Abstract
Detailed local flow structures are investigated in bubbling and turbulent fluidized bed with FCC particles. The operating conditions ranges from 0.06 to 1.4 m/s. Extensive experiments are carried out using a newly developed optical fiber probe system, which can measure the solids concentration and velocity at multi-points. The results reveal that with increasing Ug, local solids concentrations go through three evolution stages, reflecting a gradual regime transition process. Under all operating conditions, upflowing and descending particles co-exist at all measuring locations. The upflowing particle velocity is strong function of both superficial gas velocity and spatial position. However, the descending particle velocity mainly depends on superficial gas velocity. The bed radial symmetry and the effects of static bed height on the local flow structures are also investigated.
Original language | English |
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Pages (from-to) | 339-349 |
Number of pages | 11 |
Journal | Powder Technology |
Volume | 180 |
Issue number | 3 |
DOIs | |
Publication status | Published - 22 Jan 2008 |
Externally published | Yes |
Keywords
- Dynamic two-phase flow structure
- Particle velocity
- Radial symmetry
- Solids concentration
- Turbulent fluidized bed
ASJC Scopus subject areas
- General Chemical Engineering