Les Inscriptions à la Bibliothèque sont ouvertes en
ligne via le site: https://biblio.enp.edu.dz
Les Réinscriptions se font à :
• La Bibliothèque Annexe pour les étudiants en
2ème Année CPST
• La Bibliothèque Centrale pour les étudiants en Spécialités
A partir de cette page vous pouvez :
Retourner au premier écran avec les recherches... |
Détail de l'auteur
Auteur Qin Xin
Documents disponibles écrits par cet auteur
Affiner la rechercheMolecular thermodynamic model of multicomponent chainlike fluid mixtures based on a Lattice model / Qin Xin in Industrial & engineering chemistry research, Vol. 47 N° 23 (Décembre 2008)
[article]
in Industrial & engineering chemistry research > Vol. 47 N° 23 (Décembre 2008) . - p. 9678–9686
Titre : Molecular thermodynamic model of multicomponent chainlike fluid mixtures based on a Lattice model Type de document : texte imprimé Auteurs : Qin Xin, Auteur ; Changjun Peng, Auteur ; Honglai Liu, Auteur Année de publication : 2009 Article en page(s) : p. 9678–9686 Note générale : Chemistry engineering Langues : Anglais (eng) Mots-clés : Thermodynamic Fluid mixtures Lattice model Résumé : The molecular thermodynamic model of polymer solutions based on a close-packed lattice model presented in a previous work has been generally extended to multicomponent chainlike fluid mixtures. The Helmholtz function of mixing contains three terms, i.e., the contribution of athermal mixing of polymer chains, which is calculated by Guggenheim’s theory; the contribution of nearest-neighbor interactions between monomers, which is calculated by Yang et al.’s model of the Helmholtz function of mixing for a multicomponent Ising lattice; and the contribution of the formation of polymer chains from monomers, which is obtained according to the sticky-point theory of Cummings, Zhou, and Stell. The liquid−liquid phase equilibria of ternary chainlike mixtures predicted by this model are in good agreement with Monte Carlo simulation results and superior to the results calculated by Flory−Huggins (FH) theory and revised Freed theory (RFT) obviously. This model not only can describe types 1−3 phase separations of Treybal classification satisfactorily, but can also correlate well the coexistence curves of binary polymer blends systems with an upper critical solution temperature (UCST) or a lower critical solution temperature (LCST). Meanwhile, model parameters correlated from the binary system can be further extended to predict the corresponding liquid−liquid equilibrium of ternary mixtures, including systems of ionic liquids. En ligne : http://pubs.acs.org/doi/abs/10.1021/ie800924r [article] Molecular thermodynamic model of multicomponent chainlike fluid mixtures based on a Lattice model [texte imprimé] / Qin Xin, Auteur ; Changjun Peng, Auteur ; Honglai Liu, Auteur . - 2009 . - p. 9678–9686.
Chemistry engineering
Langues : Anglais (eng)
in Industrial & engineering chemistry research > Vol. 47 N° 23 (Décembre 2008) . - p. 9678–9686
Mots-clés : Thermodynamic Fluid mixtures Lattice model Résumé : The molecular thermodynamic model of polymer solutions based on a close-packed lattice model presented in a previous work has been generally extended to multicomponent chainlike fluid mixtures. The Helmholtz function of mixing contains three terms, i.e., the contribution of athermal mixing of polymer chains, which is calculated by Guggenheim’s theory; the contribution of nearest-neighbor interactions between monomers, which is calculated by Yang et al.’s model of the Helmholtz function of mixing for a multicomponent Ising lattice; and the contribution of the formation of polymer chains from monomers, which is obtained according to the sticky-point theory of Cummings, Zhou, and Stell. The liquid−liquid phase equilibria of ternary chainlike mixtures predicted by this model are in good agreement with Monte Carlo simulation results and superior to the results calculated by Flory−Huggins (FH) theory and revised Freed theory (RFT) obviously. This model not only can describe types 1−3 phase separations of Treybal classification satisfactorily, but can also correlate well the coexistence curves of binary polymer blends systems with an upper critical solution temperature (UCST) or a lower critical solution temperature (LCST). Meanwhile, model parameters correlated from the binary system can be further extended to predict the corresponding liquid−liquid equilibrium of ternary mixtures, including systems of ionic liquids. En ligne : http://pubs.acs.org/doi/abs/10.1021/ie800924r