2009
DOI: 10.1016/j.cep.2009.09.004
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CFD simulation of gas–solid flow in a spouted bed with a non-porous draft tube

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Cited by 52 publications
(32 citation statements)
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“…Despite these disadvantages, the nonporous draft tube is the suitable technology when particle history needs to be tracked. Nevertheless, it is not the right option when the gas plays an active role, as in drying processes [41].…”
Section: Resultsmentioning
confidence: 99%
“…Despite these disadvantages, the nonporous draft tube is the suitable technology when particle history needs to be tracked. Nevertheless, it is not the right option when the gas plays an active role, as in drying processes [41].…”
Section: Resultsmentioning
confidence: 99%
“…In the past numerous investigations were performed and the influence of the hydrodynamics parameters such as drag function [21][22][23][24][25], particle viscosity model [24,25], particle-particle restitution coefficient [24][25][26], particle-wall restitution coefficient, and specularity coefficient [27][28][29] on the CFD results of the spouted beds were investigated. In the present study, the optimized values of hydrodynamics parameters that were obtained in our earlier work [30] were used and the effect of the RDF on the CFD results for the 2D spouted beds was evaluated.…”
Section: Introductionmentioning
confidence: 99%
“…Although numerous CFD studies on the hydrodynamics of fluidized and spouted beds were reported in the literature [11][12][13][14][15][16][17][18][19][20][21][22][23][24][25][26], very few if any investigations includes the heat transfer in the spouted beds. For many applications of spouted beds such as drying equipment, chemical reactors, and biological processes, knowledge of temperature distribution is critical.…”
Section: Introductionmentioning
confidence: 99%