Development of a countercurrent multistage fluidized-bed reactor and mathematical modeling for prediction of removal efficiency of sulfur dioxide from flue gases / C. R. Mohanty in Industrial & engineering chemistry research, Vol. 48 N°3 (Février 2009)  

Public ISBD [article]  inIndustrial & engineering chemistry research > Vol. 48 N°3 (Février 2009) . - p. 1629–1637 Titre : Development of a countercurrent multistage fluidized-bed reactor and mathematical modeling for prediction of removal efficiency of sulfur dioxide from flue gases Type de document : texte imprimé Auteurs : C. R. Mohanty, Auteur ; G. Malavia, Auteur ; B. C. Meikap, Auteur Année de publication : 2009 Article en page(s) : p. 1629–1637 Note générale : Chemical engineering Langues : Anglais (eng) Mots-clés : Flue Gases -- sulfur dioxide Fluidization mathematical modeling Résumé : A bubbling countercurrent multistage fluidized-bed reactor for the sorption of sulfur dioxide by hydrated lime particles was simulated employing a two-phase model, with the bubble phase assumed to be in plug flow and with the emulsion phase either in plug flow (EGPF model) or in perfectly mixed flow (EGPM model). The model calculations were compared with experimental data in term of percentage removal efficiency of sulfur dioxide. Both models were applied to understand the influence of operating parameters on the reactor performance. The comparison showed that the EGPF model agreed well with the experimental data. From the perspective of use of a multistage fluidized-bed reactor as air pollution control equipment in industry, the model could be considered general enough for predicting the performance of reactors for gas−solid treatment. En ligne : http://pubs.acs.org/doi/abs/10.1021/ie801615c [article] Development of a countercurrent multistage fluidized-bed reactor and mathematical modeling for prediction of removal efficiency of sulfur dioxide from flue gases [texte imprimé] / C. R. Mohanty, Auteur ; G. Malavia, Auteur ; B. C. Meikap, Auteur . - 2009 . - p. 1629–1637. Chemical engineering Langues : Anglais (eng) in Industrial & engineering chemistry research > Vol. 48 N°3 (Février 2009) . - p. 1629–1637 Mots-clés : Flue Gases -- sulfur dioxide Fluidization mathematical modeling Résumé : A bubbling countercurrent multistage fluidized-bed reactor for the sorption of sulfur dioxide by hydrated lime particles was simulated employing a two-phase model, with the bubble phase assumed to be in plug flow and with the emulsion phase either in plug flow (EGPF model) or in perfectly mixed flow (EGPM model). The model calculations were compared with experimental data in term of percentage removal efficiency of sulfur dioxide. Both models were applied to understand the influence of operating parameters on the reactor performance. The comparison showed that the EGPF model agreed well with the experimental data. From the perspective of use of a multistage fluidized-bed reactor as air pollution control equipment in industry, the model could be considered general enough for predicting the performance of reactors for gas−solid treatment. En ligne : http://pubs.acs.org/doi/abs/10.1021/ie801615c

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