The paper outlines and exemplifies a multi-dimensional multi-phase Computational Fluid Dynamics (CFD) model for the various processes that occur in fluidized bed reactors. The model is based on the Eulerian description of the two phases: gas and particles. This means that separate conservation equations are set up for these phases. Calculations are shown for some examples that include flow patterns in circulating beds.
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Hjertager et al. (1992) studied this question.
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