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 Jacques X. Bouillard
Documents disponibles écrits par cet auteur
Affiner la rechercheExperimental and CFD analyses of bubble parameters in a variable - thickness fluidized bed / Lyczkowski, Robert W. in Industrial & engineering chemistry research, Vol. 49 N° 11 (Juin 2010)
[article]
in Industrial & engineering chemistry research > Vol. 49 N° 11 (Juin 2010) . - pp. 5166–5173
Titre : Experimental and CFD analyses of bubble parameters in a variable - thickness fluidized bed Type de document : texte imprimé Auteurs : Lyczkowski, Robert W., Auteur ; Jacques X. Bouillard, Auteur ; Isaac K. Gamwo, Auteur Année de publication : 2010 Article en page(s) : pp. 5166–5173 Note générale : Industrial chemistry Langues : Anglais (eng) Mots-clés : Analyse Fluidized Bed Résumé : Bubble characteristics in a variable-thickness fluidized bed containing nine tubes were experimentally investigated by analyzing absolute and differential pressure fluctuations. The latter were obtained from vertically aligned probes traversing the bed interior for three bed thicknesses: thin, square, and full. The important bubble parameters, namely, frequencies, effective diameters, and velocities, were determined by analyzing autocorrelations and cross-correlations obtained from these differential pressure signals for the thin and square beds. Wall effects were assessed by comparing the pressure fluctuations as the bed thickness was increased from thin to square. It was found that bubbles move faster within and above the tube bank than below it. This behavior was also found to be more pronounced in the wall regions of the full bed, which might explain why some commercial fluidized-bed combustors experience unusual metal wastage near their tube supports. Although bubble sizes consistently agreed between thin and square beds, bubble velocity reduction was observed for the thin bed. The experimental thin-bed differential pressure measurements were analyzed using a two-phase computational fluid dynamics (CFD) hydrodynamic model. Excellent agreement was obtained between the experimental results and predictions from our hydrodynamic model for autocorrelations, cross-correlations, power spectral densities, and bubble parameters. ISSN : 0888-5885 En ligne : http://pubs.acs.org/doi/abs/10.1021/ie901294e [article] Experimental and CFD analyses of bubble parameters in a variable - thickness fluidized bed [texte imprimé] / Lyczkowski, Robert W., Auteur ; Jacques X. Bouillard, Auteur ; Isaac K. Gamwo, Auteur . - 2010 . - pp. 5166–5173.
Industrial chemistry
Langues : Anglais (eng)
in Industrial & engineering chemistry research > Vol. 49 N° 11 (Juin 2010) . - pp. 5166–5173
Mots-clés : Analyse Fluidized Bed Résumé : Bubble characteristics in a variable-thickness fluidized bed containing nine tubes were experimentally investigated by analyzing absolute and differential pressure fluctuations. The latter were obtained from vertically aligned probes traversing the bed interior for three bed thicknesses: thin, square, and full. The important bubble parameters, namely, frequencies, effective diameters, and velocities, were determined by analyzing autocorrelations and cross-correlations obtained from these differential pressure signals for the thin and square beds. Wall effects were assessed by comparing the pressure fluctuations as the bed thickness was increased from thin to square. It was found that bubbles move faster within and above the tube bank than below it. This behavior was also found to be more pronounced in the wall regions of the full bed, which might explain why some commercial fluidized-bed combustors experience unusual metal wastage near their tube supports. Although bubble sizes consistently agreed between thin and square beds, bubble velocity reduction was observed for the thin bed. The experimental thin-bed differential pressure measurements were analyzed using a two-phase computational fluid dynamics (CFD) hydrodynamic model. Excellent agreement was obtained between the experimental results and predictions from our hydrodynamic model for autocorrelations, cross-correlations, power spectral densities, and bubble parameters. ISSN : 0888-5885 En ligne : http://pubs.acs.org/doi/abs/10.1021/ie901294e