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- Fluidization: Fundamentals
- (89g) Issues and Solutions in Deep Fluidized Bed Startup
The fluidized bed used in this study consists of a main vessel with a diameter of 7-ft (2.13 m) and a height of 26-ft (7.92 m), a standpipe with a diameter of 3-ft (0.91 m) and a height of 64-ft (19.50 m), and a riser that is 1-ft (0.30 m) in diameter and 96-ft (29.26 m) tall. The bed is equipped with multiple differential pressure transducers (Honeywell and Rockwell) to monitor density in the three sections of the fluidized bed: the main vessel, standpipe, and riser.
This research presents examples of startup challenges in tall, fluidized beds, their consequences, and strategies to address stagnant sections during startup. Specifically, the study explores methods for mitigating startup issues in deep fluidized beds containing Geldart Group A powders by introducing additional aeration ports. These ports are activated only during startup and are switched off once the bed or standpipe is fully fluidized. Additionally, the findings suggest that a fluidized bed can sometimes operate with a partially plugged plenum, but the issue may not be fully resolved until all solids are drained from the system.