Experimental VLE at 101.32 kPa in binary systems composed of ethyl methanoate and alkan-1-ols or alkan-2-ols and treatment of data using a correlation with temperature-dependent parameters (original ) (raw )Densities and Vapor−Liquid Equilibrium Values for Binary Mixtures Composed of Methanol + an Ethyl Ester at 141.3 kPa with Application of an Extended Correlation Equation for Isobaric VLE Data
juan ortega
Journal of Chemical & Engineering Data, 1998
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A new method for the prediction of VLE and thermodynamic properties. Preliminary results with alkane–ether–alkanol systems
Sergi Sama , Giorgio Soave
Fluid Phase Equilibria, 1999
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Thermodynamic properties of (ethylbenzene + an alkane or + an alkyl ethanoate): experimentalHmEandVmEvalues
Juan Ortega
Physics and Chemistry of Liquids, 2009
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Correlation and evaluation of VLE data for light n-alkane binary mixtures
Roman Stryjek
Pure and Applied Chemistry, 2000
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Isobaric vapor–liquid equilibria for systems composed by 2-ethoxy-2-methylbutane, methanol or ethanol and water at 101.32kPa
Ana Cabrera Soto
Fluid Phase Equilibria, 2005
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Measurement and correlation of isobaric vapour–liquid equilibrium data and excess properties of ethyl methanoate with alkanes (hexane to decane)
Juan Ortega
Fluid Phase Equilibria, 2004
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Density, Excess Molar Volume and Vapor–Liquid Equilibrium Measurements at 101.3 kPa for Binary Mixtures Containing Ethyl Acetate and a Branched Alkane: Experimental Data and Modeling
Vincent Caqueret
Liquids
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Application of the ERAS model to H E and V E of 1-alkanol + 1-alkene and 1-alkanol + 1-alkyne mixtures
June Chalmers
Fluid Phase Equilibria, 1995
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Measurements and Correlations of the Isobaric Vapor–Liquid Equilibria of Binary Mixtures and Excess Properties for Mixtures Containing an Alkyl (Methyl, Ethyl) Butanoate with an Alkane (Heptane, Nonane) at 101.3 kPa
juan ortega
Journal of Chemical & Engineering Data, 2012
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Improvements in the Experimentation and the Representation of Thermodynamic Properties (iso-p VLE and yE) of Alkyl Propanoate + Alkane Binaries
Raul Rios
Journal of Chemical & Engineering Data, 2013
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Isobaric Vapor−Liquid Equilibrium Data and Excess Properties of Binary Systems Comprised of Alkyl Methanoates + Hexane
ignacio de la nuez
Journal of Chemical & Engineering Data, 2007
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Isobaric vapor-liquid equilibrium data for the binary systems 1,2-dimethoxyethane + alcohols
Sagrario Beltrán
Journal of Chemical and Engineering Data, 1991
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Isobaric vapor–liquid equilibria for binary and ternary mixtures with cyclohexane, cyclohexene, and morpholine at 100kPa
Antonio Aucejo
Fluid Phase Equilibria, 2010
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Vapor-liquid equilibria at 101.32 kPa in mixtures formed by the first four butyl alkanoates and butan-2-ol
Juan Ortega
Fluid Phase Equilibria, 1996
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Measurements and Modeling of VLE Data for Butyl Acetate with 2-Propanol or 2-Butanol. Binary Systems at 0.15 and 0.6 MPa
Isabel GARCÍA MONTESDEOCA
Journal of Chemical & Engineering Data, 2017
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Experimental VLE Data of Binary Systems of Ester + Alcohol at 0.6 MPa. Verification using new Association Parameters for the Point– to–Point Test
Isabel GARCÍA MONTESDEOCA
2023
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Multiproperty Correlation of Experimental Data of the Binaries Propyl Ethanoate + Alkanes (Pentane to Decane). New Experimental Information for Vapor–Liquid Equilibrium and Mixing Properties
juan ortega
Journal of Chemical & Engineering Data, 2013
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Isobaric Vapor-Liquid Equilibria of Gasoline Additives Systems At 101.3 kPa
Prof. Dr. Khalid Farhod
uotechnology.edu.iq
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Thermodynamic Study of Binary Mixtures Containing an Isobutylalkanol and an Alkyl (Ethyl to Butyl) Alkanoate (Methanoate to Butanoate), Contributing with Experimental Values of Excess Molar Enthalpies and Volumes, and Isobaric Vapor−Liquid Equilibria
Stefano Ottani
Journal of Chemical & Engineering Data, 1999
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Thermophysical Properties of Low-Density Pure Alkanes and Their Binary Mixtures Calculated by Means of an (n-6) Lennard-Jones Temperature-Dependent Potential
Uwe Hohm
International Journal of Thermophysics, 2006
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Isobaric Vapor Liquid Equilibrium at 101.3 kPa for the Binary Mixtures 2-Methyl-2-Butene/TAME and 2-Methyl-1-Butene/TAME
Valentin PLESU
16th International Conference on Process Integration, Modelling and Optimisation For Energy Saving and Pollution Reduction (Pres'13), 2013
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Advances in the Correlation of Thermodynamic Properties of Binary Systems Applied to Methanol Mixtures with Butyl Esters
Juan Ortega
Industrial & Engineering Chemistry Research, 2010
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Phase Equilibria in the Systems Ethyl 1,1-Dimethylethyl Ether + Methylcyclohexane, 2,2,4Trimethylpentane + Methylcyclohexane, and Ethyl 1,1-Dimethylethyl Ether + 2,2,4Trimethylpentane + Methylcyclohexane at 94.00 kPa
Graciela Galindo , Ricardo Reich
Journal of Chemical and Engineering Data, 1999
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Vapor Pressure and VLE Data Measurements on Ethyl Acetate/Ethanol Binary System at 0.1, 0.5, and 0.7 MPa
PEDRO SUSIAL
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 2011
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Isobaric Vapor–Liquid Equilibria for the Binary Mixtures Composed of Ethylene Glycol, 1,2-Propylene Glycol, 1,2-Butanediol, and 1,3-Butanediol at 10.00 kPa
György Pátzay
Journal of Chemical & Engineering Data, 2013
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Isobaric VLE for the binary systems Isobutyl acetate +Methanol or +1-Propanol at 0.15 MPa
PEDRO SUSIAL
Afinidad -Barcelona-
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Vapor−Liquid Equilibria Data for Binary Systems of Ethylbenzene + Xylene Isomers at 100.65 kPa
Willias Rodrigues
Journal of Chemical and Engineering Data, 2005
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Azeotropic and Heats of Mixing Data for Several Binary Organic Systems Containing 1-Methoxy-2-propanol and 2-Butoxy Ethanol
Jürgen Gmehling
Journal of Chemical & Engineering Data, 2006
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Liquid–liquid equilibria for -alkanes (C, C, C)+propylbenzene+NMP mixtures at temperatures between 298 and 328K
Jasem Alkandary
Fluid Phase Equilibria, 2005
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Phase Equilibria in the Systems Ethyl 1,1-Dimethylethyl Ether + Benzene + 2,2,4Trimethylpentane and Benzene + 2,2,4Trimethylpentane at 94.00 kPa
Ricardo Reich
Physics and Chemistry of Liquids, 2001
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IJERT-Isobaric Vapour-Liquid Equilibrium of Binary Mixture of 1, 2-Di-chloroethane with 1-Heptanol at 95.72 Kpa
IJERT Journal
International Journal of Engineering Research and Technology (IJERT), 2014
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Phase Equilibria in the Systems Cyclohexane + 2,2,4-Trimethylpentane and Ethyl 1,1-Dimethylethyl Ether + Cyclohexane + 2,2,4-Trimethylpentane at 94.00 kPa
Ricardo Reich
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Vapor-liquid equilibrium data for propylene+ ethanol, propylene+ MEK, and propylene+ MTBE
Esteban Brignole
Journal of Chemical & …, 1997
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Isobaric Vapor-Liquid Equilibria of Mesitylene + 1- Heptanol and Mesitylene +1-Octanol at 97.3 kPa
Aarti Sharma
2009
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