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Comment on “Isobaric Vapor + Liquid Equilibrium Measurements and Calculations for Using Nontraditional Models for the Association Systems of Ethyl Acetate + 2-Ethylhexanoic Acid and Propyl Acetate + 2-Ethylhexanoic Acid at Atmospheric Pressure”

Journal of chemical and engineering data, 2021-01, Vol.66 (1), p.848-851

2021

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Liquid–Liquid Equilibria in Binary Solutions Formed by [Pyridinium-Derived][F4B] Ionic Liquids and Alkanols: New Experimental Data and Validation of a Multiparametric Model for Correlating LLE Data

Industrial & engineering chemistry research, 2011-11, Vol.50 (21), p.12259-12270

2011

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A fresh look at the thermodynamic consistency of vapour-liquid equilibria data

The Journal of chemical thermodynamics, 2017-02, Vol.105, p.385-395

2017

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Assessment of liquid–liquid equilibrium data by solving the Gibbs‐Duhem equation

AIChE journal, 2022-05, Vol.68 (5), p.n/a

2022

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Comment on “Quality Assessment Algorithm for Vapor−Liquid Equilibrium Data” (Kang, J. W.; Diky, V.; Chirico, R. D.; Magee, J. W.; Muzny, C. D.; Abdulagatov, I.; Kazakov, A.F.; Frenkel, M. J. Chem. Eng. Data 2010, 55, 3631−3640)

Journal of chemical and engineering data, 2010-11, Vol.55 (11), p.5394-5394

Wisniak, Jaime

2010

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Extension of the validation method for vapor–liquid equilibrium data to systems with nonvolatile components

AIChE journal, 2019-08, Vol.65 (8), p.n/a

2019

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A rigorous method to evaluate the consistency of experimental data in phase equilibria. Application to VLE and VLLE

AIChE journal, 2017-11, Vol.63 (11), p.5125-5148

2017

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New Advances in the Modeling and Verification of Experimental Information for Ester–Alkane Solutions: Application to a Batch-Distillation Case

Industrial & engineering chemistry research, 2020-04, Vol.59 (17), p.8346-8360

2020

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Jojoba Oil (Simmondsia Chinensis) as a Natural Plasticizer for Ethylene Propylene Diene Monomer Elastomers

Industrial & engineering chemistry research, 2019-10, Vol.58 (43), p.20147-20153

2019

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New Parametric Model to Correlate the Gibbs Excess Function and Other Thermodynamic Properties of Multicomponent Systems. Application to Binary Systems

Industrial & engineering chemistry research, 2010-01, Vol.49 (1), p.406-421

2010

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The polyazeotropic behaviour of the benzene plus hexafluorobenzene system revisited

The Journal of chemical thermodynamics, 2017-10, Vol.113, p.340-349

2017

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Comments on “Vapor–Liquid Equilibrium for Ternary and Binary Systems of Tetrahydrofuran, Cyclohexane, and 1,2-Propanediol at 101.3 kPa”

Journal of chemical and engineering data, 2016-05, Vol.61 (5), p.1961-1963

2016

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A new test for the thermodynamic consistency of vapor-liquid equilibrium

Industrial & engineering chemistry research, 1993-07, Vol.32 (7), p.1531-1533

Wisniak, Jaime

1993

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Further Advance to a Practical Methodology To Assess Vapor–Liquid Equilibrium Data: Influence on Binaries Rectification

Journal of chemical and engineering data, 2019-09, Vol.64 (9), p.3933-3944

2019

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A New Reference State for the Calculation of Activity Coefficients: Comment on the Paper “Molecular Theory of the Activity Coefficient and Their Reference Fugacities at the Supercritical State”

Industrial & engineering chemistry research, 2009-03, Vol.48 (5), p.2738-2738

2009

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Contributions to the modeling and behavior of solutions containing ethanoates and hydrocarbons. New experimental data for binaries of butyl ester with alkanes (C5–C10)

Fluid phase equilibria, 2016-03, Vol.412, p.79-93

2016

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Solubility of (+)-catechin in water and water-ethanol mixtures within the temperature range 277.6–331.2K: Fundamental data to design polyphenol extraction processes

Fluid phase equilibria, 2014-11, Vol.382, p.279-285

2014

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Comments on “isobaric (vapor + liquid) equilibria for three binary systems (toluene + anisole, n-butylbenzene + anisole, and guaiacol + anisole) at 101.33 kPa”

Fluid phase equilibria, 2014-12, Vol.383, p.188-192

2014

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Comments on “Experimental Isobaric Vapor−Liquid Equilibrium Data for Binary Mixtures of Cyclic Ethers with (1-Methylethyl)benzene” (Gill, B. K.; Rattan, V. K.; Kapoor, S. J. Chem. Eng. Data 2008, 53, 2041−2043)

Journal of chemical and engineering data, 2009-03, Vol.54 (3), p.1165-1167

2009

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Advances in the Correlation of Thermodynamic Properties of Binary Systems Applied to Methanol Mixtures with Butyl Esters

Industrial & engineering chemistry research, 2010-10, Vol.49 (19), p.9548-9558

2010

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rigorous approach for predicting the slope and curvature of the temperature–entropy saturation boundary of pure fluids

Energy (Oxford), 2012-09, Vol.45 (1), p.888-899

2012

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Correlation and prediction of interface tension for fluid mixtures: An approach based on cubic equations of state with the wong-sandler mixing rule

Journal of phase equilibria and diffusion, 2005-08, Vol.26 (3), p.215-224

2005

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Improvements in the Experimentation and the Representation of Thermodynamic Properties (iso‑p VLE and y E) of Alkyl Propanoate + Alkane Binaries

Journal of chemical and engineering data, 2014-01, Vol.59 (1), p.125-142

2014

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Multiproperty modeling for a set of binary systems. Evaluation of a model to correlate simultaneously several mixing properties of methyl ethanoate+alkanes and new experimental data

Fluid phase equilibria, 2013-03, Vol.341, p.105-123

2013

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Phase Equilibrium Behavior in Water (1) + n-Alkane (2) Mixtures

Industrial & engineering chemistry research, 2007-01, Vol.46 (3), p.947-954

2007

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Comment on “Isobaric Vapor + Liquid Equilibrium Measurements and Calculations for Using Nontraditional Models for the Association Systems of Ethyl Acetate + 2-Ethylhexanoic Acid and Propyl Acetate + 2-Ethylhexanoic Acid at Atmospheric Pressure”

Liquid–Liquid Equilibria in Binary Solutions Formed by [Pyridinium-Derived][F4B] Ionic Liquids and Alkanols: New Experimental Data and Validation of a Multiparametric Model for Correlating LLE Data

A fresh look at the thermodynamic consistency of vapour-liquid equilibria data

Assessment of liquid–liquid equilibrium data by solving the Gibbs‐Duhem equation

Comment on “Quality Assessment Algorithm for Vapor−Liquid Equilibrium Data” (Kang, J. W.; Diky, V.; Chirico, R. D.; Magee, J. W.; Muzny, C. D.; Abdulagatov, I.; Kazakov, A.F.; Frenkel, M. J. Chem. Eng. Data 2010, 55, 3631−3640)

Extension of the validation method for vapor–liquid equilibrium data to systems with nonvolatile components

A rigorous method to evaluate the consistency of experimental data in phase equilibria. Application to VLE and VLLE

New Advances in the Modeling and Verification of Experimental Information for Ester–Alkane Solutions: Application to a Batch-Distillation Case

Jojoba Oil (Simmondsia Chinensis) as a Natural Plasticizer for Ethylene Propylene Diene Monomer Elastomers

New Parametric Model to Correlate the Gibbs Excess Function and Other Thermodynamic Properties of Multicomponent Systems. Application to Binary Systems

The polyazeotropic behaviour of the benzene plus hexafluorobenzene system revisited

Comments on “Vapor–Liquid Equilibrium for Ternary and Binary Systems of Tetrahydrofuran, Cyclohexane, and 1,2-Propanediol at 101.3 kPa”

A new test for the thermodynamic consistency of vapor-liquid equilibrium

Further Advance to a Practical Methodology To Assess Vapor–Liquid Equilibrium Data: Influence on Binaries Rectification

A New Reference State for the Calculation of Activity Coefficients: Comment on the Paper “Molecular Theory of the Activity Coefficient and Their Reference Fugacities at the Supercritical State”

Contributions to the modeling and behavior of solutions containing ethanoates and hydrocarbons. New experimental data for binaries of butyl ester with alkanes (C5–C10)

Solubility of (+)-catechin in water and water-ethanol mixtures within the temperature range 277.6–331.2K: Fundamental data to design polyphenol extraction processes

Comments on “isobaric (vapor + liquid) equilibria for three binary systems (toluene + anisole, n-butylbenzene + anisole, and guaiacol + anisole) at 101.33 kPa”

Comments on “Experimental Isobaric Vapor−Liquid Equilibrium Data for Binary Mixtures of Cyclic Ethers with (1-Methylethyl)benzene” (Gill, B. K.; Rattan, V. K.; Kapoor, S. J. Chem. Eng. Data 2008, 53, 2041−2043)

Advances in the Correlation of Thermodynamic Properties of Binary Systems Applied to Methanol Mixtures with Butyl Esters

rigorous approach for predicting the slope and curvature of the temperature–entropy saturation boundary of pure fluids

Correlation and prediction of interface tension for fluid mixtures: An approach based on cubic equations of state with the wong-sandler mixing rule

Improvements in the Experimentation and the Representation of Thermodynamic Properties (iso‑p VLE and y E) of Alkyl Propanoate + Alkane Binaries

Multiproperty modeling for a set of binary systems. Evaluation of a model to correlate simultaneously several mixing properties of methyl ethanoate+alkanes and new experimental data

Phase Equilibrium Behavior in Water (1) + n-Alkane (2) Mixtures

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