Calculation of vapor-liquid equilibria from infinite-dilution excess enthalpy data using the Wilson or NRTL equation

Arthur S. Gow

doi:10.1021/ie00024a028

Calculation of vapor-liquid equilibria from infinite-dilution excess enthalpy data using the Wilson or NRTL equation

Industrial & Engineering Chemistry Research ◽

10.1021/ie00024a028 ◽

1993 ◽

Vol 32 (12) ◽

pp. 3150-3161 ◽

Cited By ~ 86

Author(s):

Arthur S. Gow

Keyword(s):

Infinite Dilution ◽

Excess Enthalpy ◽

Nrtl Equation ◽

Vapor Liquid Equilibria ◽

Enthalpy Data ◽

Vapor Liquid

Corrigendum to “Isothermal (vapor + liquid) equilibria and excess enthalpy data of {1-hexene + methyl butyl ether (MBE)} and {1-hexene + methyl tert-butyl ether (MTBE)} binary systems at several temperatures” [J. Chem. Thermodyn. 54 (2012) 83–89]

The Journal of Chemical Thermodynamics ◽

10.1016/j.jct.2015.04.019 ◽

2015 ◽

Vol 88 ◽

pp. 142-143

Author(s):

Rachida Hani ◽

Roland Solimando ◽

Latifa Negadi ◽

Jacques Jose ◽

Ahmed Ait Kaci

Keyword(s):

Binary Systems ◽

Excess Enthalpy ◽

Methyl Tert Butyl Ether ◽

Butyl Ether ◽

Tert Butyl ◽

Vapor Liquid Equilibria ◽

Enthalpy Data ◽

Vapor Liquid

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

Journal of Chemical & Engineering Data ◽

10.1021/je980294s ◽

1999 ◽

Vol 44 (3) ◽

pp. 539-543 ◽

Cited By ~ 7

Author(s):

Sven Horstmann ◽

Hergen Gardeler ◽

Rainer Bölts ◽

Jürgen Gmehling

Keyword(s):

Binary Systems ◽

Excess Enthalpy ◽

Temperature Range ◽

Vapor Liquid Equilibria ◽

Enthalpy Data ◽

Vapor Liquid

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

Industrial & Engineering Chemistry Research ◽

10.1021/ie9012453 ◽

2010 ◽

Vol 49 (4) ◽

pp. 1844-1847 ◽

Cited By ~ 5

Author(s):

Sarah Thiede ◽

Sven Horstmann ◽

Thomas Meisel ◽

Jacobus Sinnema ◽

Jürgen Gmehling

Keyword(s):

Binary System ◽

Experimental Determination ◽

Excess Enthalpy ◽

Distillation Columns ◽

Test Mixture ◽

System 2 ◽

Vapor Liquid Equilibria ◽

Enthalpy Data ◽

Vapor Liquid

Vapor−Liquid Equilibria and Excess Enthalpy Data for the Binary System Propionic Aldehyde + 2-Methyl-2-butanol at 333.15 K

Journal of Chemical & Engineering Data ◽

10.1021/je010113d ◽

2001 ◽

Vol 46 (6) ◽

pp. 1487-1489 ◽

Cited By ~ 4

Author(s):

Sven Horstmann ◽

Jürgen Gmehling

Keyword(s):

Binary System ◽

Excess Enthalpy ◽

Vapor Liquid Equilibria ◽

Enthalpy Data ◽

Vapor Liquid

Isothermal Vapor−Liquid Equilibrium, Excess Enthalpy Data, and Activity Coefficients at Infinite Dilution for the Binary System Water + Methyl Lactate

Journal of Chemical & Engineering Data ◽

10.1021/je049824c ◽

2005 ◽

Vol 50 (1) ◽

pp. 85-88 ◽

Cited By ~ 5

Author(s):

Maria Teresa Sanz ◽

Jürgen Gmehling

Keyword(s):

Binary System ◽

Activity Coefficients ◽

Infinite Dilution ◽

Excess Enthalpy ◽

Liquid Equilibrium ◽

Vapor Liquid Equilibrium ◽

Methyl Lactate ◽

System Water ◽

Enthalpy Data ◽

Vapor Liquid

Vapor−Liquid Equilibria and Excess Enthalpy Data for the Binary Systems 2-Methyltetrahydrofuran with 2,2,4-Trimethylpentane (Isooctane), Ethanol, Toluene, Cyclohexane, and Methylcyclohexane§

Journal of Chemical & Engineering Data ◽

10.1021/je990023x ◽

1999 ◽

Vol 44 (5) ◽

pp. 959-964 ◽

Cited By ~ 12

Author(s):

Sven Horstmann ◽

Hergen Gardeler ◽

Rainer Bölts ◽

David Zudkevitch ◽

Jürgen Gmehling

Keyword(s):

Binary Systems ◽

Excess Enthalpy ◽

Vapor Liquid Equilibria ◽

Enthalpy Data ◽

Vapor Liquid

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

Journal of Chemical & Engineering Data ◽

10.1021/je800888n ◽

2009 ◽

Vol 54 (7) ◽

pp. 2045-2048 ◽

Cited By ~ 6

Author(s):

Latifa Negadi ◽

Ilham Mokbel ◽

Amina Negadi ◽

Ahmed Ait Kaci ◽

Jacques Jose ◽

...

Keyword(s):

Binary System ◽

Butyric Acid ◽

Excess Enthalpy ◽

Vapor Liquid Equilibria ◽

Enthalpy Data ◽

Vapor Liquid

Isothermal (vapor+liquid) equilibria and excess enthalpy data of {1-hexene+methyl butyl ether (MBE)} and {1-hexene+methyl tert-butyl ether (MTBE)} binary systems at several temperatures

The Journal of Chemical Thermodynamics ◽

10.1016/j.jct.2012.03.016 ◽

2012 ◽

Vol 54 ◽

pp. 83-89 ◽

Cited By ~ 1

Author(s):

Rachida Hani ◽

Roland Solimando ◽

Latifa Negadi ◽

Jacques Jose ◽

Ahmed Ait Kaci

Keyword(s):

Binary Systems ◽

Excess Enthalpy ◽

Methyl Tert Butyl Ether ◽

Butyl Ether ◽

Tert Butyl ◽

Vapor Liquid Equilibria ◽

Enthalpy Data ◽

Vapor Liquid

The NRTL equation as a predictive tool for vapor–liquid equilibria

Fluid Phase Equilibria ◽

10.1016/j.fluid.2003.10.013 ◽

2004 ◽

Vol 218 (1) ◽

pp. 33-39 ◽

Cited By ~ 17

Author(s):

Alessandro Vetere

Keyword(s):

Predictive Tool ◽

Nrtl Equation ◽

Vapor Liquid Equilibria ◽

Vapor Liquid

Prediction of vapor-liquid equilibria of aqueous systems in the subcritical range by using the NRTL equation

Fluid Phase Equilibria ◽

10.1016/0378-3812(94)80022-7 ◽

1994 ◽

Vol 99 ◽

pp. 63-74 ◽

Cited By ~ 7

Author(s):

Alessandro Vetere

Keyword(s):

Aqueous Systems ◽

Nrtl Equation ◽

Vapor Liquid Equilibria ◽

Vapor Liquid