A new spouted bed reactor non-isothermal modelling is developed, in which t
he spout, the fountain, and the annulus region are taken into account. The
flow pattern is based on the streamtube formulation with a special approach
for flat-bottomed reactors. Heat transfers are included by means of an het
erogeneous approach. The parameters influence study shows the resolution sc
heme stability. The model results are compared with experimental data from
literature for CO catalytic oxidation on alumina-supported Co3O4. Accurate
predictions of bed temperature level and conversion are achieved. (C) 1999
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