Particulate Science And Technology · 2016 · 21 citations · 15 references
EngineeringChemical EngineeringPhysicsFluid DynamicsHeat TransferThermodynamicsHeat Transfer ModelingPacked Bed FlowTransport Property SimulationBed ExpansionDrag CoefficientDrag ForceDrying In Fluidized BedsFluidized BedsHeat Transfer In Fluidized BedsModeling Of Fluidization DynamicsThermal Treatment
A one-dimensional mathematical model of particulate solids thermal treatment in a fluidized bed based on the theory of Markov chains is proposed. A feature of the model takes into account the variation of particle properties that takes place during the fluidization. This variation occurs due to thermo-physical and chemical processes that take place during particulate solids treatment in the fluidized bed. These variations affect the particle settling velocity which is the main parameter that forms the bed expansion and local velocity of flow around the particles that strongly influences the thermo-physical and chemical processes in the bed. A generalized correlation for the drag force coefficient is proposed and tested for various materials. It was necessary to have more precise calculation of the particle settling velocity in the model. The model was developed to describe the drying process in the bed. A good correlation between computed and experimental data was achieved.
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A short note on the drag correlation for spheres
Richard Turton, Octave Levenspiel · Powder Technology · 1986 · 436 citations
Engineering, Physics, Fluid Dynamics +13
Transactions of the Institution of Chemical Engineers
Nature · 1924 · 398 citations