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Modeling of NO removal over CuO/γ-Al2O3 catalyst in a bubbling fluidized bed reactor / Muhammad F. Irfan in Industrial & engineering chemistry research, Vol. 48 N° 17 (Septembre 2009) 

Public ISBD [article]  in Industrial & engineering chemistry research > Vol. 48 N° 17 (Septembre 2009) . - pp. 7959–7964 Titre : Modeling of NO removal over CuO/γ-Al2O3 catalyst in a bubbling fluidized bed reactor Type de document : texte imprimé Auteurs : Muhammad F. Irfan, Auteur ; Sang Done Kim, Auteur ; Muhammad R. Usman, Auteur Année de publication : 2009 Article en page(s) : pp. 7959–7964 Note générale : Chemical engineering Langues : Anglais (eng) Mots-clés : CuO/γ-Al2O3  catalyst  Bubbling  fluidized  bed  reactor Résumé : The NO reduction over CuO/γ-Al2O3 catalyst in a bubbling fluidized bed reactor has been determined on the basis of the two-phase model at the maximum conversion temperature of 300 °C. This temperature is critical as it deals maximum conversion, NH3 adsorption/desorption, and NH3 oxidation, which also takes place above this temperature and hence causes a decrease of NO reduction. The effects of superficial gas velocity (ug), [NH3]/[NO] molar ratio, and the static bed height (hs) on the reduction efficiency of NO over CuO/γ-Al2O3 as a bed material in a fluidized bed reactor with variation of reaction temperatures (rate constant, kr) have been determined, and a model has been developed for the NO removal process in a bubbling fluidized bed using the two-phase theory. The results are compared with the simulation results obtained through the Maple and MATLAB simulation tools. En ligne : http://pubs.acs.org/doi/abs/10.1021/ie8018214 [article] Modeling of NO removal over CuO/γ-Al2O3 catalyst in a bubbling fluidized bed reactor [texte imprimé] / Muhammad F. Irfan, Auteur ; Sang Done Kim, Auteur ; Muhammad R. Usman, Auteur . - 2009 . - pp. 7959–7964. Chemical engineering Langues : Anglais (eng) in Industrial & engineering chemistry research > Vol. 48 N° 17 (Septembre 2009) . - pp. 7959–7964 Mots-clés : CuO/γ-Al2O3  catalyst  Bubbling  fluidized  bed  reactor Résumé : The NO reduction over CuO/γ-Al2O3 catalyst in a bubbling fluidized bed reactor has been determined on the basis of the two-phase model at the maximum conversion temperature of 300 °C. This temperature is critical as it deals maximum conversion, NH3 adsorption/desorption, and NH3 oxidation, which also takes place above this temperature and hence causes a decrease of NO reduction. The effects of superficial gas velocity (ug), [NH3]/[NO] molar ratio, and the static bed height (hs) on the reduction efficiency of NO over CuO/γ-Al2O3 as a bed material in a fluidized bed reactor with variation of reaction temperatures (rate constant, kr) have been determined, and a model has been developed for the NO removal process in a bubbling fluidized bed using the two-phase theory. The results are compared with the simulation results obtained through the Maple and MATLAB simulation tools. En ligne : http://pubs.acs.org/doi/abs/10.1021/ie8018214