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The value of minimum fluidization velocity of the pilot-scale bubbling fluidized bed combustor is approximately obtained to be at around 1.0 m/s.
The minimum fluidization velocity, fluidization terminal velocity, and average fluidizing velocity were calculated, in order to understand the fluid-dynamic behaviour of gasification of this fuel.
The predicted simulation results of minimum fluidization velocity and pressure drop values of the pilot-scale bubbling fluidized bed combustor have good agreement with the experimental measurements.
Therefore, the hydrodynamic properties such as the bed pressure drop and minimum fluidization velocity are the most important parameters studied in the numerical modelling of fluidized beds.
At this minimum fluidization velocity the pressure drop remains constant.
Minimum fluidization velocity was determined by measuring pressure drop.
An empirical correlation was developed for determining minimum fluidization velocity.
Experimentally determined minimum fluidization velocity allowed to select the necessary molar flow rate of substrates.
The hydrodynamic characteristics determined include the minimum fluidization velocity, bed fluctuation, and bed expansion ratios.
The results show transient regime in the case of minimum fluidization velocity.
Performances of the new method significantly improves the prediction of minimum fluidization velocity.
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