Article | REF: BE8255 V1

Fluidized beds - General characterization and applications

Author: Gérard ANTONINI

Publication date: October 10, 2007 | Lire en français

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    3. Gas velocity at fluidization threshold. Bed expansion correlations

    Consider a thick stack of divided solids at rest, resting on a horizontal, porous plate. This forms a fixed bed of interstitial porosity ε 0 , cross-section A and height H 0 .

    If, after crossing the support plate, an upward gas flow is imposed through the bed, the vertical aeraulic force imposed increases with the gas flow rate:

    with :

    U
     : 
    gas velocity in an empty barrel, or surface velocity.

    Above a certain flow rate, this force can compensate for the apparent weight of the particle bed, the inter-particle distance increases and the bed relaxes, its thickness becoming H > H 0...

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    Gas velocity at fluidization threshold. Bed expansion correlations