UB Paderborn / Katalog / Suche / in CDI

1 – 25 von 158

Sortiert nach

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

Link zum Volltext

Verfügbarkeit prüfen

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

Link zum Volltext

Verfügbarkeit prüfen

The polyazeotropic behaviour of the benzene plus hexafluorobenzene system revisited

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

2017

Link zum Volltext

Verfügbarkeit prüfen

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

Link zum Volltext

Verfügbarkeit prüfen

Analysis of the VLE data in “Measurement and correlations of density, viscosity, and vapour-liquid equilibrium for fluoro alcohols”

The Journal of chemical thermodynamics, 2017-04, Vol.107, p.216-220

2017

Link zum Volltext

Verfügbarkeit prüfen

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

Link zum Volltext

Verfügbarkeit prüfen

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

Link zum Volltext

Verfügbarkeit prüfen

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

Link zum Volltext

Verfügbarkeit prüfen

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

Link zum Volltext

Verfügbarkeit prüfen

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

Link zum Volltext

Verfügbarkeit prüfen

Comments on “Experimental Measurements of Vapor–Liquid Equilibrium Data for the Binary Systems of Methanol + 2‑Butyl Acetate, 2‑Butyl Alcohol + 2‑Butyl Acetate, and Methyl Acetate + 2-Butyl Acetate at 101.33 kPa”

Journal of chemical and engineering data, 2013-12, Vol.58 (12), p.3563-3566

2013

Link zum Volltext

Verfügbarkeit prüfen

Measurements of the Excess Properties and Vapor−Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)

Journal of chemical and engineering data, 2010-12, Vol.55 (12), p.5519-5533

2010

Link zum Volltext

Verfügbarkeit prüfen

Comments on “Analysis of the Nonrandom Two-Liquid Model for Prediction of Liquid–Liquid Equilibria”

Journal of chemical and engineering data, 2015-05, Vol.60 (5), p.1526-1529

2015

Link zum Volltext

Verfügbarkeit prüfen

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

Link zum Volltext

Verfügbarkeit prüfen

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

Link zum Volltext

Verfügbarkeit prüfen

Unnoticed Pitfalls of Soave-Type Alpha Functions in Cubic Equations of State

Industrial & engineering chemistry research, 2003-10, Vol.42 (22), p.5662-5673

2003

Link zum Volltext

Verfügbarkeit prüfen

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

Link zum Volltext

Verfügbarkeit prüfen

The Herington test for thermodynamic consistency

Industrial & engineering chemistry research, 1994-01, Vol.33 (1), p.177-180

Wisniak, Jaime

1994

Link zum Volltext

Verfügbarkeit prüfen

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

Link zum Volltext

Verfügbarkeit prüfen

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

Link zum Volltext

Verfügbarkeit prüfen

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

Link zum Volltext

Verfügbarkeit prüfen

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

Link zum Volltext

Verfügbarkeit prüfen

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

Link zum Volltext

Verfügbarkeit prüfen

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

Link zum Volltext

Verfügbarkeit prüfen

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

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

1999

Link zum Volltext

Verfügbarkeit prüfen

1 – 25 von 158

Suche als RSS-Feed

Aktive Filter

KollektionSpringerLINK Contemporary (Konsortium Baden-Württemberg)

Zeitschrift / SerieIndustrial & Engineering Chemistry Product Research And Development

ThemaChemistry

Suchergebnisse filtern

Filter anzeigen

Nur zeigen

Geprüft (Peer-Review)
(156)
Mit Volltextzugriff
(158)

Publikationsform

Artikel
(158)

Sprache

Englisch
(158)

Erscheinungsjahr

n.n

Thema

14 weitere anzeigen...

Weniger anzeigen...

Menü

Weitere Dienste

Einstellungen

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

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)

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”

Analysis of the VLE data in “Measurement and correlations of density, viscosity, and vapour-liquid equilibrium for fluoro alcohols”

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

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

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)

Comments on “Experimental Measurements of Vapor–Liquid Equilibrium Data for the Binary Systems of Methanol + 2‑Butyl Acetate, 2‑Butyl Alcohol + 2‑Butyl Acetate, and Methyl Acetate + 2-Butyl Acetate at 101.33 kPa”

Measurements of the Excess Properties and Vapor−Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)

Comments on “Analysis of the Nonrandom Two-Liquid Model for Prediction of Liquid–Liquid Equilibria”

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

Unnoticed Pitfalls of Soave-Type Alpha Functions in Cubic Equations of State

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

The Herington test for thermodynamic consistency

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

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

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

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

Aktive Filter

Suchergebnisse filtern