4.7 Article

Hydrodynamics in the transport zone of a large-scale circulating fluidized bed boiler

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POWDER TECHNOLOGY
卷 414, 期 -, 页码 -

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ELSEVIER
DOI: 10.1016/j.powtec.2022.118099

关键词

Fluidized bed; Hydrodynamics; Fast fluidization; Elutriation; Riser diameter

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Five field tests were conducted to measure the pressure drops in the transport zone of a 550-MWe CFB boiler in order to investigate its hydrodynamics. The calculated circulating rates Gs were compared with estimations based on elutriation constant and saturation-carrying capacity theories, showing good agreement for the elutriation constant but discrepancies for the saturation-carrying capacity. The effect of riser diameter on Gs was discussed, indicating an independence of the circulating rate beyond a certain dimension.
To investigate the hydrodynamics in large-scale CFB boilers, the pressure drops in the transport zone of a 550-MWe CFB boiler were measured by conducting five field tests. The circulating rates Gs were calculated based on the pressure drop in the transport zone and then compared with the estimations via the correlations of the elutriation constant in single-particle elutriation theory and those of the saturation-carrying capacity in fast fluidization theory. The Colakyan & Levenspiel correlation of elutriation constant exhibited a good agreement with the experiments within +/- 14.02% error range. It's reasonable to use it for calculating Gs in large-scale CFB boilers because of its wide experimental conditions. The flow regime remained uncertain due to the discrepancies in the saturation-carrying capacity estimated by different correlations. The effect of riser diameter on Gs was discussed, including the dimension of Dt, ind, beyond which the circulating rate was suggested to be independent of the riser diameter.

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