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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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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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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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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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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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Comments on “Boiling temperature measurements on the binary mixtures formed by tert-butanol with some chloroethanes and chloroethylenes at 94.6kPa”

Fluid phase equilibria, 2004-09, Vol.224 (1), p.155-156

Wisniak, Jaime

2004

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Some observations regarding the prediction of isochoric heat capacities by engineering EOS models

Fluid phase equilibria, 2009-03, Vol.277 (2), p.121-125

2009

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Simultaneous prediction of the critical and sub-critical phase behavior in mixtures using equation of state I. Carbon dioxide-alkanols

Chemical engineering science, 2001-12, Vol.56 (23), p.6485-6510

2001

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Comments on “Boiling temperature measurements on the binary mixtures formed by tert-butanol with some chloroethanes and chloroethylenes at 94.6 kPa”

Fluid phase equilibria, 2004-09, Vol.224 (1), p.155-156

Wisniak, Jaime

2004

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Physical properties of (jojoba oil + n-hexane) compared with other (vegetable oil + n-hexane) mixtures

The Journal of chemical thermodynamics, 2008-10, Vol.40 (10), p.1477-1484

2008

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Correlation and prediction of mixing thermodynamic properties of ester-containing systems: Ester+alkane and ester+ester binary systems and the ternary dodecane+ethyl pentanoate+ethyl ethanoate

The Journal of chemical thermodynamics, 2012-11, Vol.54, p.41-48

2012

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Simultaneous prediction of the critical and sub-critical phase behavior in mixtures using equations of state II. Carbon dioxide–heavy n-alkanes

Chemical engineering science, 2003-06, Vol.58 (12), p.2529-2550

2003

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Potential uses of jojoba oil and meal — a review

Industrial crops and products, 1994-10, Vol.3 (1), p.43-68

Wisniak, Jaime

1994

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Simultaneous prediction of interfacial tension and phase equilibria in binary mixtures: An approach based on cubic equations of state with improved mixing rules

Fluid phase equilibria, 2005-01, Vol.227 (2), p.225-238

2005

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Limiting conditions for the critical pressure step point behavior in the Global Phase Diagram of binary mixtures composed by spherical molecules of equal sizes

The Journal of supercritical fluids, 2009-03, Vol.48 (2), p.108-119

2009

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Density, excess volume, and excess coefficient of thermal expansion of the binary systems of dimethyl carbonate with butyl methacrylate, allyl methacrylate, styrene, and vinyl acetate at T = (293.15, 303.15, and 313.15) K

The Journal of chemical thermodynamics, 2008-12, Vol.40 (12), p.1671-1683

2008

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Analysis of residuals — a useful tool for phase equilibrium data analysis

Fluid phase equilibria, 1999-10, Vol.164 (1), p.61-82

1999

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Densities and volumes of mixing of the ternary system toluene + butyl acrylate + methyl methacrylate and its binaries at 298.15 K

The Journal of chemical thermodynamics, 2007, Vol.39 (1), p.88-95

2007

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Densities and excess volumes of benzene with ethyl acrylate, butyl acrylate, methyl methacrylate, and styrene at 298.15 K

Thermochimica acta, 2003-03, Vol.398 (1), p.39-46

2003

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Densities, isobaric thermal compressibilities and derived thermodynamic properties of the binary systems of cyclohexane with allyl methacrylate, butyl methacrylate, methacrylic acid, and vinyl acetate at t = (298.15 and 308.15) K

Thermochimica acta, 2005-10, Vol.437 (1), p.1-6

2005

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Comments on “Computing all the azeotropes in refrigerant mixtures through equations of state” by Naveed Aslam and Aydin K. Sunol [Fluid Phase Equilib. 224 (2004), 97–109]

Fluid phase equilibria, 2005-09, Vol.236 (1), p.261-266

2005

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Estimation of interfacial behavior using the global phase diagram approach: I. Carbon dioxide– n-alkanes

Thermochimica acta, 2004-03, Vol.411 (2), p.171-176

2004

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Simultaneous prediction of the critical and sub-critical phase behavior in mixtures using equations of state II. Carbon dioxide-heavy \+i\n\-i\-alkanes

Chemical engineering science, 2003-06, Vol.58 (12), p.2529-2550.

2003

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

The polyazeotropic behaviour of the benzene plus hexafluorobenzene system revisited

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”

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

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

Comments on “Boiling temperature measurements on the binary mixtures formed by tert-butanol with some chloroethanes and chloroethylenes at 94.6kPa”

Some observations regarding the prediction of isochoric heat capacities by engineering EOS models

Simultaneous prediction of the critical and sub-critical phase behavior in mixtures using equation of state I. Carbon dioxide-alkanols

Comments on “Boiling temperature measurements on the binary mixtures formed by tert-butanol with some chloroethanes and chloroethylenes at 94.6 kPa”

Physical properties of (jojoba oil + n-hexane) compared with other (vegetable oil + n-hexane) mixtures

Correlation and prediction of mixing thermodynamic properties of ester-containing systems: Ester+alkane and ester+ester binary systems and the ternary dodecane+ethyl pentanoate+ethyl ethanoate

Simultaneous prediction of the critical and sub-critical phase behavior in mixtures using equations of state II. Carbon dioxide–heavy n-alkanes

Potential uses of jojoba oil and meal — a review

Simultaneous prediction of interfacial tension and phase equilibria in binary mixtures: An approach based on cubic equations of state with improved mixing rules

Limiting conditions for the critical pressure step point behavior in the Global Phase Diagram of binary mixtures composed by spherical molecules of equal sizes

Density, excess volume, and excess coefficient of thermal expansion of the binary systems of dimethyl carbonate with butyl methacrylate, allyl methacrylate, styrene, and vinyl acetate at T = (293.15, 303.15, and 313.15) K

Analysis of residuals — a useful tool for phase equilibrium data analysis

Densities and volumes of mixing of the ternary system toluene + butyl acrylate + methyl methacrylate and its binaries at 298.15 K

Densities and excess volumes of benzene with ethyl acrylate, butyl acrylate, methyl methacrylate, and styrene at 298.15 K

Densities, isobaric thermal compressibilities and derived thermodynamic properties of the binary systems of cyclohexane with allyl methacrylate, butyl methacrylate, methacrylic acid, and vinyl acetate at t = (298.15 and 308.15) K

Comments on “Computing all the azeotropes in refrigerant mixtures through equations of state” by Naveed Aslam and Aydin K. Sunol [Fluid Phase Equilib. 224 (2004), 97–109]

Estimation of interfacial behavior using the global phase diagram approach: I. Carbon dioxide– n-alkanes

Simultaneous prediction of the critical and sub-critical phase behavior in mixtures using equations of state II. Carbon dioxide-heavy \+i\n\-i\-alkanes

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