Jürgen Gmehling
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German chemist
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Jürgen Gmehlingchemistry Degrees
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Chemistry
Jürgen Gmehling's Degrees
- PhD Chemistry University of Oldenburg
Why Is Jürgen Gmehling Influential?
(Suggest an Edit or Addition)According to Wikipedia, Jürgen Gmehling is a retired German professor of technical and industrial chemistry at the Carl von Ossietzky University of Oldenburg. Biography His career started with an apprenticeship as a laboratory assistant at the Duisburg copper works before he studied chemical engineering at the engineering school in Essen and then chemistry in Dortmund and Clausthal. He received his diploma from the University of Dortmund in 1970 and his PhD in 1973. After this he worked as a scientific coworker in Dortmund before he became a private lecturer and, after his habilitation, an assistant professor.
Jürgen Gmehling's Published Works
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Total number of citations to an author for the works they published in a given year. This highlights publication of the most important work(s) by the author
Published Works
- Vapor-Liquid Equilibrium Data Collection (1977) (893)
- PSRK: A Group Contribution Equation of State Based on UNIFAC (1991) (553)
- Measurement of Activity Coefficients at Infinite Dilution in Ionic Liquids Using the Dilutor Technique (2002) (344)
- 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) (2005) (334)
- Reaction Kinetics and Chemical Equilibrium of Homogeneously and Heterogeneously Catalyzed Acetic Acid Esterification with Methanol and Methyl Acetate Hydrolysis (2000) (293)
- A Modified UNIFAC (Dortmund) Model. 3. Revision and Extension (1998) (262)
- Vapor-liquid Equilibria Using Unifac: A Group-Contribution Method (2012) (251)
- Computerized Design of Multicomponent Distillation Columns Using the UNIFAC Group Contribution Method for Calculation of Activity Coefficients (1977) (218)
- Chemical Thermodynamics for Process Simulation (2012) (207)
- Determination of new asog parameters (1990) (206)
- Measurement and correlation of vapor–liquid equilibria and excess enthalpies of binary systems containing ionic liquids and hydrocarbons (2004) (181)
- A Modified UNIFAC (Dortmund) Model. 4. Revision and Extension (2002) (160)
- 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 (2002) (159)
- Vapor-liquid equilibrium data collection. Aqueous-organic systems (1977) (159)
- Development of an universal group contribution equation of state (2001) (147)
- Performance of a Conductor-Like Screening Model for Real Solvents Model in Comparison to Classical Group Contribution Methods (2005) (146)
- 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]− (2004) (145)
- Solid-Liquid Equilibria Using UNIFAC (1978) (144)
- Esterification of a Fatty Acid by Reactive Distillation (2003) (132)
- Further Development of Modified UNIFAC (Dortmund): Revision and Extension 5 (2006) (129)
- A gE model for single and mixed solvent electrolyte systems: 1. Model and results for strong electrolytes (1994) (127)
- Measurement of Activity Coefficients at Infinite Dilution in Solvent Mixtures Using the Dilutor Technique (2000) (127)
- 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 (2005) (125)
- Measurement of heat capacities of ionic liquids by differential scanning calorimetry (2006) (124)
- n-Butyl Acetate Synthesis via Reactive Distillation: Thermodynamic Aspects, Reaction Kinetics, Pilot-Plant Experiments, and Simulation Studies (2002) (123)
- Measurement and prediction of vapor–liquid equilibria of ternary systems containing ionic liquids (2005) (121)
- Experimental determination of carbon dioxide solubility data in aqueous alkanolamine solutions (2004) (118)
- Densities of Toluene, Carbon Dioxide, Carbonyl Sulfide, and Hydrogen Sulfide over a Wide Temperature and Pressure Range in the Sub- and Supercritical State (2001) (118)
- Transesterification processes by combination of reactive distillation and pervaporation (2004) (118)
- 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 Phases (1997) (114)
- Prediction of vapor-liquid equilibria in mixed-solvent electrolyte systems using the group contribution concept (1999) (111)
- PSRK group contribution equation of state: comprehensive revision and extension IV, including critical constants and α-function parameters for 1000 components (2005) (108)
- Reactive Distillation (2000) (108)
- Synthesis of Distillation Processes Using Thermodynamic Models and the Dortmund Data Bank (1998) (103)
- 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 modified UNIFAC (Dortmund) (2007) (100)
- Further development, status and results of the PSRK method for the prediction of vapor-liquid equilibria and gas solubilities☆ (1995) (100)
- Extension and revision of the group contribution method GCVOL for the prediction of pure compound liquid densities (2003) (99)
- Activity Coefficients at Infinite Dilution (1994) (95)
- From UNIFAC to Modified UNIFAC (Dortmund) (2001) (93)
- Synthesis and Hydrolysis of Methyl Acetate by Reactive Distillation Using Structured Catalytic Packings: Experiments and Simulation (2001) (93)
- P-x and γ∞ data for the different binary butanol-water systems at 50 °C (1994) (91)
- Solid-liquid equilibria in binary mixtures of organic compounds (1995) (86)
- Development of a Universal Group Contribution Equation of State. 2. Prediction of Vapor-Liquid Equilibria for Asymmetric Systems (2002) (85)
- Measurement and prediction of solubilities of active pharmaceutical ingredients. (2010) (83)
- Present status and potential of group contribution methods for process development (2009) (81)
- Heats of mixing data collection (1984) (79)
- Solubilities of NaCl, KCl, LiCl, and LiBr in Methanol, Ethanol, Acetone, and Mixed Solvents and Correlation Using the LIQUAC Model (2010) (76)
- Further Development of Modified UNIFAC (Dortmund): Revision and Extension 6 (2016) (73)
- Modification of PSRK mixing rules and results for vapor-liquid equilibria, enthalpy of mixing and activity coefficients at infinite dilution (2002) (73)
- Experimental Determination and Prediction of Gas Solubility Data for Methane + Water Solutions Containing Different Monovalent Electrolytes (2003) (71)
- Measurement and prediction of activity coefficients at infinite dilution (γ∞), vapor–liquid equilibria (VLE) and excess enthalpies (HE) of binary systems with 1,1-dialkyl-pyrrolidinium bis(trifluoromethylsulfonyl)imide using mod. UNIFAC (Dortmund) (2009) (71)
- PSRK group contribution equation of state: revision and extension III (2000) (71)
- Review of thermophysical property measurements on mixtures containing MTBE, TAME, and other ethers with non-polar solvents (1999) (69)
- Vapor Pressures of Methyl tert-Butyl Ether, Ethyl tert-Butyl Ether, Isopropyl tert-Butyl Ether, tert-Amyl Methyl Ether, and tert-Amyl Ethyl Ether (1994) (65)
- Prediction of phase equilibria and excess properties for systems with ionic liquids using modified U (2011) (64)
- Development of a Universal Group Contribution Equation of State III. Prediction of Vapor−Liquid Equilibria, Excess Enthalpies, and Activity Coefficients at Infinite Dilution with the VTPR Model (2002) (63)
- Esterification of acetic acid with isopropanol coupled with pervaporation: Part I: Kinetics and pervaporation studies (2006) (60)
- Esterification of Ethylene Glycol with Acetic Acid Catalyzed by Amberlyst 36 (2008) (60)
- Experimental determination of hydrogen sulfide solubility data in aqueous alkanolamine solutions (2004) (58)
- Thermodynamic properties of ethanol + water. I. Vapour-liquid equilibria measurements from 90 to 150°C by the static method (1985) (57)
- Esterification of acetic acid with isopropanol coupled with pervaporation: Part II. Study of a pervaporation reactor (2006) (56)
- Performance of COSMO-RS with Sigma Profiles from Different Model Chemistries (2007) (55)
- Further development of the PSRK model for the prediction of gas solubilities and vapor-liquid -equilibria at low and high pressures II (1997) (55)
- Influence of ionic liquids on the separation factor of three standard separation problems (2009) (55)
- From UNIFAC to modified UNIFAC to PSRK with the help of DDB (1995) (55)
- Present status of the modified UNIFAC model for the prediction of phase equilibria and excess enthalpies for systems with ionic liquids (2014) (55)
- Experimental and predicted phase equilibria and excess properties for systems with ionic liquids (2008) (50)
- Prediction of vapor–liquid equilibria for asymmetric systems at low and high pressures with the PSRK model (1998) (48)
- Measurements of different thermodynamic properties of systems containing ionic liquids and correlation of these properties using modified UNIFAC (Dortmund) (2010) (48)
- A revised LIQUAC and LIFAC model (LIQUAC*/LIFAC*) for the prediction of properties of electrolyte containing solutions (2013) (48)
- Revised parameters and typical results of the VTPR group contribution equation of state (2012) (48)
- Solubility Calculation of Active Pharmaceutical Ingredients in Alkanes, Alcohols, Water and their Mixtures Using Various Activity Coefficient Models (2011) (48)
- Experimental Determination of Vapor−Liquid Equilibrium Data for Asymmetric Systems (2002) (47)
- Experimental determination of the critical line for (carbon dioxide + ethane) and calculation of various thermodynamic properties for (carbon dioxide + n-alkane) using the PSRK model (2000) (46)
- (Vapour + liquid) equilibria of ternary systems with ionic liquids using headspace gas chromatography (2010) (46)
- The Dortmund Data Bank: A computerized system for retrieval, correlation, and prediction of thermodynamic properties of mixtures (1989) (45)
- Modified LIQUAC and Modified LIFACA Further Development of Electrolyte Models for the Reliable Prediction of Phase Equilibria with Strong Electrolytes (2006) (45)
- Vapor-Liquid Equilibria by UNIFAC Group Contribution, Revision and Extension 2 (1979) (45)
- Vapor–liquid equilibria and excess properties for methyl tert-butyl ether (MTBE) containing binary systems (2002) (44)
- Present status of group-contribution methods for the synthesis and design of chemical processes (1998) (43)
- Group contribution prediction of surface charge density profiles for COSMO‐RS(Ol) (2007) (42)
- Excess Molar Volumes and Viscosity Deviations for the Ternary System N,N-Dimethylformamide + N-Methylformamide + Water and the Binary Subsystems at 298.15 K (2005) (42)
- A data bank for azeotropic data — status and applications (1995) (41)
- Selection of Solvents or Solvent Mixtures for Liquid–Liquid Extraction Using Predictive Thermodynamic Models or Access to the Dortmund Data Bank (2014) (41)
- 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 Volume-Translated Peng−Robinson (2004) (41)
- Vapor−Liquid Equilibria and Vapor Pressure Data for the Systems Ethyl tert-Butyl Ether + Ethanol and Ethyl tert-Butyl Ether + Water (1999) (40)
- Measurement and prediction of binary adsorption equilibria of vapors on dealuminated Y-zeolites (DAY) (1998) (40)
- Measurement of activity coefficients at infinite dilution in N-methyl-2-pyrrolidone and N-formylmorpholine and their mixtures with water using the dilutor technique (2004) (38)
- Modified UNIFAC (Dortmund): Reliable Model for the Development of Thermal Separation Processes (2001) (37)
- Selection of entrainers for the separation of the binary azeotropic system methanol + dimethyl carbo (2011) (37)
- Comparison of the a Priori COSMO-RS Models and Group Contribution Methods: Original UNIFAC, Modified UNIFAC(Do), and Modified UNIFAC(Do) Consortium (2012) (37)
- Effects of Lithium Nitrate on the Vapor−Liquid Equilibria of Methyl Acetate + Methanol and Ethyl Acetate + Ethanol (2001) (36)
- High-temperature liquid chromatography. Part III: Determination of the static permittivities of pure solvents and binary solvent mixtures--implications for liquid chromatographic separations. (2009) (36)
- Measurement of Activity Coefficients at Infinite Dilution of Benzene, Toluene, Ethanol, Esters, Ketones, and Ethers at Various Temperatures in Water Using the Dilutor Technique (2004) (36)
- Prediction of Gas Solubilities in Aqueous Electrolyte Systems Using the Predictive Soave−Redlich−Kwong Model (2001) (36)
- Measurement and correlation of biodiesel densities at pressures up to 130 MPa (2013) (35)
- Prediction of octanol‐water partition coefficients, Henry coefficients and water solubilities using UNIFAC (1998) (35)
- Improvement of the SRK equation of state for representing volumetric properties of petroleum fluids using Dortmund Data Bank (1999) (33)
- Group Contribution Methods for Phase Equilibrium Calculations. (2015) (33)
- Experimental determination of critical data of mixtures and their relevance for the development of thermodynamic models (2001) (33)
- An equation of state for the description of phase equilibria and caloric quantities on the basis of the “chemical theory” (1986) (33)
- A comparison of the predictive capability of different group contribution methods (1990) (32)
- Densities of Sulfur Hexafluoride and Dinitrogen Monoxide over a Wide Temperature and Pressure Range in the Sub- and Supercritical States (2002) (32)
- Measurement of Activity Coefficients at Infinite Dilution Using Gas−Liquid Chromatography. 6. Results for Systems Exhibiting Gas−Liquid Interface Adsorption with 1-Octanol (1997) (32)
- The effect of gas pressure on the melting behavior of compounds (2003) (32)
- Prediction of liquid heat capacities by the group contribution equation of state VTPR (2006) (31)
- Activity coefficients at infinite dilution of alkanes and alkenes in 1-alkyl-3-methylimidazolium tetrafluoroborate (2009) (31)
- 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 (1996) (31)
- A gE model for single and mixed solvent electrolyte systems: 2. Results and comparison with other models (1994) (29)
- Experimental determination and correlation of liquid density data of electrolyte mixtures containing water or methanol (2003) (29)
- Binary Solid−Liquid Equilibria of Organic Systems Containing Different Amides and Sulfolane (1999) (28)
- Extension of the VTPR Group Contribution Equation of State: Group Interaction Parameters for Additional 192 Group Combinations and Typical Results (2014) (28)
- Aqueous-organic systems (1977) (28)
- Application of the PSRK Model for Systems Containing Strong Electrolytes (2004) (28)
- High-temperature liquid chromatography. Part II: Determination of the viscosities of binary solvent mixtures--implications for liquid chromatographic separations. (2009) (27)
- Experimental determination and calculation of gas solubility data for nitrogen in different solvents (2007) (27)
- From van der Waals to VTPR: The systematic improvement of the van der Waals equation of state (2010) (26)
- Solubility of H2S and CO2 in N‐octyl‐2‐pyrrolidone and of H2S in methanol and benzene (2002) (25)
- Solid−Liquid Equilibria for Different Heptanones with Benzene, Cyclohexane, and Ethanol (1996) (24)
- Estimation of Pure-Component Properties of Biodiesel-Related Components: Fatty Acid Methyl Esters, Fatty Acids, and Triglycerides (2013) (24)
- Group contribution methods for the estimation of activity coefficients (1986) (23)
- Phase Equilibrium and Excess Enthalpy Data for the System Methanol + 2,2‘-Diethanolamine + Water (2002) (23)
- Prediction of solubilities of salts, osmotic coefficients and vapor–liquid equilibria for single and mixed solvent electrolyte systems using the LIQUAC model (2009) (23)
- Measurement of Heat Capacities for Nine Organic Substances by Tian−Calvet Calorimetry (2000) (23)
- Prediction of gas solubilities by a modified UNIFAC equation (1983) (22)
- Isothermal phase equilibria and excess molar enthalpies for binary systems with dimethyl ether at 323.15 K (2007) (22)
- Vapor-liquid equilibria and enthalpies of mixing in a temperature range from 298.15 to 413.15 K for the further development of Modified UNIFAC (Dortmund) (2001) (22)
- Prediction of phase equilibria with strong electrolytes with the help of the volume translated Peng-Robinson group contribution equation of state (VTPR) (2006) (21)
- Potential of group contribution methods for the prediction of phase equilibria and excess properties of complex mixtures (2003) (21)
- Solid−Liquid Equilibria of Viscous Binary Mixtures with Alcohols (1997) (21)
- Experimental determination of critical points of pure components and binary mixtures using a flow apparatus (1999) (21)
- Vapor–liquid equilibria of ternary systems with 1-ethyl-3-methylimidazolium ethyl sulfate using headspace gas chromatography (2011) (21)
- Vapor−Liquid Equilibria and Enthalpies of Mixing for the Binary System Water + N-Methyl-2-pyrrolidone in the Temperature Range 80−140 °C (1996) (20)
- Solubility and density measurements of palmitic acid in supercritical carbon dioxide + alcohol mixtures (2010) (20)
- Prediction of different thermodynamic properties for systems of alcohols and sulfate-based anion Ionic Liquids using modified UNIFAC (2013) (20)
- Thermodynamics of Phase Equilibria in Aqueous Strong Electrolyte Systems (2011) (20)
- Binary Solid−Liquid Equilibria of Organic Systems Containing ε-Caprolactone (2001) (19)
- Influence of sulfate-based anion ionic liquids on the separation factor of the binary azeotropic system acetone + methanol (2013) (19)
- The universal group contribution equation of state VTPR present status and potential for process development (2011) (19)
- (Vapour + liquid + liquid) equilibria and excess molar enthalpies of binary and ternary mixtures of isopropanol, water, and propylene (2008) (19)
- Joule–Thomson coefficients and Joule–Thomson inversion curves for pure compounds and binary systems predicted with the group contribution equation of state VTPR (2011) (19)
- Results of a modified unifac method for alkane-alcohol systems (1986) (19)
- Measurement of Activity Coefficients at Infinite Dilution Using Gas−Liquid Chromatography. 10. Results for Various Solutes with the Stationary Phases Dimethyl Sulfoxide, Propylene Carbonate, and N-Ethylformamide (1999) (19)
- Simple Method for Determining the Location of Distillation Region Boundaries in Quaternary Systems (2004) (19)
- Correlation of binary liquid-liquid equilibrium data over a wide temperature range using UNIQUAC and extended UNIQUAC models (1991) (19)
- Group contribution methods–ideal tools for the synthesis and design of separation processes (1999) (18)
- Guidelines for reporting of phase equilibrium measurements (IUPAC Recommendations 2012) (2012) (18)
- Compressed Liquid Densities of Methyl tert-Butyl Ether (MTBE), Ethyl tert-Butyl Ether (ETBE), and Diisopropyl Ether (DIPE) (2002) (18)
- 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 (2007) (18)
- Phase equilibria and excess properties for binary systems in reactive distillation processes: Part I. Methyl acetate synthesis (2014) (18)
- Prediction of phase equilibria and excess properties for systems with sulfones (2003) (18)
- Potential of thermodynamic tools (group contribution methods, factual data banks) for the development of chemical processes (2003) (18)
- Prediction of Gas Solubilities by a Modified UNIFAC-Equation (1983) (18)
- Development of a Universal Group Contribution Equation of State. 4. Prediction of Vapor−Liquid Equilibria of Polymer Solutions with the Volume Translated Group Contribution Equation of State (2003) (18)
- Generalized LIQUAC model for the single‐ and mixed‐solvent strong electrolyte systems (2011) (18)
- Improvement of SRK equation of state for vapor‐liquid equilibria of petroleum fluids (1999) (17)
- Activity coefficient at infinite dilution, azeotropic data, excess enthalpies and solid–liquid-equilibria for binary systems of alkanes and aromatics with esters (2005) (17)
- Phase equilibria for benzene–cyclohexene and activity coefficients at infinite dilution for the ternary systems with ionic liquids (2010) (17)
- Measurement of Activity Coefficients at Infinite Dilution Using Gas−Liquid Chromatography. 12. Results for Various Solutes with the Stationary Phases N-Ethylacetamide, N,N-Diethylacetamide, Diethylphthalate, and Glutaronitrile (2000) (17)
- A lead-207 and carbon-13 Fourier-transform nuclear magnetic resonance study of organolead compounds (1978) (17)
- gE Model for Single- and Mixed-Solvent Electrolyte Systems. 3. Prediction of Salt Solubilities in Aqueous Electrolyte Systems (2005) (17)
- Measurement of Activity Coefficients at Infinite Dilution Using Gas−Liquid Chromatography. 9. Results for Various Solutes with the Stationary Phases 2-Pyrrolidone and N-Methylformamide (1998) (16)
- Factual data banks and their application to the synthesis and design of chemical processes and the development and testing of thermophysical property estimation methods (2009) (16)
- Group contribution prediction of surface charge density distribution of molecules for COSMO-SAC (2009) (16)
- Measurements of activity coefficients at infinite dilution in vegetable oils and capric acid using the dilutor technique (2014) (16)
- Measurement of the thermodynamic properties for the reactive system ethylene glycol–acetic acid (2007) (16)
- Measurement of Thermophysical Pure Component Properties for a Few Siloxanes Used as Working Fluids for Organic Rankine Cycles (2011) (16)
- Study of the dehydration of isopropanol by a pervaporation- based hybrid process (2006) (16)
- Excess Enthalpies for Various Binary Mixtures with N-Methylacetamide or Acetic Anhydride (1996) (15)
- Measurement of Activity Coefficients at Infinite Dilution Using Gas−Liquid Chromatography. 7. Results for Various Solutes with N-Methyl-2-piperidone as Stationary Phase (1998) (15)
- Classification of Homogeneous Binary Azeotropes (2001) (15)
- Thermodynamic properties of ethanol + water II. Potentials and limits of GE models (1985) (15)
- Measurement and calculation of critical points for binary and ternary mixtures (2002) (15)
- The Determination of Activity Coefficients at Infinite Dilution with the Help of the Dilutor Technique (Inert Gas Stripping) (1999) (15)
- Solid−Liquid Equilibria for Seven Binary Systems (2001) (14)
- Liquid Densities and Excess Volumes of Diisopropyl Ether (DIPE) + 1-Butanol Mixtures from 273 to 473 K and Pressures up to 35 MPa (2002) (14)
- Present status of the group contribution equation of state VTPR and typical applications for process development (2016) (14)
- (Vapour + liquid) equilibria, (VLE) excess molar enthalpies and infinite dilution activity coefficients of selected binary systems involving n-hexyl pyridinium bis(trifluoromethylsulphonyl)imide ionic liquid: Experimental and predictions using modified UNIFAC (Dortmund) (2015) (14)
- Various Thermodynamic Properties for Binary Systems with Tertiary Ethers (1999) (14)
- Phase equilibria and excess properties for binary systems in reactive distillation processes (2001) (14)
- Dortmund data bank-basis for the development of prediction methods (1985) (14)
- Solid−Liquid Equilibria of Several Binary Systems with Organic Compounds (1998) (13)
- Thermodynamic properties of the butenes: Part I. Experimental densities, vapor pressures, and critical points (2005) (13)
- Erratum to Activity coefficients at infinite dilution of various solutes in the ionic liquids [MMIM (2005) (12)
- Isothermal P, x data and excess enthalpies for two binary systems : Experimental project results from the Design Institute for Physical Property Data (DIPPR) of the American Institute of Chemical Engineers. 3 (1999) (12)
- Status and results of group contribution methods (1993) (12)
- Measurement and Correlation of Isobaric Vapor−Liquid Equilibrium Data for the System Acetone + Methanol + Zinc Chloride (1999) (12)
- Revision and extension of the group contribution method modified UNIFAC (Dortmund) (1998) (12)
- Software Development In Chemistry 5 (1991) (12)
- Computer‐Controlled Vibrating Tube Densimeter for Liquid Density Measurement in a Wide Temperature and Pressure Range (2000) (12)
- Determination of ASOG Parameters-Extension and Revision (2011) (11)
- 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 (2001) (11)
- Development of Thermodynamic Models with a View to the Synthesis and Design of Separation Processes (1991) (11)
- Model and experimental data research of natural gas storage for vehicular usage (1997) (11)
- Experimental Determination and Prediction of Gas Solubility Data for CO2 + H2O Mixtures Containing NaNO3 or KNO3 (2003) (11)
- High pressure solid–solid and solid–liquid transition data for long chain alkanes (2008) (11)
- Isothermal Vapor−Liquid Equilibrium and Excess Enthalpy Data for the Binary Systems Propylene Oxide + 2-Methylpentane and Difluoromethane (R32) + Pentafluoroethane (R125)† (2004) (11)
- Measurement, correlation and prediction of isothermal vapor–liquid equilibria of different systems containing vegetable oils (2015) (11)
- The solid–liquid equilibrium of the binary system H2O–DMSO and the influence of a salt (NaCl, KCl) on the thermodynamic behavior: Correlations using a revised LIQUAC model (2011) (11)
- Isothermal Vapor−Liquid Equilibrium and Excess Enthalpy Data for the Binary Systems Water + Sulfolane and Methanol + N-Methyl-2-pyrrolidone† (2004) (11)
- Analysis of polyethylene glycols with respect to their oligomer distribution by high-performance liquid chromatography (1993) (11)
- Isothermal Vapor−Liquid Equilibrium and Excess Enthalpy Data for the Binary Systems Water + 1,2-Ethanediol and Propene + Acetophenone† (2004) (11)
- Isothermal Vapor−Liquid Equilibrium and Excess Enthalpy Data for the Binary Systems Diethyl Ether + Ethyl tert-Butyl Ether, 1-Pentene + Methyl Acetate, and Propene + 2-Propanol (1999) (11)
- Excess Enthalpy Data for Seven Binary Systems at Temperatures between 50 and 140 °C (2001) (10)
- Thermodynamic properties of ethanol and water— III. Description of the different excess functions (gE, hE, cEP) using an empirical model (1988) (10)
- Estimation of Enthalpies of Fusion, Melting Temperatures, Enthalpies of Transition, and Transition Temperatures of Pure Compounds from Experimental Binary Solid−Liquid Equilibrium Data of Eutectic Systems (1997) (10)
- Isothermal vapor–liquid equilibria for different binary mixtures involved in the alcoholic distillation (2008) (10)
- Vapor Pressure, Vapor−Liquid Equilibrium, and Excess Enthalpy Data for Compounds and Binary Subsystems of the Chlorohydrin Process for Propylene Oxide Production (2001) (10)
- Vapor-liquid equilibria and enthalpies of mixing for binary mixtures of N-methylacetamide with aniline, decane, ethylene glycol, naphthalene, phenol, and water (1997) (10)
- Vapour–liquid equilibria, azeotropic data, excess enthalpies, activity coefficients at infinite dilution and solid–liquid equilibria for binary alcohol–ketone systems (2008) (9)
- Measurement of Activity Coefficients at Infinite Dilution Using Gas−Liquid Chromatography. 11. Results for Various Solutes with the Stationary Phases ε-Caprolactone and Ethyl Benzoate (2000) (9)
- Liquid densities of THF and excess volumes for the mixture with water in a wide temperature and pressure range (2010) (9)
- Experimental and Theoretical Study of Chemical Equilibria in the Reactive Systems of Acetals Synthesis (2012) (9)
- Vapor−Liquid Equilibria for Four Binary Systems at 363.15 K: N-Methylformamide + Hexane, + Benzene, + Chlorobenzene, and + Acetonitrile (2003) (9)
- Organic hydroxy compounds : alcohols (1977) (9)
- Vapor-Liquid Equilibria and Excess Enthalpies for Octane + N-Methylacetamide, Cyclooctane + N-Methylacetamide, and Octane + Acetic Anhydride at 125 .degree.C (1995) (9)
- Liquid densities of acetone and n-heptane and excess volumes of the binary system in a wide temperat (2011) (9)
- Measurement and correlation of isothermal vapor-liquid equilibrium data for the system acetone + methanol + lithium bromide (1998) (9)
- Eine Übersicht zuer Berechnung von Phasengleichgewichte mit Hilfe der UNIFAC-Methode:A SURVEY OF THE CALCULATION OF PHASE-EQUILIBRIA WITH THE AID OF THE UNIFAC-METHOD (1980) (9)
- Vapor−Liquid Equilibria at 413.65 K and Excess Enthalpies at 323.15, 363.15, and 413.15 K for Mixtures of Benzene, Toluene, Phenol, and Benzaldehyde (1998) (9)
- Vapor−Liquid Equilibria and Excess Enthalpy Data for the Binary Systems 2-Methyltetrahydrofuran with 2,2,4-Trimethylpentane (Isooctane), Ethanol, Toluene, Cyclohexane, and Methylcyclohexane§ (1999) (9)
- Separation of Enantiomers by Liquid‐Liquid Counter Current Chromatography (1998) (8)
- Recommended NRTL Model Parameters by Simultaneous Correlation of VLE, Infinite Dilution Activity Coefficients and Excess Enthalpy Data (2009) (8)
- Azeotropic and solid–liquid equilibria data for several binary organic systems containing one acetal compound (2003) (8)
- Experimental and predicted properties of the binary mixtures containing an isomeric chlorobutane and butyl ethyl ether (2012) (8)
- 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† (2004) (8)
- Experimental measurement and modeling of solubility of LiBr and LiNO3 in methanol, ethanol, 1-propanol, 2-propanol and 1-butanol (2011) (8)
- Vapor−Liquid Equilibria and Excess Enthalpies for Binary Mixtures of Acrylonitrile with Hexane, Cyclohexane, Benzene, Toluene, 2-Butanone, and Acetonitrile (1996) (8)
- Measurement of Transport Properties for Selected Siloxanes and Their Mixtures Used as Working Fluids for Organic Rankine Cycles (2011) (7)
- Vapor-liquid equilibria for the system water + tert.-pentanol at 4 temperatures (1996) (7)
- Application of PSRK for Process Design (2005) (7)
- Bubble pressure measurements for the (1,1,1,2-tetrafluoroethane + triethylene glycol dimethyl ether) system (2006) (7)
- Review of Thermophysical Property Measurements on Mixtures Containing MTBE, TAME, and Other Ethers with Non‐Polar Solvents (1999) (7)
- Isothermal vapor-liquid equilibrium data for the ethanol + ethyl acetate + sodium iodide system at five temperatures (1997) (7)
- Analysis of a concept for predicting missing group interaction parameters of the UNIFAC model using connectivity indices (2009) (7)
- Liquid Densities of γ-Butyrolactone and N-Methyl-2-pyrrolidone from 273 to 473 K and at Pressures up to 40 MPa (2002) (7)
- Thermodynamics of reformulated automotive fuels (1995) (7)
- Measurement of Activity Coefficients at Infinite Dilution Using Gas−Liquid Chromatography. 13. Results for Various Solutes with the Stationary Phases 1-Ethylpyrrolidin-2-one and 1,5-Dimethylpyrrolidin-2-one (2002) (7)
- Isothermal vapour–liquid equilibria and excess enthalpies for the binary mixtures containing an isomeric chlorobutane and diisopropyl ether (2011) (6)
- Vapor−Liquid Equilibria and Excess Enthalpy Data for the Binary Systems Benzene + Benzonitrile and Toluene + Benzonitrile Covering the Temperature Range from 323.15 to 413.15 K (1999) (6)
- (p, ρ, T) properties and apparent molar volumes Vϕ of CaCl2 in methanol at T = (298.15 to 398.15) K and pressure up to 40 MPa (2005) (6)
- Isothermal Vapor−Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene) (2009) (6)
- Rebuttal to the Comments of Andreas Klamt on “Performance of a COSMO-RS Model in Comparison to Classical Group Contribution Methods” (2005) (6)
- PρTx Measurements for (1,1,1,2-Tetrafluoroethane + Triethylene Glycol Dimethyl Ether) at High Haloalkane Content (2006) (6)
- Ionic liquids in separation processes (2004) (6)
- Transitiometry: PVT – Scanning Calorimetry for the Simultaneous Determination of Thermal and Mechanical Properties (2002) (5)
- Isothermal Vapor−Liquid Equilibrium Data for the Acetone + Methanol + Lithium Nitrate System (1998) (5)
- Solid−Liquid Equilibria for Binary Organic Systems Containing 1-Methoxy-2-propanol and 2-Butoxy Ethanol (2006) (5)
- Vapor−Liquid Equilibria at 453.25 K and Excess Enthalpies at 363.15 K and 413.15 K for Mixtures of Benzene, Toluene, Phenol, Benzaldehyde, and Benzyl Alcohol with Benzyl Benzoate (1999) (5)
- Reaction Kinetics and Reactive Distillation – On the Transfer of Kinetic Data from a Batch Reactor to a Trickle‐bed Reactor (1999) (5)
- 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 (2010) (5)
- Azeotropic and heats of mixing data for various binary systems with diethoxymethane (2001) (5)
- Isothermal vapor–liquid equilibria and excess molar volumes for the ternary mixtures containing 2-methyl pyrazine (2002) (5)
- Prevalence of diabetes and impact on cardiovascular events and mortality in patients with chronic coronary syndromes, across multiple geographical regions and ethnicities. (2021) (5)
- Limitations of modern expressions for the excess Gibbs energy (1983) (5)
- High-temperature liquid chromatography. Part I. Determination of the vapour pressures of binary solvent mixtures--implications for liquid chromatographic separations. (2009) (5)
- Vapor–Liquid Equilibrium and Physical Properties for Distillation (2014) (5)
- Isothermal vapor-liquid equilibrium, excess enthalpy data, and activity coefficients at infinite dilution for the binary system water + methyl lactate (2005) (5)
- Carboxylic acids, anhydrides, esters (1982) (5)
- Measurement and prediction of ternary solid-liquid equilibria (1997) (4)
- Ebulliometric determination and prediction of (vapor + liquid) equilibria for binary and ternary mixtures containing alcohols (C1–C4) and dimethyl carbonate (2012) (4)
- Binary Solid−Liquid Equilibria of N,N-Dimethylacetamide with 1,2-Dichloroethane, Dichloromethane, and 1-Propanol (2001) (4)
- Erratum to “High pressure solid–solid and solid–liquid transition data for long chain alkanes [J. Chem. Thermodyn. 40 (2008) 1632–1637]” (2009) (4)
- Comparison of the startup of reactive distillation in packed and tray towers (2006) (4)
- Experimental Determination of the Oxygen Solubility in Benzene (2001) (4)
- Countercurrent Liquid/Liquid Chromatography. A Reliable Method for the Determination of Partition Coefficients. (1993) (4)
- Application of a modified Wilson equation to liquid mixtures showing phase splitting (1980) (4)
- Measurement of Thermodynamic Properties for the System Sulfur Hexafluoride + Water (1999) (4)
- Excess enthalpies for pseudobinary mixtures containing vegetable oils at the temperatures 298.15 K, 353.15 K and 383.15 K (2014) (4)
- Simultaneous Prediction of Densities and Vapor–Liquid Equilibria of Mixtures Containing an Isomeric Chlorobutane and Methyl tert-Butyl Ether Using the VTPR Model (2011) (4)
- Vapor−Liquid Equilibrium Data, Excess Enthalpy Data, and Azeotropic Data for the Binary System Dibutyl Ether + o-Xylene (2010) (4)
- GUIDELINES FOR REPORTING OF PHASE EQUILIBRIUM MEASUREMENTS (2011) (4)
- Isothermal vapor–liquid equilibria at 383.15–413.15 K for the binary system methanol + dimethyl carbonate and the pressure dependency of the azeotropic point (2019) (4)
- Excess molar enthalpies of (fluorobenzene or trifluoromethylbenzene or iodoethane + methanol or toluene) at the temperature 313.15 K and pressure 0.7 MPa (1993) (4)
- Simultaneous correlation of excess gibbs energy and excess enthalpy data using the extended uniquac model (1991) (3)
- VAPOR-LIQUID EQUILIBRIUM FOR MIXTURE OF LOW BOILING SUBSTANCES (1986) (3)
- Addendum to “Further Development of Modified UNIFAC (Dortmund): Revision and Extension 6” (2017) (3)
- Measurement and Correlation of Isothermal Vapor−Liquid Equilibrium Data for the System Ethanol + 2-Propanol + Barium Iodide (2001) (3)
- Carboxylic acids, anhydrides (2002) (2)
- Vapor−Liquid Equilibria and Excess Enthalpies for Binary Mixtures of N-Methylacetamide with 1-Octene, Dipropylamine, Triethylamine, Pyridine, and Methanol at 125 °C (1997) (2)
- Azeotropic and Heats of Mixing Data for Several Binary Organic Systems Containing 1-Methoxy-2-propanol and 2-Butoxy Ethanol (2006) (2)
- Comments on “Pure and Multicomponent Adsorption Equilibrium of Carbon Dioxide, Ethylene and Propane on ZSM-5 Zeolites with Different Si/Al Ratios” (Calleja, G.; Pau, J.; Callas, J. A. J. Chem. Eng. Data 1998, 43, 944−1003) (1999) (2)
- The Performance of EOS Models in the Prediction of Vapor-Liquid Equilibria in Asymmetric Natural Gas Mixtures (1998) (2)
- Chemical Equilibrium Conversion of the tert-Amyl-methyl-ether Synthesis in the Presence of n-Pentane, Tetrahydrofuran, or Benzene (2010) (2)
- Calorimetric and acoustic study of binary mixtures containing an isomeric chlorobutane and butyl ethyl ether or methyl tert-butyl ether (2015) (2)
- Influence of water on the vapor-liquid equilibria, activity coefficients at infinite dilution and enthalpies of mixing for mixtures of N-methyl-2-pyrrolidone with C5 or C6 hydrocarbons (2004) (2)
- Vapor−Liquid Equilibria and Excess Enthalpy Data for the Binary System Propionic Aldehyde + 2-Methyl-2-butanol at 333.15 K (2001) (2)
- Comments on “Optimization of a Wastewater System Containing the Ternary Homogeneous Azeotropic System Ethyl Acetate−Ethanol−Water” (2001) (2)
- Excess enthalpies of (aniline + an alkane or an alkene) at the temperature 363.15 K (1995) (2)
- About “Analysis of the molecular interactions of organic anhydride + alkane binary mixtures using the Nitta–Chao model” by ☆: L. Lugo, E.R. López, J. Garcı́a, M.J.P. Comuñas, J. Fernández [Fluid Phase Equilib. 170 (2000) 69–85] (2001) (2)
- About “New modified UNIFAC parameters using critically evaluated phase equilibrium data” by Jeong Won Kang, Vladimir Diky, Michael Frenkel [Fluid Phase Equilib. 388 (2015) 128-141] (2015) (2)
- (p, ρ, T) properties, and apparent molar volumes Vϕ of ZnBr2 in methanol at T = (298.15 to 398.15) K and pressures up to p = 40 MPa (2005) (1)
- Vapor–Liquid Equilibrium and Excess Enthalpy Data for Systems Containing N,N-Dimethylacetamide (2017) (1)
- Activity Coefficients at Infinite Dilution. Vol. IX, Part 2 (1986) (1)
- Thermodynamic aspects of reformulation of automotive fuels (1995) (1)
- Aldehydes and ketones, ethers (1979) (1)
- Prediction of Mixture Properties Using UNIFAC (1988) (1)
- Measurement and Correlation of Isothermal Vapor−Liquid Equilibrium Data for the System Tetrahydrofuran + Methanol + Lithium Bromide (2002) (1)
- Vapor-Liquid Equilibrium Data Collection, Vol. 1 (1980) (1)
- Prediction of Different Thermodynamic Properties for Systems of Alcohols and Sulfate‐Based Anion Ionic Liquids Using Modified UNIFAC (2014) (1)
- Reply to “Comments on ‘Performance of COSMO-RS with Sigma Profiles from Different Model Chemistries'” (2008) (1)
- Recommended gE-Model Parameters by Simultaneous Fitting of Different Excess Properties (1988) (1)
- Corrigendum to “Measurement and prediction of activity coefficients at infinite dilution (γ∞), vapor–liquid equilibria (VLE) and excess enthalpies (HE) of binary systems with 1,1-dialkyl-pyrrolidinium bis(trifluoromethylsulfonyl)imide using mod. UNIFAC (Dortmund)” [Fluid Phase Equilibr. 277 (2009) 6 (2009) (1)
- Organic hydroxy compounds, alcohols and phenols (1982) (0)
- Vapor-Liquid Equilibrium Data. Physical Sciences Data, 37. Von S. Ohe. Elsevier Science Publishers, Amsterdam – New York 1989. XXX, 742 S., US-$ 260,50. (1990) (0)
- Organic hydroxy compounds : C[5+]-alcohols and phenols (2010) (0)
- EXCESS MOLAR ENTHALPIES OF 1-OCTENE + DIMETHYLCARBONATE OR DIETHYLCARBONATE OR 1,2-PROPYLCARBONATE AT 363.15 K AND 413.15 K (1998) (0)
- 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 (2003) (0)
- Handbook of Heats of Mixing: Supplementary Volume. Von J. J. Christensen, R. L. Rowley und R. M. Izatt. John Wiley & Sons, Chichester ‐‐ New York 1988. XIII, 1145 S., geb., £ 130,–. (1989) (0)
- Thermodynamic models and factual data banks - ideal tools for the development of chemical processes (2011) (0)
- Recent advances in thermal separation processes (特集 My Recent Advance in Separation Technology) (2005) (0)
- Studies in Modem Thermodynamics 7. Liquid‐Liquid Equilibria. Von J.‐P. Novak, J. Matous, J. Pick. Elsevier Science Publishers, Amsterdam – Oxford – New York 1987. 321 S., zahlr. Abb. u. Tab., geb., US‐$ 100,– (1988) (0)
- Buchbesprechung: Physical and Chemical Equilibrium for Chemical Engineers. Von N. De Nevers (2004) (0)
- Direct calculation of SRK parameters from experimental PvT data in the saturation state (1995) (0)
- DDBPC: A Program System for the Management, Correlation and Calculation of Thermodynamic Properties of Pure Components and Mixtures (1991) (0)
- Solubilities and compressed liquid densities of palmitic acid in supercritical carbon dioxide (2007) (0)
- Aqueous-organic systems : tables and diagrams of data for binary and multicomponent mixtures up to moderate pressures ; constants of correlation equations for computer use (1991) (0)
- Gas solubility data bank for further development of phase equilibrium models (1988) (0)
- Halogen, nitrogen, sulfur, and other compounds (1984) (0)
- Chapter 3:Experimental, Calculated and Predicted Solubilities - Basis for the Synthesis and Design of Thermal Separation Processes (2007) (0)
- Software development in chemistry 5 : proceedings of the 5th Workshop "Computers in Chemistry," Oldenburg, November 21-23, 1990 (1991) (0)
- Databank and Software Package for Adsorption Equilibria of Gases and Vapors (1998) (0)
- About Phase equilibria on four binary systems containing 3- methylthiophene by E. Sapei, et al. [Fluid Phase Equilib. 279 (2009)81-86] (2009) (0)
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