Static and dynamic bifurcation behaviors dominate the operation of fluidized bed catalytic reactors for the production of polyethylene (UNIPOL Process) and have important implications on the safe operating temperature and polyethylene production rate. The investigations show that the multiplicity of
The effect of particle size and bed height on the expansion of mixed phase (gas—liquid) fluidized beds
✍ Scribed by K. Østergaard; P.I. Theisen
- Publisher
- Elsevier Science
- Year
- 1966
- Tongue
- English
- Weight
- 376 KB
- Volume
- 21
- Category
- Article
- ISSN
- 0009-2509
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✦ Synopsis
The expansion of gas-liquid fluidized beds has been measured for beds of glass ballotini fluidized by air/water. Particle diameters varied from 0.28 to 2.2 mm, and settled bed heights from U-107 cm. The flow rates of air and water were varied independently.
The expansion of a liquid fluidized bed is often reduced when a swarm of gas bubbles is injected into the bed. This bed contraction is largest for beds of small particles; a contraction of 48 per cent has been observed in a highly expanded bed of 0.28 mm ballotini. For small particles the largest contraction was observed in beds of high height to diameter ratio. For larger particles the contraction is less pronounced, and no significant effect of the ratio between bed height and diameter was observed.
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Gas mixing in a 6.5 in fluidized bed of sand was studied using frequency response techniques with He and CO\* tracers. Samples taken in the bed, where the probe saw mainly dense phase gas, had a lower amplitude ratio than samples at the top of the bed where the bubble contribution predominated. The