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The smaller size particle, the more bed porosity and heat transfer.
The bed porosity data fitted well with Richardson Zaki equation with an exponent of 2.53.
At the same time, the grain size and OLV should provide fluidised bed porosity of above 0.58 0.78.
At the same time the grain size and OLR should provide the value of fluidized bed porosity more than 0.6.
The bed porosity was determined by the subtraction of one and the ratio between the true density and apparent density.
The bed permeability and coordination number are determined by both the bed porosity and the particle shape.
These differences were associated with significant differences in the dead fuel proportion and fuel bed porosity between recruitment strategies.
The effect of the bed porosity distribution and particle size to the simulation results is also discussed.
Mass transfer characteristic parameters are also correlated with liquid flow, particle size and bed porosity.
Moreover, application of uniform bed porosity can predict the hydrodynamics parameters under cyclic operations.
The bed porosity has been described with the pseudo-fluid model.
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