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Phase equilibrium measurements and thermodynamic modeling of aqueous solutions of polyamines CO2 absorbents: 3-aminopropylmethylamine, 3-aminopropyldimethylamine and N,N-diethyl 1,3-propanediamine at temperatures from 273 K to 363 K

THERMODYNAMIC PROPERTIES OF BINARY LIQUID MIXTURES OF ETHANE AND ETHYLENE WITH METHANE AND THE RARE GASES

Vapor−Liquid Equilibrium for Dimethyl Disulfide + Butane, +trans-But-2-ene, + 2-Methylpropane, + 2-Methylpropene, + Ethanol, and 2-Ethoxy-2-methylpropane

Isothermal vapour–liquid equilibrium measurements for six binary systems of C4 hydrocarbons + 2-propanone

Effect of surface area parameters on the vapor–liquid equilibrium calculations using a lattice fluid equation of state with hydrogen bonding

Thermodynamics of molecular interactions in 1,2-dibromoethane + benzene or toluene mixtures

Thermodynamics of Liquid Mixtures of Argon and Krypton

Isothermal Vapor–Liquid Equilibria of n-Tetradecane + Ethyl Hexanoate, Ethyl Decanoate, and Ethyl Tetradecanoate

Vapor–liquid equilibria of binary systems composed of polyoxyethylene 4-octylphenyl ether and alcohols: Experimental measurements and correlation

Komplexbildung und Wasserstoffbrückenassoziation von Trimethyl‐ und Methylamin in Tetrachlorkohlenstoff und Hexan (nach Dampfdruckmessungen)

Reduction of total-pressure vapor—liquid equilibrium data. Common pitfalls encountered

Isothermal binary vapour–liquid equilibrium for butanes and butenes with dimethylsulphide

Vapor-Liquid equilibrium for systems comprised of a non-volatile strong electrolyte in a mixed solvent

Isothermal vapour–liquid equilibrium data for the binary propan-2-one+chloroalkanes mixtures at temperatures from 298.15 K to 313.15 K

The significance of the Wilson constants in the theoretical description of vapor pressures over binary mixtures

An Assessment of Thermodynamic Consistency Tests for Vapor-Liquid Equilibrium Data

(Vapor + liquid) equilibrium behavior of (n-pentane + ethanol) at 372.7, 397.7, and 422.6 K

Liquid–vapor equilibria of binary systems containing alcohols (1-butanol, or 2-butanol or 1-hexanol) present in the production by chemical process of 2,5-dimethyl furan from biomass

A new continuous dilution vapor liquid equilibrium apparatus: The activity coefficients of benzene and water in cyclohexane at 50°C

Phase equilibria of strong electrolytes in aqueous solutions from total pressure measurements

Excess Gibbs energies of the ternary system ehtanol + tetrahydrofuran + cyclohexane at 298.15 K

Isothermal v.l.e. and excess molar Gibbs energy of binary and ternary mixtures containing diisopropyl ether,n -heptane and isopropanol at T= 313.15 K

The Effects of Diethyl Carbonate in Light Naphtha Blending to Utilize New Energy Resource

Using the NRTL model with the Vidal equation of state EOS-qE formulation for vapor/liquid equilibrium calculations

Determination of ternary vlle by p(x1,x2) measurements

Vapour pressures and excess Gibbs energies of o-xylene +, m-xylene +, p-xylene +, and isopropylbenzene + carbon tetrachloride at 303.15 K

Excess Gibbs free energy of butyl acetate with cyclohexane and aromatic hydrocarbons at 308.15K

Thermodynamic consistency of vapor‐liquid equilibrium data at high pressure

Isothermal liquid-vapour equilibria 1. The binary systems formed by toluene + methyl ethyl ketone, + methyl propyl ketone, and + methyl isobutyl ketone

Measurements and Correlation of Isobaric Vapor–Liquid Equilibria and the Isothermal Surface Tension of the Methyl Butyrate + Dibutyl Ether Binary Mixture

Vapour—liquid equilibria measurements for some binary mixtures showing partial miscibility

Isothermal Vapor−Liquid Equilibria of (Monoethanolamine + Water) and (4-Methylmorpholine + Water) Binary Systems at Several Temperatures

A new equilibrium cell with variable cell volume for static vapour-pressure measurements

The Thermodynamic Excess Properties of Binary Mixtures: I. Hexanol-1 +o-Xylene

Vapour pressures at several temperatures and excess functions of n-butanol with 2,2-dimethylbutane and with 2,3-dimethylbutane at 298.15 K

Vapor—liquid phase equilibria for the isoprene—n-pentane binary system from 300 to 330 K

Molar excess Gibbs free energy of 1-Propanol or 2-Propanol + aromatic hydrocarbons at 298.15 K in terms of an association model with a Flory contribution term

Thermodynamic behaviour of mixtures containing fluoroalcohols II. (2,2,2-trifluoroethanol + benzene)

Modeling Vapor Pressure Data of Ternary α-Methylstyrene–Toluene–Poly(α-methylstyrene) System

Thermodynamic study of tetrachloromethane or heptane + cycloalkane mixtures

Excess Gibbs free energies at seven temperatures and excess enthalpies and volumes at 298.15 K of butanone with 1-propanol or 2-propanol

Polarographic investigation of the interactions between nitrobenzene radical anions, water and univalent cations in dimethylformamide/water mixtures

Properties of mixed crystalline organic material prepared by zone levelling II. Vapour pressures and excess Gibbs energies of (p-dichlorobenzene + p-dibromobenzene)

Thermodynamics of weak interactions: excess enthalpies and excess Gibbs free energies of mixing

The thermodynamic properties of acetone + cyclohexanol mixtures at 25 °C

An extension of Barker's method for reduction of VLE data

Thermodynamic analysis of vapour-liquid phase diagrams I. Binary systems of nonelectrolytes with complete miscibility; Application of the PXFIT- and the LIQFIT-method

Phase equilibrium and excess Gibbs energy functions of acetophenone with 1,1,2-trichloroethene and cyclohexane binary mixtures by using NRTL, UNIQUAC, UNIFAC and VANLAAR models at a local atmospheric pressure of 95.3kPa

Isothermal vapour–liquid equilibria of binary systems of 1,2-dichloroethane with ethers

Vapor—liquid equilibrium measurements for the n-pentane—methanol—acetone ternary at 372.7 K and their prediction from the constituent binaries

Thermodynamics of aqueous solutions of methyldiethanolamine and diisopropanolamine

Isothermal liquid-vapour equilibria of mixtures containing organic compounds. 3. Excess Gibbs free energies of cyclohexane + a linear ether.

Total vapour pressure and excess Gibbs energy for binary mixtures of 1,1,2,2-tetrachlorethane or tetrachloroethene with cyclohexane at nine temperatures

Excess properties and vapour pressure of (3-diethylaminopropylamine+n-alkanes)

Vapor–liquid equilibrium of octane-enhancing additives in gasolines

Calculation of salt effect on vapor-liquid equilibrium by a new pseudo binary approach

Isothermal Vapor–Liquid Equilibria of Binary Mixtures Containing N,N-Dimethylacetamide with 1,3,5-Trimethylbenzene or Propan-2-ol or Dimethyl Sulfoxide

Vapor−Liquid Equilibria and Interfacial Tensions of the System Ethanol + 2-Methoxy-2-methylpropane

Isothermal vapor–liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions

Excess Properties of Liquid Cyclohexane/Hydrocarbon Mixtures II. Excess Gibbs Energy Determined from Total Vapour Pressure Data

Evaluation and correlation of vapor-liquid equilibria in the ternary system nitrogen-argon-oxygen

Solubilities, Fugacities and All That in Solution Chemistry

Excess Gibbs free energies of some binary mixtures of 1,2-dichloroethane and hydrocarbons

Vapour-liquid equilibria measurements for carbon dioxide with normal and isobutane from 250 to 280 K

Isothermal vapor–liquid equilibria of binary systems containing green solvents derived from biomass: (Furfuryl alcohol+toluene), (furfuryl alcohol+ethanol), or (furfural+toluene)

Total pressure measurements for 1-propanol + 1-pentanol, 1-propanol + 2-pentanol, 2-propanol + 1-pentanol, and 2-propanol + 2-pentanol at 313.15 K

(Vapour + liquid) equilibria of (n-hexane + n-octane + n-hexadecane)

Excess Properties of Binary Mixtures Composed of a Polar Component and an Alkane

Vapour pressures and thermodynamic properties of hexan-1-ol + n-hexane between 298.230 and 342.824 K

Excess molar gibbs free energies of (1,2-dibromoethane+an aromatic hydrocarbon) at 308.15 K

Modeling of Carbon Dioxide Absorption by Aqueous Ammonia Solutions Using the Extended UNIQUAC Model

On the evaluation of the Kirkwood-Buff integrals of aqueous acetone mixtures

Vapor–Liquid Equilibrium Data for the Morpholine-4-carbaldehyde + n-Hexane or n-Heptane Binary Systems Using a Static-Synthetic Apparatus

Reduction of total-pressure vapor-liquid equilibrium data. Comparison of data reduction methods, reliability of γi∞ values, and effect of the equation of state assumed

Prediction of anthracene solubility in alcohol + alkane solvent mixtures using binary alcohol + alkane VLE data. Comparison of Kretschmer-Wiebe and mobile order models

Phase equilibrium properties of binary aqueous solutions containing ethanediamine, 1,2-diaminopropane, 1,3-diaminopropane, or 1,4-diaminobutane at several temperatures

Vapor–liquid equilibria of binary mixtures containing an alcohol and a branched ether. Experimental results and modeling

John Adair Barker 24 March 1925–27 October 1995

GE model independent application of the Gibbs-Helmholtz validation method to P-x data

Vapour pressures and excess Gibbs energies of mixtures of benzene with chlorobenzene, n-hexane, and n-heptane at 25°C

Extended UNIQUAC model for thermodynamic modeling of CO2 absorption in aqueous alkanolamine solutions

Reappraisal of the Vidal equation-of-state formulation for vapor/liquid equilibrium

Excess volumes and gibbs free energies of mixtures containing alkanenitriles

Vapor–Liquid Equilibrium Measurement and Thermodynamic Correlations of 4-Nonyl Phenol Diethoxylate with sec-Butanol at Elevated Pressures

Thermodynamic properties of the n-hexane and benzene system at elevated temperatures

Thermodynamic properties of aqueous solutions of hydrophilic compounds 1. Pyridine and methylpyridines

Isothermal and isobaric vapor–liquid equilibria for the binary system trimethylbenzoquinone + n-hexanol

Vapor-liquid equilibrium data for ethanol-n-heptane-1-propanol and ethanol-n-heptane-2-propanol and their interpretation by a simple association model

Excess molar Gibbs energies of 2-methylpropan-1-ol with benzene or toluene or o- or m- and p-xylene at 308.15 K in terms of an association model

A thermodynamic study of solutions of liquid hydrocarbon mixtures in water

A review of Barker’s activity coefficient method and VLE data reduction

Vapour pressure and thermodynamic properties of dodecan-1-ol + n-hexane between 298.230 and 342.824 K

Vapour pressures and excess Gibbs energies of {pyridine + (methyl- or ethyl- or n-propyl- or n-butyl-benzene)&}; at T = 373.15 K

Isothermal vapor–liquid equilibria and excess Gibbs free energies in some binary nitroalkane+chloroalkane mixtures at temperatures from 298.15K to 318.15K

Coupled optimization and evaluation of phase equilibria and thermodynamic properties of the benzene‐cyclohexane system

Vapor–liquid equilibrium of octane-enhancing additives in gasolines

An Improved Local Composition Expression and Its Implication for Phase Equilibrium Models

Excess thermodynamic properties of binary and ternary mixtures containing methyl 1,1-dimethylethyl ether (MTBE), -heptane, and methanol at= 313.15 K

Berechnung von Dampf/Flüssig‐Gleichgewichtsdaten binärer Gemische aus Dampfdruckdaten

Isothermal vapor–liquid equilibrium and excess molar enthalpies of the binary mixtures furfural+methyl isobutyl ketone, +2-butanol and +2-methyl-2-butanol

A method for multicomponent equilibrium calculations by using dew point pressure‐vapor composition data

Thermodynamic properties of (n-alkoxyethanols + organic solvents). XII. Total vapour pressure measurements for (n-hexane,n-heptane or cyclohexane + 2-methoxyethanol) at different temperatures

Liquid Mixtures of Xenon with Fluorinated Species:  Xenon + Sulfur Hexafluoride

Vapor–liquid equilibrium of octane-enhancing additives in gasolines

Vapour pressures and excess Gibbs energies in mixtures of a pyridine base + 2-propanol, + 2-butanol, + i-butanol, and + t-butanol at 313.15 K

Thermodynamic Modelling of Mdea(Aq)-Nh3(Aq)-K2co3(Aq)-Co2(Aq) Using the Extended Uniquac Model

Vapour pressures at several temperatures of binary mixtures of di‐n‐propylether+2‐methyl‐1‐propanol, +2‐butanol, or +2‐methyl‐2‐propanol, and excess functions, at T= 298.15 K. Thermodynamic description according to the ERAS‐model

Liquid Mixtures Involving Cyclic Molecules. 2:  Xenon + Cyclobutane

Isothermal vapour-liquid equilibrium at eight temperatures and excess functions at 298.15 K of di-n-propylether with 1-propanol or 2-propanol

Excess Properties and Vapor Pressure of 2-Diethylaminoethylamine + n-Heptane

Isothermal Vapor–Liquid Equilibria and Excess Gibbs Energies for Binary Mixtures of Cyclic Ethers with 1,2-Dichloroethane

Vapor pressure isotope effects in the benzene (B)–cyclohexane (C) system from 5 to 80 °C. I. The pure liquids B-d,B-d1,o r t h o-,m e t a-, and p a r a-B-d2, B-d6,C-d, and C-d12. II. Excess free energies and isotope effects on excess free energies in the solutions B-h6/B-d6, C-h12/C-d12, B-h6/C-h12, B-d6/C-h12, and B-h6/C-d12

A New Technique for Studying Vapour–liquid Equilibria of Multi-Component Systems

Vapor–Liquid Equilibrium for the Systems 2-Methylpropane + Methanol, + 2-Propanol, + 2-Butanol, and + 2-Methyl-2-propanol at 364.5 K

Phase Equilibrium Properties of Binary Systems (Furfural + Ethanol or Butan-2-ol) at Several Temperatures

Vapor—liquid equilibrium measurements for the methanol—acetone system at 372.8, 397.7 and 422.6 K

Vapor liquid equilibrium for the binary systems 2-methylpentane + 2-butanol at 329.2 K and n-hexane + 2-butanol at 329.2 and 363.2 K with a static apparatus

Zur Berechnung von Aktivitätskoeffizienten in ternären Systemen mit einer nichtflüchtigen Komponente aus Messungen des Gesamtdampfdruckes

Experimental investigation of the vapour–liquid equilibrium of binary and ternary mixtures containing dibutyl ether (DBE), cyclohexane and toluene at 313.15K

Liquid–Liquid Phase Equilibria of Aqueous Biphasic Systems Based on Glycerol Formal: Application on Tetracycline Recovery from Water

Vapour pressures of (butan-1-ol + hexane) at temperatures between 283.10 K and 323.12 K

Vapor–Liquid Equilibria of Binary Mixtures Containing 2-Butanol and Hydrocarbons at 313.15 K

Excess enthalpies, and vapor-liquid equilibrium and surface properties of the highly non-ideal associated mixtures formed by an alcohol and propanal

Excess Gibbs energies and excess enthalpies of liquid binary mixtures containing nitroalkanes

Thermodynamics of the xenon + methyl chloride system

Vapor–liquid equilibrium data for methanol–water–NaCl at 45°C

Isobaric vapour–liquid equilibria for binary mixtures of n-heptane with bromobenzene, chlorobenzene and fluorobenzene at atmospheric pressure

Thermodynamics of liquid ethylene + xenon at 161.38 K

Vapor−Liquid Equilibrium in the Binary Systems 2-Butanol +tert-Amyl Methyl Ether, 2-Butanol + Heptane, and Heptane +tert-Amyl Methyl Ether

Excess Gibbs free energies, excess enthalpies, and excess volumes for 2,3-dimethylbutane+ cyclo-octane

Excess Gibbs free energy and excess enthalpy for mixtures of benzene and 1,1,2‐trichlorotrifluoroethane

Surface Adsorption in Ternary Surfactant Mixtures above the Critical Micelle Concentration: Effects of Asymmetry on the Composition Dependence of the Excess Free Energy

Isothermal (vapour+liquid) equilibrium for binary mixtures of (tetrahydrofuran+1,1,2,2-tetrachloroethane or tetrachloroethene) at nine temperatures

Vapour pressures and excess functions of 1,4-dimethylpiperazine + n-heptane, or cyclohexane measurement and prediction

Isothermal Vapor–Liquid Equilibrium of Ethanol + Glycerol and 2-Propanol + Glycerol at Different Temperatures

Vapor Pressures and Activity Coefficients of (1-Propanol + 1,8-Cineole) at 10 Temperatures between 278.15 K and 323.15 K

Isothermal vapor-liquid equilibria for binary liquid mixtures of ethylmercaptan and propylmercaptan with some common solvents

Analysis of phase diagrams employing Bayesian excess parameter estimation

Vapor−Liquid Equilibrium for Tetrahydrothiophene + n-Butane, + trans-2-Butene, + 2-Methylpropane, and + 2-Methylpropene

The solvation potential at the interface between water and methanol + water mixtures

Vapour–liquid equilibria of {xCH3F+(1−x)HCl} at temperatures of 159.01K and 182.33K

Isothermal Vapor−Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)

Isothermal vapour-liquid equilibria in cyclohexanone + dichloroalkane binary mixtures at temperatures from 298.15 to 318.15K

Isothermal Vapor−Liquid Equilibrium for Methanol and 2,3-Dimethyl-1-butene at 343.06 K, 353.27 K, 363.19 K, and 372.90 K

Isothermal Vapor–Liquid Equilibrium for Binary Mixtures of Polyoxyethylene Dodecanoate with Methanol, Ethanol, or Propan-2-ol

Ternary systems: A numerical method for calculation of vapor‐liquid equilibrium data from total pressure measurements

Excess Free Energies and Volumes of two Simple Binary Liquid Mixtures: Methane‐Krypton and Nitrogen‐Methane

Vapor–liquid equilibria of two binary mixtures: benzene+n-tetradecane and benzene+squalane

Experimental determination and theoretical modeling of isobaric vapor–liquid equilibria, liquid mass density, surface tension and dynamic viscosity for the methyl butyrate and tert-butanol binary mixture

Determination and correlation of vapor–liquid equilibrium for binary systems consisting of close-boiling components

Experimental Binary Vapor–Liquid Equilibrium Data of Morpholine with Methanol, 1-Propanol, and 2-Ethoxyethanol

Vapour pressures and thermodynamic properties of decan-1-ol + n-hexane between 283.160 and 333.151 K

Isothermal Binary Vapor−Liquid Equilibrium for 2-Methylpropane and n-Butane with 1,2-Ethanedithiol and 2-Methyl-2-propanethiol

Vapour–liquid equilibrium of octane enhancing additives in gasolines 7: Total pressure data and gE for the ternary mixture tert-amyl methyl ether (TAME), methanol and hexane at 313.15K

Measurement and correlation of vapor–liquid equilibra for cyclohexane+ethylene glycol monoisopropyl ether and cyclohexane+ethylene glycol monoisobutyl ether systems

VLE for cryogenic methyl fluoride + nitrous oxide + xenon at 182.33 K

Separation of ethanol – water mixture by extractive distillation using pyridinium-based ionic liquid 1-ethyl-3-methylpyridinium ethylsulfate

Excess enthalpies, excess Gibbs free energies, and excess volumes for (di-n-butyl ether + benzene) and excess Gibbs free energies and excess volumes for (di-n-butyl ether + tetrachloromethane) at 298.15 and 308.15 K

Excess Gibbs energies of liquid binary mixtures.

Isothermal (vapour + liquid) equilibrium at several temperatures of (1-chlorobutane + 1-butanol, or 2-methyl-2-propanol)

Thermodynamics of liquid mixtures of krypton+ethane

Effect of a third component on the interactions in a binary mixture determined from the fluctuation theory of solutions

Vapor-liquid equilibria of strong electrolytes in systems containing mixed solvent

Vapor–Liquid Equilibrium for the Systems trans-2-Butene + Methanol, + 1-Propanol, + 2-Propanol, + 2-Butanol, and + 2-Methyl-2-propanol at 364.5 K

Phase behavior of arbutin/ethanol/supercritical CO2 at elevated pressures

Isobaric vapor–liquid equilibrium and isothermal surface tensions of 2,2′-oxybis[propane]+2,5-Dimethylfuran

Phase equilibria of binary systems containing ethylene carbonate and an aromatic compound

Vapor–liquid equilibrium measurements of dimethylsulfide, +ethanol, +dimethylether, +methylacetate with a static total pressure method

A new apparatus for measuring the vapour pressure of liquid mixtures excess Gibbs free energy of octamethylcyclotetrasiloxane + cyclohexane at 308.15 K

A general method for calculating the excess Gibbs free energy from isothermal vapour-liquid equilibria

Vapour pressures of (n-hexane + an α,ω-dichloroalkane)

Thermodynamics of liquid methane+ethane

Thermodynamics of Fuels with a Biosynthetic Component. II. Vapor–Liquid Equilibrium Data for Binary and Ternary Mixtures Containing Ethyl 1,1-Dimethylethyl Ether, 1-Hexene, and Cyclohexane at T = 313.15 K

Calculation of ternary equilibrium vapor compositions from total vapor pressure‐liquid composition data

Thermodynamic behaviour of fluorocarbon mixtures: excess Gibbs functions and excess volumes of hexafluorobenzene + N,N′-dimethylaniline and + isopropylcyclohexane

Isothermal vapor-liquid equilibria of mixtures containing organic compounds. Part 5: Excess Gibbs energies of dichloromethane or chlorobutane + linear ether or acetal mixtures at 25�C1

Isothermal vapour pressures and excess functions of 3,5- and 2,6-dimethylpyridine with toluene measurement and prediction

Total pressure measurements for benzene with 1-propanol, 2-propanol, 1-pentanol, 3-pentanol, and 2-methyl-2-butanol at 313.15 K

Thermodynamic study of mixtures containing dibromomethane

Vapour—liquid equilibria of the systems acetone—benzene, benzene—cyclohexane and acetone—cyclohexane at 25°C

Solubility of hydrogen in bio-oil compounds

(Vapour + liquid) equilibria of (n-hexane + n-hexadecane), (n-hexane + n-octane), and (n-octane + n-hexadecane)

A comprehensive thermodynamic study of heat stable acetic acid salt of monoethanolamine

(Vapour+liquid) equilibria of {xCH3Cl+(1−x)HCl} at temperatures (159.01 and 182.33) K

Effect of triple‐bond position on thermodynamic properties of mixtures: Phase equilibria for the system acetone‐3‐hexyne

The thermodynamic properties of binary mixtures containing an octane II. Excess Gibbs functions

The thermodynamic excess functions of krypton+ethene liquid mixtures

Vapour pressures and excess Gibbs free energies of (cyclohexanol + n-heptane) between 303.147 and 373.278 K

A versatile thermodynamic consistency test for incomplete phase equilibrium data of high-pressure gas–liquid mixtures

Thermodynamics of binary mixtures containing N-methyl-2-pyrrolidinone

Vapour pressures and excess Gibbs energies of (butan-1-ol + n-octane or n-decane) at 373.15 and 383.15 K

Isobaric Vapor–Liquid Equilibrium of the Binary Mixtures Toluene + Styrene and Styrene + α-Methylstyrene

Dew points of pure DBN and DBU and vapor–liquid equilibria of water+DBN and water+DBU systems for cellulose solvent recycling

Vapour pressures and excess Gibbs energies of {quinoline + (trans-bicyclo[4.4.0]decane or n-decane or n-butylbenzene)} at T = 393.15 K and excess volumes of (quinoline + n-butylbenzene) at T = 298.15 K

Vapour–liquid equilibrium for the systems butane+methanol, +2-propanol, +1-butanol, +2-butanol, +2-methyl-2-propanol at 364.5K

Investigation of the isothermal (vapour+liquid) equilibria of aqueous 2-amino-2-methyl-1-propanol (AMP), N-benzylethanolamine, or 3-dimethylamino-1-propanol solutions at several temperatures

Experimental determination of the isothermal (vapour+liquid) equilibria of binary aqueous solutions of sec-butylamine and cyclohexylamine at several temperatures

Vapour liquid equilibrium with association in both phases

Activity coefficients and excess molar Gibbs energies of (p-xylene + tetrachloromethane)

How Dilute Is the Henry's Law Region? II

Vapour pressures of butan-1-ol with n-hexadecane between 293.18 and 323.18 K. Description of butan-1-ol + n-alkane systems by ERAS model

Isothermal Vapor−Liquid Equilibrium of (1-Butanol + 1,8-Cineole) at 10 Temperatures between (278.15 and 323.15) K

Sugars as hydrogen-bond donors tune the phase behavior in a novel liquid–liquid biphasic system formed by hydrophilic deep eutectic solvents and n-propanol

Ultrasonic absorption in aqueous binary mixtures. II. p-Dioxan–water at 11° and 25 °C

Thermodynamics of associating component + saturated hydrocarbon mixtures at low pressures. II. Extension of the model to correlate isothermal vapour liquid equilibria and volumetric properties of n-alcohol + n-alkane mixtures

The excess Gibbs energy of liquid CH4 + CF4 at 98 K

Thermodynamische Untersuchungen an binären Flüssigkeitsgemischen von Methylchlorid, Methylbromid, Propan

Excess Gibbs free energy and excess volume of methanol + pyridine, + 2-methylpyridine, and + 2,6-dimethylpyridine

The prediction of vapor—liquid equilibrium from heat of mixing data of binary hydrocarbon—ether and hydrocarbon—aldehyde mixtures

The As-Cu-Ni System: A Chemical Thermodynamic Model for Ancient Recycling

Experimental determination and theoretical modeling of the vapor–liquid equilibrium and densities of the binary system butan-2-ol+tetrahydro-2H-pyran

Reanalysis of the Much Referenced Ethanol‐trichloromethane Mixture Vapor Pressure Data: A Discussion of the Principal Association Species Present

Phase equilibrium properties of the ternary mixture dibutyl ether+toluene+heptane at 313.15K

Experimental and Predicted Values of Bubble Point Pressure for Binary and Ternary Systems Consisting of 1-Butanol, 2-Methyl-1-propanol, Glycerol, and Water

Total vapour pressure and excess Gibbs energy for binary mixtures of 1,1,2,2-tetrachlorethane or tetrachloroethene with benzene at nine temperatures

Vapor–liquid equilibria for binary α-pinene + alkanols system

Heat of mixing of R22-absorbent mixtures

Excess Gibbs free energies of di-ethyl ether + hexafluorobenzene and di-isopropyl ether + hexafluorobenzene at 298.131 K

Solute–solute interactions in water. II. An analysis through the Kirkwood–Buff integrals for 14 organic solutes

Total vapour pressure and excess Gibbs energy for binary mixtures of 1,1,2,2-tetrachloroethane or tetrachloroethene with tetrachloromethane at nine temperatures

Vapour pressures and excess functions of N, N, N′, N′-tetramethylalkanediamine + cyclohexane. A group contribution study of the NN proximity effect

Occurrence of a Double Azeotrope in the Binary System Hexafluorobenzene+Benzene

Precision Methods for the Determination of the Solubility of Gases in Liquids

Excess molar Gibbs free energies of ethyl iodide plus aromatic hydrocarbons at 308.15 K

Vapor−Liquid Equilibrium for Methoxymethane + Methyl Formate, Methoxymethane + Hexane, and Methyl Formate + Methanol

Isothermal vapour-liquid equilibria of mixtures of organic compounds

Bulk and surface properties of the highly non-ideal associated mixtures formed by methanol and propanal

Vapor‐Liquid equilibria for five cryogenic mixtures

Thermodynamic behaviour of mixtures containing fluoroalcohols I. (Water + 2,2,2-trifluoroethanol)

Pressions de vapeur et enthalpies libres d'exces de systemes binaires: Hexamethylphosphorotriamide (HMPT) + n-hexane; n-heptane; n-octane: A 298,15 K; 303,15 K; 313,15 K; 323,15 K; 333,15 K

Phase equilibrium properties of binary aqueous solutions of benzylamine, 1,2-bis(2-aminoethoxy)ethane, or 2-[2-(dimethylamino)ethoxy]ethanol

Excess enthalpies, excess volumes, and excess Gibbs free energies for benzene+p-xylene at 288.15, 198.15, 308.15, and 318.15 K

The vapor pressure behavior and association of mixtures of 1-hexanol and n-hexane between 293 and 373 K

The mixing properties of hexafluorobenzene with carbon tetrachloride and with perfluoromethylcyclohexane

A THERMODYNAMIC MODEL OF THE HEAT CAPACITY OF COMPOSITIONALLY COMPLEX MULTICOMPONENT POLYMER SOLUTIONS: KRAFT BLACK LIQUOR

Application of model-free computation techniques and limiting conditions for azeotropy. An additional assessment of experimental data

Vapor-liquid equilibrium thermodynamics of N2 + CH4: Model and Titan applications

Liquid – liquid equilibria in binary and ternary systems of phenol + hydrocarbons (n–dodecane or n–hexadecane) and water + phenol + hydrocarbons (n–dodecane or n–hexadecane) at temperatures between 298K and 353K

Isothermal Vapor + Liquid Equilibrium and Thermophysical Properties for 1-Butyl-3-methylimidazolium Bromide + 1-Butanol Binary System

Vapour-liquid equilibrium and excess molar volume of (trans-1,2-dichloroethene + cyclopentane) at 293.15 K

Computation and thermodynamic interpretation of high-pressure vapour—liquid equilibrium—a review

Measurement and correlation of (vapor + liquid) equilibria for the {2-propoxyethanol (C3E1) +n-hexane} and the {2-propoxyethanol (C3E1) +n-heptane} systems

Topological and Thermodynamic Studies for Binary Mixtures of 1,4-Dioxane with Anilines at 308.15 K

Dampfdruckuntersuchungen an Methyljodid und Trideuteromethyljodid sowie deren Mischungen mit n‐Hexan

Vapour pressure and excess Gibbs free energy of binary mixtures of hydrogen sulphide with ethane, propane, and n-butane at temperature of 182.33K

Equilibre liquide-vapeur isotherme des systèmes hexamethylphosphorotriamide-benzène et hexamethylphosphorotriamide-toluène

(Vapour+liquid) equilibria of {x CH3Cl+(1−x) CH3F} at temperatures of 159.01 K and 182.33 K

Vapour pressures and excess Gibbs energies of cyclohexane + o-xylene, + m-xylene, and + p-xylene

Vapour-liquid equilibrium in systems with association in both phases

Thermodynamic properties of binary mixtures of cyclohexane with cyclic amines or cyclic ethers at 298.15 K

Vapour–liquid equilibria of binary and ternary mixtures containing 1-butanol, 2,2,4-trimethylpentane and 1-hexene at T=313.15K

Vapor–Liquid Equilibria, Excess Enthalpy, and Density of Aqueous γ-Valerolactone Solutions.

Measurement of vapor—liquid equilibrium for binary systems containing polynuclear aromatic compounds

Excess enthalpies, excess volumes, and excess Gibbs free energies for n-hexane + di-n-butyl ether at 298.15 and 308.15 K

Experimental investigation of the vapor–liquid equilibrium at 313.15 K of the ternary system tert-amylmethyl ether (TAME)+n-heptane+methanol

VLE and LLE of perfluoroalkane + alkane mixtures

Vapour–liquid equilibrium for the systems diethyl sulphide+1-butene, +cis-2-butene, +2-methylpropane, +2-methylpropene, +n-butane, +trans-2-butene

Vapour–liquid equilibrium for the 1-butene + methanol, + ethanol, + 2-propanol, + 2-butanol and + 2-methyl-2-propanol systems at 326 K

Thermodynamics of binary mixtures of N-methyl-2-pyrrolidinone and ketone. Experimental results and modelling of the (solid+liquid) equilibrium and the (vapour+liquid) equilibrium. The modified UNIFAC (Do) model characterization

Thermodynamics of the partially miscible {x(CH3)2C(OH)CH2COCH3 + (1 − x)CH3(CH2)4CH3} at temperatures between 288.15 K and 318.15 K

Vapour pressures and excess Gibbs energies of (2-methylpyridine + methylbenzene), (2,4-dimethylpyridine + 1,2-dimethylbenzene), and (2,6-dimethylpyridine + 1,2- or 1,3- or 1,4-dimethylbenzene or ethylbenzene) at T = 373.15 K

Isothermal vapour–liquid equilibrium at several temperatures and excess functions at 298.15 K of butanone with 2-methyl-1-propanol or 2-methyl-2-propanol

P-x isothermal equilibrium data for two ternary systems containing long-chain bioalcohols: (1-butanol or 2-butanol + cyclohexane + methylbenzene) at 313.15 K

Berechnung des Phasengleichgewichts ternärer Gemische aus Dampfdruckmessungen

Infinite dilution activity coefficient and vapour liquid equilibrium measurements for dimethylsulphide and tetrahydrothiophene with hydrocarbons

Vapor–Liquid Equilibrium and Interfacial Tension for the 1-Butanol + Cyclopentyl Methyl Ether Binary Mixture

A model-free method for calculating vapor-liquid equilibria for multicomponent systems from total-pressure or boiling-point data

Thermodynamic properties of binary mixtures of I‐hexyne and polar organic solvents

Vapor–Liquid Equilibria of Binary Mixtures Containing 1-Butanol and Hydrocarbons at 313.15 K

(Vapour + liquid) equilibria of (β- or γ-picoline + a C6 to C9 n-alkane) at 348.15 K

Thermodynamic study of perfluorohexane+ether mixtures

Vapor Pressure Measurements and Predictions for Binary Systems Containing Ethyl Octanoate or Ethyl Dodecanoate as Biodiesels and n-Tetradecane as Petrodiesel Compound

Vapour pressures and excess Gibbs energies of {(3-methylpyridine or 3-ethylpyridine) + (methyl- or ethyl- or propyl- or butyl-benzene)&} at T = 373.15 K

Measurement and Correlation of Isothermal Binary Vapor–Liquid Equilibrium for Diethyl Carbonate + Isooctane/n-Heptane/Toluene Systems

Calculation of multicomponent vapour—liquid equilibrium from liquid boiling temperature data

Prediction of anthracene solubilities in binary alcohol+alcohol solvent mixtures using alcohol-specific mobile order theory stability constants

Excess Gibbs free energies of methylcyclohexane + benzene, + methylbenzene, and + ethylbenzene at 303.15 and 323.15 K

Thermodynamics of binary mixtures containing linear or cyclic alkenes + n-alkanes or cyclohexane

Excess thermodynamic properties for {xCO2 + (1 − x)C2H6} (I): experiment and theory

Vapor–Liquid Equilibria, Density, Sound Velocity, and Refractive Index for Binary Mixtures Containing 2-(2-Ethoxyethoxy)ethanol and 1-Propanol or 2-Propanol or 1-Butanol or 2-Butanol at Different Temperatures

Vapor–Liquid Equilibria and Interfacial Tensions of the System Ethanol + 2-Methoxy-2-methylbutane

Vapour pressures for binary liquid mixtures of methylethylketone with methylene chloride, 1,2-dichloroethane, trichloroethene, tetrachloroethene and cyclohexane

Excess gibbs free energies of mixtures of substances containing nitrogen groups

Excess thermodynamic functions for ternary systems containing fuel oxygenates and substitution hydrocarbons

A geochemical model of non-ideal solutions in the methane–ethane–propane–nitrogen–acetylene system on Titan

Total vapour pressures for binary liquid mixtures of acetone with tetrachloroethylene, trichloroethylene, methylene chloride, 1,2-dichloroethane and cyclohexane at 273.15 K

Thermodynamics of liquid mixtures of xenon and methyl fluoride

Thermodynamic properties of aqueous mixtures of hydrophilic compounds 2. Aminoethanol and its methyl derivatives

Excess Gibbs free energies of (tetrachloromethane + an alcohol or a cyclic ether) at 298.15 K

Experimental measurement of phase equilibria in dilute solutions

Isothermal (p, x, y) relations and activity coefficients for benzene +chlorobenzene, +fluorobenzene, and +thiophene at 348.15 K

Excess properties and vapour pressure of {3-diethylaminopropylamine+cyclohexane}

Calculations of speciation of associated solutions from vapour pressure-composition data

Isothermal Vapor–Liquid Equilibrium Data of Propan-1-ol + 2,2,4-Trimethylpentane and Butan-1-ol + 2,2,4-Trimethylpentane at 318.15 K

Solubility characteristics of R22-DMF refrigerant-absorbent combination

Liquid-vapour equilibria in {xCH2Cl2 + (1 − x)C4H9CH:CH2} at 298.17 K

Low-Pressure Vapor-Liquid Data Reduction Using only Equilibrium Composition Data

Thermodynamic properties of binary and ternary mixtures containing sulfolane VI. Vapour-liquid equilibria for (benzene + sulfolane) and (toluene + sulfolane)

Ultrasonic absorption properties of binary aqueous mixtures

Excess functions of (1-bromobutane + benzene) at various temperatures

Activity coefficients and excess partial molar enthalpies for (ethanol + hexane) from 283 to 318 K

Excess Gibbs free energies of mixtures of tetrakis(2-ethylbutoxy)silane + cyclohexane, + benzene, and + carbon tetrachloride at 308.15 K

Unusual Excess Free Energies of Mixing in Mixtures of Partially Fluorinated and Hydrocarbon Surfactants at the Air–Water Interface: Correlation with the Structure of the Layer

Phase equilibrium properties of binary mixtures containing 1,3-pentanediamine (or 1,5-diamino-2-methylpentane) and water at several temperatures

Vapour-liquid equilibrium in the krypton-xenon system

P—x measurements for ethanol—n-Heptane—isobutanol at 303.15 K

Treatment of binary Vapour-Liquid equilibrium data

PHASE EQUILIBRIA FOR THE N-PENTANE-?beta;METOXIPROPIONITRILE SYSTEM T 37.8 AND 43.3 °C

Calculation of Vapor‐Liquid Equilibrium Data of Binary Mixtures Using Vapor Pressure Data

Experimental determination and theoretical modeling of the vapor–liquid equilibrium and surface tensions of hexane+tetrahydro-2H-pyran

Thermodynamic properties of liquid mixtures containing 1,3-dioxolane and anilines: Excess molar volumes, excess molar enthalpies, excess Gibb's free energy and isentropic compressibilities changes of mixing

Non-ideality of methanol solutions of artificial serum in the mole fraction range from 5 × 10−4 to 5 × 10−3 at 25 °C

Evaluation of parameters for nonlinear thermodynamic models

Thermodynamic consistency testing of PTx-data via the Gibbs-Helmholtz equation 2.: Methodology and limitations

Isothermal vapor–liquid equilibria and excess enthalpies of binary mixtures of propyl ethanoate+1-hexyne, +2-hexyne, +3-hexyne

Neutron reflection and the thermodynamics of the air–water interface

Vapour–liquid equilibrium for the ethyl ethanoate+1-butene, +cis-2-butene, +trans-2-butene, +2-methylpropene, +n-butane and +2-methylpropane

Measurement of phase equilibrium and interfacial tension for the (1-propanol + cyclopentyl methyl ether) binary mixture

Preferential interaction of dimethyl sulfoxide and phosphatidyl choline membranes

Vapour–liquid equilibrium of octane-enhancing additives in gasolines

Isothermal (vapour+liquid) equilibrium at several temperatures of (1-chlorobutane+1-octanol, or 1-decanol)

Excess enthalpies, excess volumes, and excess Gibbs free energies for (n-hexane + n-dodecane) at 298.15 and 308.15 K

Phase Equilibrium Properties of Binary and Ternary Mixtures Containing Dibutyl Ether, Cyclohexane, and Heptane or 1-Hexene at T = 313.15 K

Excess thermodynamic functions for ternary systems containing fuel oxygenates and substitution hydrocarbons. 1. Total-pressure data and GE for methyl tert-butyl etherbenzenecyclohexane at 313.15 K

Vapour–liquid equilibria, enthalpy of mixing of binary mixtures containing diisopropylether ‘DIPE’ and monoaromatic hydrocarbons

Vapour pressures at several temperatures between 288.15 K and 323.15 K of di-n-propylether with 1-hexanol or 1-octanol. Application of the ERAS model

HmE, VmE, and GmE of {xCl2HCCHCl2 + (1 − x)C6H14} at several temperatures

Thermodynamic properties of liquid mixtures of hydrogen chloride and tetrafluoromethane

Preferential solvation in {amide + alcohol} binary mixtures. : Part 2. The N-methylpyrrolidinone + methanol mixture at T = 313.15 K: thermodynamic results and molecular dynamics calculations

VLE and viscosity modeling of N-methyl-2-pyrrolidone (NMP) + water (or 2-propanol or 2-butanol) mixtures by cubic-plus-association equation of state

Phase equilibrium modeling in biodiesel production by reactive distillation

Statistical Thermodynamics of Associated Solutions

Vapor-liquid equilibria in binary mixtures formed from hexamethyldisiloxane, toluene and ethanol

Vapour pressures and excess Gibbs free energies of (2,3,3-trimethylbutan-2-ol + n-heptane) between 298.150 and 363.279 K

Measurement of vapor-liquid equilibrium in systems with components of very different volatility by the total pressure static method

Thermodynamic Properties of Binary and Ternary Mixtures Containing Di-isopropyl Ether, 2-Propanol, and Benzene at T = 313.15 K