| Article ID | Journal | Published Year | Pages | File Type |
|---|---|---|---|---|
| 661648 | International Journal of Heat and Mass Transfer | 2006 | 11 Pages |
Abstract
A phenomenological model of solids mixing in a circulating fluidized bed is formulated. The characteristic feature of this model is taking into account the convective flows of particles in the radial direction, which provide the observed in practice essential decrease of the concentration of particles over the riser height. It is established by comparison of calculated and experimental curves of mixing that the value of the coefficient of radial dispersion of particles lies within the range 0.0006–0.006 m2/s.
Related Topics
Physical Sciences and Engineering
Chemical Engineering
Fluid Flow and Transfer Processes
Authors
Yu.S. Teplitskii, V.I. Kovenskii, E.F. Nogotov, V.A. Borodulya,