Voidage and pressure profile characteristics of sand-iron ore−coal−FCC single-particle systems in the riser of a pilot plant circulating fluidized bed / M. Das in Industrial & engineering chemistry research, Vol. 47 n°11 (Juin 2008)  

Public ISBD [article]  inIndustrial & engineering chemistry research > Vol. 47 n°11 (Juin 2008) . - p. 4018–4024 Titre : Voidage and pressure profile characteristics of sand-iron ore−coal−FCC single-particle systems in the riser of a pilot plant circulating fluidized bed Type de document : texte imprimé Auteurs : M. Das, Auteur ; B. C. Meikap, Auteur ; R. K. Saha, Auteur Année de publication : 2008 Article en page(s) : p. 4018–4024 Note générale : Bibliogr. p. 4024 Langues : Anglais (eng) Mots-clés : Single-particle systems  Circulating fluidized bed  Iron ore  Coal Résumé : Hydrodynamic behaviors of single system of particles were investigated in a circulating fluidized bed (CFB) unit. Particles belonging to Geldart groups A and B like sand of various sizes (80, 300, 417, 522, 599, and 622 μm), FCC catalyst (120 μm), iron ore (166 and 140 μm), and coal (335 and 168 μm) were used to study the hydrodynamic characteristics. Superficial air velocity used in the present study ranged between 2.01 and 4.681 m/s and corresponding mass fluxes were 12.5−50 kg/(m2 s). A CFB needs the creation of some special hydrodynamic conditions, namely a certain combination of superficial gas velocity, solids circulation rate, particle diameter, density of particle, etc. which can give rise to a state wherein the solid particles are subjected to an upward velocity greater than the terminal or free fall velocity of the majority of the individual particles. The hydrodynamics of the bed was investigated in depth and theoretical analysis is presented to support the findings. Based on gas−solid momentum balance in the riser, a distinction between apparent and real voidage has been made. The effects of acceleration and friction on the real voidage have been estimated. Results indicated a 0.995 voidage for higher superficial gas velocity of 4.681 m/s. En ligne : http://pubs.acs.org/doi/abs/10.1021/ie800282f [article] Voidage and pressure profile characteristics of sand-iron ore−coal−FCC single-particle systems in the riser of a pilot plant circulating fluidized bed [texte imprimé] / M. Das, Auteur ; B. C. Meikap, Auteur ; R. K. Saha, Auteur . - 2008 . - p. 4018–4024. Bibliogr. p. 4024 Langues : Anglais (eng) in Industrial & engineering chemistry research > Vol. 47 n°11 (Juin 2008) . - p. 4018–4024 Mots-clés : Single-particle systems  Circulating fluidized bed  Iron ore  Coal Résumé : Hydrodynamic behaviors of single system of particles were investigated in a circulating fluidized bed (CFB) unit. Particles belonging to Geldart groups A and B like sand of various sizes (80, 300, 417, 522, 599, and 622 μm), FCC catalyst (120 μm), iron ore (166 and 140 μm), and coal (335 and 168 μm) were used to study the hydrodynamic characteristics. Superficial air velocity used in the present study ranged between 2.01 and 4.681 m/s and corresponding mass fluxes were 12.5−50 kg/(m2 s). A CFB needs the creation of some special hydrodynamic conditions, namely a certain combination of superficial gas velocity, solids circulation rate, particle diameter, density of particle, etc. which can give rise to a state wherein the solid particles are subjected to an upward velocity greater than the terminal or free fall velocity of the majority of the individual particles. The hydrodynamics of the bed was investigated in depth and theoretical analysis is presented to support the findings. Based on gas−solid momentum balance in the riser, a distinction between apparent and real voidage has been made. The effects of acceleration and friction on the real voidage have been estimated. Results indicated a 0.995 voidage for higher superficial gas velocity of 4.681 m/s. En ligne : http://pubs.acs.org/doi/abs/10.1021/ie800282f

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