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Bed height at minimum fluidizing conditions (m).
Bed voidage at minimum fluidizing conditions.
Height at minimum fluidizing conditions is calculated by the correlation given by McAuley et al. [5].
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Reynolds number at minimum fluidizing condition.
These transfer coefficients were then used to calculate jd, mass transfer factors, for this fluidized bed system and also the product jdRef which has been found to depend on Remf, the corresponding Reynolds number at minimum fluidization conditions.
The behaviour of a gas solid flow in a bubbling fluidized bed operated near the minimum fluidization condition is strongly influenced by the frictional stresses between the particles, these being highly concentrated and their motion dominated by enduring contact among them and with the walls.
The results indicated that a lower bed pressure drop (without considering lower gas velocity in a fixed bed stage) and higher minimum fluidized velocity are achieved with increasing agitation speed.
Minimum fluidization velocity, fluidizing behavior and adsorption/desorption properties of the sorbent particles were determined in a laboratory scale fluidized bed reactor (i.d., 0.03 m) in the temperature range up to 1073 K.
Therefore the minimum fluidization air velocity to fluidize the sand particles and pressure drop are crucial hydrodynamic parameters for analysing the operation and design of fluidized bed combustors.
In the case of the fluidized bed, the minimum fluidization velocity (0.086 m/s) and minimum bubbling velocity (0.12 m/s) were also identified on the basis of the well-pronounced local minima in the profiles of the new parameters.
A predicting correlation for the minimum fluidization velocity in a supercritical water fluidized bed was obtained based on the experimental results of a fixed bed and the fluidized bed pressure drop.
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