Abstract
The regime transition velocity from bubbling to turbulent fluidization was investigated in a 0.267 m diameter fluidized bed with FCC particles. Different transition velocities and processes are found from the measurements of differential pressure fluctuations and local solids concentration. The measurements of differential pressure fluctuations shows a relatively quicker global regime transition, while the local regime transition obtained from the local solids concentration presents a more gradual process marked by two transition velocities. These transition velocities increase with initial static bed height. For the same initial static bed height, increasing the spacing between two pressure taps leads to lower pressure fluctuations and the appearance of two transition velocities.
Original language | English |
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Pages (from-to) | 553-562 |
Number of pages | 10 |
Journal | Canadian Journal of Chemical Engineering |
Volume | 86 |
Issue number | 3 |
DOIs | |
Publication status | Published - Jun 2008 |
Externally published | Yes |
Keywords
- Bubbling fluidization
- Differential pressure
- Flow regime transition
- Local solids concentration
- Turbulent fluidization
ASJC Scopus subject areas
- General Chemical Engineering