The Performance Of Drag Models On
Flow Behaviour In The CFD Simulation Of A
Fluidized Bed
Author(s)
B. M. Halvorsen, J. P. du Plessis & S. Woudberg
Abstract
The aim of this study is to verify the use of a newly developed drag model in the
simulation of fluidized beds. The drag model is based on a geometric description
of the geometry found in a fluidised bed, treating it as a spatially and temporally
variable inhomogeneous, locally isotropic, porous medium. Account is taken of
the fact that flow conditions in low porosity parts of a bed can be viewed as flow
between particles. At high porosities the bed resembles flow past the particles of
a dilute assemblage and for that the current model is complemented with results
from other models. The new drag model, as well as other models found in
literature, was tested in the numerical simulations. Computational results are
compared mutually, as well as to experimental data, and the differences and
discrepancies discussed.
Keywords: fluidized bed, numerical simulation, drag model.
1 Introduction
Fluidized beds are widely used in industrial chemical processes. In a fluidized
bed gas is passing upwards through a bed of particles and the earliest
applications of fluidization were for the purpose of enhancing chemical
reactions. Fluidized beds in chemical industry include two main types of
reactions, catalytic gas phase reactions and gas-solid reactions. In catalytic gas
phase reactions the particles are not undergoing any chemical reaction. This is
Keywords
fluidized bed, numerical simulation, drag model.
Related Book
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