Industrial & Engineering Chemistry Research · 1998 · 23 citations · 9 references
EngineeringPetroleum EngineeringFluid DynamicsFluid MechanicsTransport PhenomenaMarine RisersRiser SystemsCatalytic CrackingCross-sectional Void FractionFluidizationHydrodynamicsOperating ConditionsRiser DynamicsRiser Flow DynamicsRiser Hydrodynamics
On the basis of the benchmark modeling exercise at Fluidization VIII, predicting riser hydrodynamics continues to be more of an art than a science. Ten different hydrodynamic models were compared with a set of experimental data that covered a wide range of operating conditions and showed reasonable to poor overall agreement. Herein, we describe the model that gave the best overall agreement with the experimental data. Density is calculated by a correlation based on slip factor, and the radial voidage profile depends solely on the cross-sectional average void fraction. Both the gas and velocity profile follows a power law type expression; the gas velocity at the wall is zero. The model predictions agree well with experiments conducted with sand but not as well as those conducted with fluidized catalytic cracking catalyst.
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Scaling considerations for circulating fluidized bed risers
Gregory S. Patience, Jamal Chaouki, Franco Berruti et al. · Powder Technology · 1992 · 120 citations
Engineering, Physics, Fluid Dynamics +10
Gas and solid behavior in cracking circulating fluidized beds
M.P. Martin, P. Turlier, J.R. Bernard et al. · Powder Technology · 1992 · 89 citations
Engineering, Chemical Engineering, Mechanical Engineering +10
Similar profiles of solid flux in circulating fluidized-bed risers
Martin Rhodes, Xiaosuo Wang, Hui Cheng et al. · Chemical Engineering Science · 1992 · 86 citations
Engineering, Physics, Fluid Dynamics +12