one-dimensional model for the riser section of a circulating fluidised bed has been developed which describes the steady-state hydrodynamic key variables in the radial direction for fully developed axisymmetric flow. Both the gas and the solid phase are considered as two continuous media, fully pene
A circulating liquid fluidised bed
โ Scribed by L.G. Gibilaro; R. Di Felice; P.U. Foscolo
- Publisher
- Elsevier Science
- Year
- 1988
- Tongue
- English
- Weight
- 286 KB
- Volume
- 43
- Category
- Article
- ISSN
- 0009-2509
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๐ SIMILAR VOLUMES
An experimental study on the gas dispersion behaviour of a cocurrent downflow gas-solids suspension in a 140 mm i.d. circulating fluidised bed (CDCFB) using the steady-state tracer method is presented. The influence of gas velocity, solids circulating rate and particle density on radial gas dispersi
Shorter Commumcations 137 those presented m Ref [l] The range of values of 4 over which muIt& solutions exist, ti Indeed they do exist, may be located by first computmg the two real roots of T(y) on the Interval I < y C I+ j? and subsequently usmg those roots m eqn (1) to compute duectly the endpomt