0000000000666786

AUTHOR

And Juan B. Montón

showing 3 related works from this author

Isobaric Vapor−Liquid Equilibria for the Binary System 3-Methylpentane + 2-Methyl-2-propanol and for the Ternary System Methyl 1,1-Dimethylethyl Ethe…

1999

Isobaric vapor−liquid equilibria data were obtained for the 3-methylpentane + 2-methyl-2-propanol binary system and methyl 1,1-dimethylethyl ether + 3-methylpentane + 2-methyl-2-propanol ternary system at 101.3 kPa in a temperature range from 329 to 356 K. The data were found to be thermodynamically consistent according to the Van Ness−Byer−Gibbs method for the binary system and according to the McDermott−Ellis method for the ternary one. The binary system shows a minimum boiling azeotrope that boils at 333.4 K and contains 82.6 mol % of 3-methylpentane. The binary interaction parameters obtained from this work and literature data are used to predict the vapor−liquid equilibrium for the ter…

Propanolchemistry.chemical_compoundUNIQUACTernary numeral systemchemistryGeneral Chemical EngineeringAzeotropeNon-random two-liquid modelThermodynamicsGeneral ChemistryBinary systemTernary operation3-MethylpentaneJournal of Chemical & Engineering Data
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Isobaric Vapor−Liquid Equilibria of the Water + 1-Propanol System at 30, 60, and 100 kPa

1996

Isobaric vapor−liquid equilibria for the water + 1-propanol system are reported at 30, 60, and 100 kPa. The results were found to be thermodynamically consistent according to Van Ness−Byer−Gibbs, Kojima, and Wisniak methods. The system shows a minimum boiling azeotrope, and the azeotropic composition is scarcely shifted with pressure. Results were compared with literature values. The data were correlated with Margules, Van Laar, Wilson, NRTL, and UNIQUAC liquid-phase activity coefficient models.

Activity coefficientBoiling pointUNIQUACVapor pressureChemistryGeneral Chemical EngineeringBoilingAzeotropeNon-random two-liquid modelThermodynamicsIsobaric processGeneral ChemistryJournal of Chemical & Engineering Data
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Isobaric Vapor−Liquid Equilibria of the Water + 2-Propanol System at 30, 60, and 100 kPa

1996

Isobaric vapor−liquid equilibria were obtained for the water + 2-propanol system at 30, 60, and 100 kPa. The activity coefficients were found to be thermodynamically consistent by the methods of Van Ness−Byer−Gibbs, Kojima, and Wisniak. The data were correlated with five liquid phase activity coefficient models (Margules, Van Laar, Wilson, NRTL, and UNIQUAC).

Activity coefficientPropanolBoiling pointchemistry.chemical_compoundUNIQUACSynthetic fuelChemistryGeneral Chemical EngineeringNon-random two-liquid modelThermodynamicsIsobaric processGeneral ChemistryRefractive indexJournal of Chemical & Engineering Data
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