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 Jannike Solsvik
Documents disponibles écrits par cet auteur
Affiner la rechercheOn the Consistent Modeling of Porous Catalyst Pellets / Jannike Solsvik in Industrial & engineering chemistry research, Vol. 51 N° 24 (Juin 2012)
[article]
in Industrial & engineering chemistry research > Vol. 51 N° 24 (Juin 2012) . - pp. 8222-8236
Titre : On the Consistent Modeling of Porous Catalyst Pellets : Mass and Molar Formulations Type de document : texte imprimé Auteurs : Jannike Solsvik, Auteur ; Stian Tangen, Auteur ; Hugo A. Jakobsen, Auteur Année de publication : 2012 Article en page(s) : pp. 8222-8236 Note générale : Industrial chemistry Langues : Anglais (eng) Mots-clés : Pellet Catalyst Modeling Résumé : Accurate modeling ofintrapartide heat and mass transport is a prerequisite for the design of many industrial processes and the interpretation of experiments. In the recent literature, deviations are noticed between simulation results of mole and mass formulated pellet model equations. For this reason, in this study, a comprehensive mathematical and numerical analysis has been performed. Several pellet model complexities are simulated to elucidate the effects of modeling assumptions on the behavior of the mass and mole formulated pellet model equations. Noted findings are as follows: (i) The simulation results show that the Wilke and Wilke-Bosanquet models with respect to the mass and mole average velocity definitions are not consistent. The Maxwell―Stefan and dusty gas closures are recommended; identical simulation results can be obtained with the mass and mole formulated pellet equations where the species mole and mass diffusion fluxes are defined relative to the respective average mixture velocities. (ii) Considering simplified models in which the convective terms are neglected, the species mole balance should be manipulated with the continuity equation to enforce the continuity balance of the mole number change. For the rigorous models retaining the convective terms, model manipulation by use of the continuity equation is still beneficial simplifying the model complexity and thus the implementation. Moreover, it is important to identify the velocity definitions used in the pellet equations and apply them consistently. DEWEY : 0888-5885 En ligne : http://cat.inist.fr/?aModele=afficheN&cpsidt=26029657 [article] On the Consistent Modeling of Porous Catalyst Pellets : Mass and Molar Formulations [texte imprimé] / Jannike Solsvik, Auteur ; Stian Tangen, Auteur ; Hugo A. Jakobsen, Auteur . - 2012 . - pp. 8222-8236.
Industrial chemistry
Langues : Anglais (eng)
in Industrial & engineering chemistry research > Vol. 51 N° 24 (Juin 2012) . - pp. 8222-8236
Mots-clés : Pellet Catalyst Modeling Résumé : Accurate modeling ofintrapartide heat and mass transport is a prerequisite for the design of many industrial processes and the interpretation of experiments. In the recent literature, deviations are noticed between simulation results of mole and mass formulated pellet model equations. For this reason, in this study, a comprehensive mathematical and numerical analysis has been performed. Several pellet model complexities are simulated to elucidate the effects of modeling assumptions on the behavior of the mass and mole formulated pellet model equations. Noted findings are as follows: (i) The simulation results show that the Wilke and Wilke-Bosanquet models with respect to the mass and mole average velocity definitions are not consistent. The Maxwell―Stefan and dusty gas closures are recommended; identical simulation results can be obtained with the mass and mole formulated pellet equations where the species mole and mass diffusion fluxes are defined relative to the respective average mixture velocities. (ii) Considering simplified models in which the convective terms are neglected, the species mole balance should be manipulated with the continuity equation to enforce the continuity balance of the mole number change. For the rigorous models retaining the convective terms, model manipulation by use of the continuity equation is still beneficial simplifying the model complexity and thus the implementation. Moreover, it is important to identify the velocity definitions used in the pellet equations and apply them consistently. DEWEY : 0888-5885 En ligne : http://cat.inist.fr/?aModele=afficheN&cpsidt=26029657