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Correlation and prediction for isobaric vapor – liquid equilibria of the diethyl ether + methanol + 1 - butanol ternary system and the constituent binary systems at 101.325 kPa / Daming Gao in Industrial & engineering chemistry research, Vol. 51 N° 1 (Janvier 2012) 

Public ISBD [article]  in Industrial & engineering chemistry research > Vol. 51 N° 1 (Janvier 2012) . - pp. 567–575 Titre : Correlation and prediction for isobaric vapor – liquid equilibria of the diethyl ether + methanol + 1 - butanol ternary system and the constituent binary systems at 101.325 kPa Type de document : texte imprimé Auteurs : Daming Gao, Auteur ; Hui Zhang, Auteur ; Dechun Zhu, Auteur Année de publication : 2012 Article en page(s) : pp. 567–575 Note générale : Chimie industrielle Langues : Anglais (eng) Mots-clés : Vapor  Liquid  Methanol  Butanol  ternary  system Résumé : The vapor–liquid equilibrium (VLE) data for the diethyl ether + methanol + 1-butanol ternary system and three constituent binary systems were measured at different liquid phase compositions using a dynamic recirculating still at 101.325 kPa. The activity coefficients of the solution were correlated with the Wilson, nonrandom two-liquid (NRTL), Margules, van Laar, and universal quasichemical activity coefficient (UNIQUAC) models through the fit of least-squares method. In addition, the VLE data of the ternary system were also predicted from these binary interaction parameters of Wilson, NRTL, Margules, van Laar, and UNIQUAC model parameters without any additional adjustment, which obtained the calculated vapor-phase compositions and bubble points compared with the measured values. The calculated bubble points with the model parameters of activity coefficients were in good agreement with the experimental data. The ASOG group contribution method also was used for prediction of the three binary systems. The thermodynamic consistency of the experimental VLE data was checked out by means of the Wisniak’s L–W test for the binary systems and the Wisniak–Tamir’s modification of McDermott–Ellis test for the ternary system, respectively. DEWEY : 660 ISSN : 0888-5885 En ligne : http://pubs.acs.org/doi/abs/10.1021/ie201805m [article] Correlation and prediction for isobaric vapor – liquid equilibria of the diethyl ether + methanol + 1 - butanol ternary system and the constituent binary systems at 101.325 kPa [texte imprimé] / Daming Gao, Auteur ; Hui Zhang, Auteur ; Dechun Zhu, Auteur . - 2012 . - pp. 567–575. Chimie industrielle Langues : Anglais (eng) in Industrial & engineering chemistry research > Vol. 51 N° 1 (Janvier 2012) . - pp. 567–575 Mots-clés : Vapor  Liquid  Methanol  Butanol  ternary  system Résumé : The vapor–liquid equilibrium (VLE) data for the diethyl ether + methanol + 1-butanol ternary system and three constituent binary systems were measured at different liquid phase compositions using a dynamic recirculating still at 101.325 kPa. The activity coefficients of the solution were correlated with the Wilson, nonrandom two-liquid (NRTL), Margules, van Laar, and universal quasichemical activity coefficient (UNIQUAC) models through the fit of least-squares method. In addition, the VLE data of the ternary system were also predicted from these binary interaction parameters of Wilson, NRTL, Margules, van Laar, and UNIQUAC model parameters without any additional adjustment, which obtained the calculated vapor-phase compositions and bubble points compared with the measured values. The calculated bubble points with the model parameters of activity coefficients were in good agreement with the experimental data. The ASOG group contribution method also was used for prediction of the three binary systems. The thermodynamic consistency of the experimental VLE data was checked out by means of the Wisniak’s L–W test for the binary systems and the Wisniak–Tamir’s modification of McDermott–Ellis test for the ternary system, respectively. DEWEY : 660 ISSN : 0888-5885 En ligne : http://pubs.acs.org/doi/abs/10.1021/ie201805m