Gmehling
        Liquid Densities of g-Butyrolactone and N-Methyl-2-Pyrrolidone (NMP) from 273 to 473 K and Pressures up to 40 MPa
        J. Chem. Eng. Data 47, 1547-1552 (2002)

      • J. Ahlers, J. Gmehling
        Development of an Universal Group Contribution Equation of State: III Prediction of Vapor-Liquid Equilibria, Excess Enthalpies and Activity Coefficients at Infinite Dilution with the VTPR Model
        Ind. Eng. Chem. Research 41, 5890-5899 (2002)

      • S. Horstmann, P. Mougin, F. Lecomte, K. Fischer, J. Gmehling
        Phase Equilibrium and Excess Enthalpy Data for the System Methanol + 2,2'-Diethanolamine + Water
        J. Chem. Eng. Data 47, 1496-1501 (2002)

      • E. C. Ihmels, J. Gmehling
        Liquid Densities and Excess Volumes of Diisopropyl Ether (DIPE) + 1-Butanol Mixtures from 273 to 473 K at Pressures up to 35 MPa
        J. Chem. Eng. Data 47, 1314-1319 (2002)

      • E. C. Ihmels, J. Gmehling
        Compressed Liquid Densities of Methyl tert-Butyl Ether ( MTBE), Ethyl tert-Butyl Ether (ETBE), and Diisopropyl Ether (DIPE)
        J. Chem. Eng. Data 47, 1307-1313 (2002)

      • J. Gmehling
        Moderne thermodynamische Modelle und Dortmunder Datenbank
        Vakuum in Forschung und Praxis 14(5) 272-279 (2002).
      • M. Wilken, K. Fischer, J. Gmehling
        Transitiometry: PVT-modulated Calorimetry for the simultaneous determination of caloric and mechanical thermophysical properties
        Chem.Eng.Technol. 25, 779-784 (2002)

      • M. Krummen, P. Wasserscheid, J. Gmehling
        Measurement of Activity Coefficients at Infinite Dilution in Ionic Liquids Using the Dilutor Technique
        J. Chem. Eng. Data 47, 1411-1417 (2002)

      • J. Kiepe, S. Horstmann, K. Fischer, J. Gmehling
        Experimental Determination and Prediction of Gas Solubility Data for CO2 + H2O Mixtures Containing NaCl or KCl at Temperatures between 313 and 393 K and Pressures up to 10 MPa
        Ind. Eng. Chem. Res. 41, 4393-4398 (2002)

      • S. Steinigeweg, J. Gmehling
        n-Butyl Acetate Synthesis via Reactive Distillation: Thermodynamic Aspects, Reaction Kinetics, Pilot Plant Experiments and Simulation Studies
        Ind. Eng. Chem. Research 41, 5483-5490 (2002)

      • So-Jin Park, Kyu-Jin Han, J. Gmehling
        Vapor-Liquid Equilibria and Excess Properties for Methyl tert-butyl ether (MTBE) Containing Binary Systems
        Fluid Phase Equilib. 200, 399-409 (2002)

      • J. Ahlers, J. Gmehling
        Development of an Universal Group Contribution Equation of State - II. Prediction of Vapor-Liquid Equilibria for Asymmetric Systems
        Ind. Eng. Chem. Research 41, 3489-3498 (2002)

      • M. Krummen, T. M. Letcher, J. Gmehling
        Measurement of Activity Coefficients at Infinite Dilution Using Gas-Liquid Chromatography. 13. Results for Various Solutes with the Stationary Phases 1-Ethyl-pyrrolidin-2-one and 1,5-Dimethyl-pyrrolidin-2-one
        J. Chem. Eng. Data 47, 906-910 (2002)

      • S. Horstmann, K. Fischer, J. Gmehling
        Measurement and Calculation of Critical Points for Binary and Ternary Mixtures
        AIChE J. 48(10), 2350-2356 (2002)

      • H. Gardeler, K. Fischer, J. Gmehling
        Experimental Determination of Vapor-Liquid Equilibrium Data for Asymmetric Systems
        Ind. Eng. Chem. Res. 41, 1051-1056 (2002)

      • So-Jin Park, Kyu-Jin Han, M.-J. Choi, J. Gmehling
        Isothermal Vapor-Liquid Equilibria and Excess Molar Volumes for the Ternary Mixtures Containing 2-Methyl Pyrazine
        Fluid Phase Equilib. 193, 109-121 (2002)

      • E. C. Ihmels, S. Horstmann, K. Fischer, G. Scalabrin, J. Gmehling
        Compressed Liquid and Supercritical Densities of 1,1,1,2,3,3,3-Heptafluoropropane ( R227ea)
        Int. J. Thermophys. 23, 1571-1585 (2002)

      • J. Gmehling, R. Wittig, J. Lohmann, R. Joh
        A Modified UNIFAC (Dortmund) Model. 4. Revision and Extension
        Ind. Eng. Chem. Res. 41, 1678-1688 (2002)

      • W. Yan, R. Zhang, J. Gmehling
        Measurement and Correlation of Isothermal Vapor-Liquid Equilibrium Data for the System Tetrahydrofuran + Methanol + Lithium Bromide
        J. Chem. Eng. Data 47, 482-486 (2002)

      • E. Christian Ihmels, J. Gmehling
        Desities of Sulfur Hexafluoride and Dinitrogen Monoxide over a Wide Temperature and Pressure Range in the Sub- and Supercritical State
        Int. J. Thermophys. 23, 709-743 (2002)

      • J. Chen, K. Fischer, J. Gmehling
        Modification of PSRK mixing rules and results for vapor-liquid equilibria, enthalpy of mixing and activity coefficients at infinite dilution
        Fluid Phase Equilib. 200, 411-429 (2002)

      • K. Fischer, J. Chen, M. Petri, J. Gmehling
        Solubility of H2S and CO2 in N-Octylpyrrolidone-2 and of H2S in methanol and benzene
        AIChE J. 48(4) 887-893 (2002)

      2001


      • W. Yan, M. Topphoff, J. Gmehling
        Measurement and Correlation of Isothermal Vapor-Liquid Equilibrium Data for the System Ethanol + i-Propanol + Barium Iodide
        J. Chem. Eng. Data 46, 1623-1626 (2001)

      • L. Becker, J. Gmehling
        Measurement of Heat Capacities for Twelve Organic Substances by Tian-Calvet Calorimetry
        J. Chem. Eng. Data 46, 1638-1642 (2001)

      • J. Gmehling, S. Steinigeweg, T. Pöpken
        Letter to the Editor, about "Multiple Steady States in Distillation: Effect of VL(L)E Inaccuracies" by N. Bekiaris, T. E. Güttinger, M. Morari ( AIChE J. 46, 955-979 (2000))
        AIChE J. 47, 2848-2849 (2001)

      • K. Fischer, O. Noll, J. Gmehling
        Experimental Determination of thr Oxygen Solubility in Benzene
        J. Chem. Eng. Data 46, 1504-1505 (2001)

      • R. Wittig, D. Constantinescu, J. Gmehling
        Binary Solid-Liquid Equilibria of Organic Systems Containing e-Caprolactone
        J. Chem. Eng. Data 46, 1490-1493 (2001)

      • R. Wittig, J. Lohmann, R. Joh, S. Horstmann, J. Gmehling
        Vapor-Liquid Equilibria and Enthalpies of Mixing in a Temperature Range from 298.15 K to 413.15 K for the Further Development of Modified UNIFAC (Dortmund)
        Ind. Eng. Chem. Res. 40, 5831-5838 (2001)

      • J. Ahlers, J. Gmehling
        Development of an Universal Group Contribution Equation of State - I. Prediction of Liquid Densities for Pure Compounds with a Volume Translated Peng-Robinson Equation of State
        Fluid Phase Equilib. 191, 177-188 (2001)

      • D. Constantinescu, R. Wittig, J. Gmehling
        Azeotropic and Heats of Mixing Data for Various Binary Systems with Diethoxymethane
        Fluid Phase Equilib. 191, 99-109 (2001)

      • J. Gmehling, J. Lohmann
        Letter to the Editor, about "Analysis of the Molecular Interactions of Organic Anhydride + Alkane Binary Mixtures Using the Nitta-Chao Model" by L. Lugo, E.R. López, J. Garcia, M.J.P. Comunas, J. Fernández ( Fluid Phase Equilib. 170, 69-85 (2000))
        Fluid Phase Equilib. 189, 193-195 (2001)

      • S. Horstmann, J. Gmehling
        Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System Propionic Aldehyde + 2-Methyl-2-Butanol at 333.15 K
        J. Chem. Eng. Data 46, 1487-1489 (2001)

      • M. Wilken, K. Fischer, J. Gmehling
        Transitiometrie: PVT-modulierte Kalorimetrie zur simultanen Bestimmung thermischer und mechanischer Stoffeigenschaften
        Chem.-Ing.-Tech. 73, 1300-1306 (2001)

      • M. Topphoff, J. Kiepe, J. Gmehling
        Effects of Lithium Nitrate on the Vapor-Liquid Equilibria of Methyl Acetate + Methanol and Ethyl Acetate + Ethanol
        J. Chem. Eng. Data 46, 1333-1337 (2001)

      • E. C. Ihmels, J. Gmehling
        Densities of Toluene, Carbon Dioxide, Carbonyl Sulfide, and Hydrogen Sulfide over a Wide Temperature and Pressure Range in the Sub- and Supercritical State
        Ind. Eng. Chem. Res. 40, 4470-4477 (2001)

      • A. del Rio, S. Horstmann, J. A. R. Renuncio, J. Gmehling
        Isothermal Vapor-Liquid Equilibrium and Excess Enthalpy Data for the Binary Systems Methyl tert-Butyl Ether + Cyclohexane and Ethyl tert-Butyl Ether + Cyclohexane, n-Hexane, and n-Heptane in a Temperature Range from 298.15 to 393.15 K
        J. Chem. Eng. Data 46, 1181-1187 (2001)

      • I. Shulgin, K. Fischer, O. Noll, J. Gmehling
        Classification of Homogeneous Binary Azeotropes
        Ind. Eng. Chem. Res. 40, 2742-2747 (2001)

      • Z. Atik, J. Ahlers, J. Lohmann, J. Gmehling
        Binary Solid-Liquid Equilibria of N,N-Dimethylacetamide with 1,2-Dichloroethane, Dichloromethane, and 1-Propanol,
        J. Chem. Eng. Data 1190-1192 (2001)

      • Jiding Li, M. Topphoff, K. Fischer, J. Gmehling
        Prediction of Gas Solubilities in Aqueous Electrolyte Systems Using the PSRK Model
        Ind. Eng. Chem. Res. 40, 3703-3710 (2001)

      • T. Pöpken, S. Steinigeweg, J. Gmehling
        Synthesis and Hydrolysis of Methyl Acetate by Reactive Distillation Using Structured Catalytic Packings: Experiments and Simulation
        Ind. Eng. Chem. Research 40, 1566-1574 (2001)

      • S. Horstmann, T. Pöpken, J. Gmehling
        Phase Equilibria and Excess Properties for Binary Systems in Reactive Distillation Processes.
        Part I: Methyl Acetate Synthesis
        Fluid Phase Equilib. 180, 221-234 (2001)

      • J. Lohmann, J. Gmehling
        Solid-Liquid Equilibria for Seven Binary Systems
        J. Chem. Eng. Data 46, 333-336 (2001)

      • J. Lohmann, R. Bölts, J. Gmehling
        Excess Enthalpy Data for Seven Binary Systems at Temperatures Between 50 and 140 °C
        J. Chem. Eng. Data 46, 208-211 (2001)

      • S. Horstmann, K. Fischer, J. Gmehling
        Experimental Determination of Critical Data of Mixtures and their Relevance for the Development of Thermodynamic Models
        Chem. Eng. Sci. 56, 6905-6913 (2001)

      • S. Horstmann, H. Gardeler, K. Fischer, F. Köster, J. Gmehling
        Vapor Pressure, Vapor-Liquid Equilibrium, and Excess Enthalpy Data for Compounds and Binary Subsystems on the Chlorohydrin Process for Propylen Oxide Production
        J. Chem. Eng. Data 46, 337-345 (2001)

      • J. Lohmann, J. Gmehling
        Modified UNIFAC ( Dortmund ) - A Reliable Model with a Large Range of Applicabilities of Industrial Interest
        J. Chem. Eng. Jpn. 34, 43-54 (2001)

      • J. Lohmann, J. Gmehling
        From UNIFAC to Modified UNIFAC ( Dortmund )
        Ind. Eng. Chem. Res. 40, 957-964 (2001)

      • J. Gmehling, S. Steinigeweg, T. Pöpken
        Comments on "Optimization of a Wastewater System Containing the Ternary Homogeneous Azeotropic System Ethyl Acetate-Ethanol-Water"
        Ind. Eng. Chem. Res. 40, 492-493 (2001)

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