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Typical bed voidage values of 0.49 0.51 (virgin trilobe).
Three simple experiments were used to obtain system delay volume, bed voidage and particle porosity, respectively.
Radial profiles of bed voidage and solid velocity were discussed in detail.
In this context transient bed voidage profiles have been analyzed in detail.
New design equations have been developed for the prediction of bed voidage and heat transfer coefficients.
As a consequence, a bigger bed voidage creates a lower dust collection efficiency in the GBF.
In all cases the particle diameter had a lesser effect on bed voidage compared to PSD width, as wider PSD was associated with a lower bed voidage due to smaller particles filling the spaces between the larger particles.
The particles and the fixed bed structural change were established by the measured particle porosity and the fixed bed voidage.
Others parameters, required to evaluate the bed performance, such as bed voidage and the axial dispersion coefficient, were also determined.
The bed voidage increased with increasing superficial liquid velocities and superficial gas velocities.
The bed was divided into two regions of constant bed voidage and gas velocity.
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