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 / Thiede, Sarah in Industrial & engineering chemistry research, Vol. 49 N° 4 (Fevrier 2010)  

Public ISBD [article]  inIndustrial & engineering chemistry research > Vol. 49 N° 4 (Fevrier 2010) . - pp 1844–1847 Titre : 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 Type de document : texte imprimé Auteurs : Thiede, Sarah, Auteur ; Horstmann, Sven, Auteur ; Meisel, Thomas, Auteur Année de publication : 2010 Article en page(s) : pp 1844–1847 Note générale : Chimie industrielle Langues : Anglais (eng) Mots-clés : Vapor liquid Binary system Methyl butanol Distillation columns. Résumé : Isothermal vapor−liquid equilibrium data for 2-methyl-1-butanol + 3-methyl-1-butanol were measured using a static synthetic method at temperatures of 343.15, 353.69, 368.15, and 404.45 K. Additionally, excess enthalpy (HE) data for the system were measured with an isothermal flow calorimeter at 363.13 K. The experimental data were correlated using temperature dependent interaction parameters for the NRTL model which were fitted to all measured data. The system was chosen as a test system for distillation columns. DEWEY : 660 ISSN : 0888-5885 En ligne : http://pubs.acs.org/doi/abs/10.1021/ie9012453 [article] 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 [texte imprimé] / Thiede, Sarah, Auteur ; Horstmann, Sven, Auteur ; Meisel, Thomas, Auteur . - 2010 . - pp 1844–1847. Chimie industrielle Langues : Anglais (eng) in Industrial & engineering chemistry research > Vol. 49 N° 4 (Fevrier 2010) . - pp 1844–1847 Mots-clés : Vapor liquid Binary system Methyl butanol Distillation columns. Résumé : Isothermal vapor−liquid equilibrium data for 2-methyl-1-butanol + 3-methyl-1-butanol were measured using a static synthetic method at temperatures of 343.15, 353.69, 368.15, and 404.45 K. Additionally, excess enthalpy (HE) data for the system were measured with an isothermal flow calorimeter at 363.13 K. The experimental data were correlated using temperature dependent interaction parameters for the NRTL model which were fitted to all measured data. The system was chosen as a test system for distillation columns. DEWEY : 660 ISSN : 0888-5885 En ligne : http://pubs.acs.org/doi/abs/10.1021/ie9012453

Exemplaires

Code-barres	Cote	Support	Localisation	Section	Disponibilité
aucun exemplaire