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Heat and mass transfer during drying of granular products – simulation with convective and conductive boundary conditions. (English) Zbl 0968.76085

Summary: Numerical simulation of grain drying in a vertical cylindrical bed has been carried out under specific boundary conditions: evaporation, which occurs with forced air flowing through the bed, is intensified with a conductive heat flux from the wall. We consider two mathematical models of heat and mass transfer through granular medium: two-temperature model (non-local temperature equilibrium model: NLTEModel), and one-temperature model (local temperature equilibrium model: LTEModel). The air-grain mass transfer is expressed with a drying rate equation outcome from experiments. The solution of the equations set is done by using a finite volume method. Different effects, such as the effect of porosity variation on energy and mass transport, are discussed, and sensitivity to external conditions is determined. Finally, we examine the validity of local thermal assumption.

MSC:

76S05 Flows in porous media; filtration; seepage
76R05 Forced convection
76T30 Three or more component flows
80A20 Heat and mass transfer, heat flow (MSC2010)
76T25 Granular flows
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