Documents disponibles écrits par cet auteur

Aiche symposium series / Lyczkowski, Robert W. 

Public ISBD [périodique]  Voir les bulletins disponibles  Titre : Aiche symposium series Type de document : texte imprimé Auteurs : Lyczkowski, Robert W., Editeur scientifique Editeur : New York : American institute of chemical engineers Année de publication : 1971-2002 ISBN/ISSN/EAN : 0065-8812 Note générale : Périodicité: Irrégulier 1984 1986-1988 Langues : Anglais (eng) Mots-clés : Génie  chimique  ;  Transfert  de  chaleur Index. décimale : 66.0 Ingénierie chimique en général DEWEY : 540 En ligne : http://www.aiche.org [périodique]  Voir les bulletins disponibles Aiche symposium series [texte imprimé] / Lyczkowski, Robert W., Editeur scientifique . - New York (Three Park Avenue, 10016-5991) : American institute of chemical engineers, 1971-2002. ISSN : 0065-8812 Périodicité: Irrégulier 1984 1986-1988 Langues : Anglais (eng) Mots-clés : Génie  chimique  ;  Transfert  de  chaleur Index. décimale : 66.0 Ingénierie chimique en général DEWEY : 540 En ligne : http://www.aiche.org

Experimental 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) 

Public ISBD [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