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Research, development and design of fluidized bed reactors has been focused towards achieving a better understanding of the behaviour of the bed material during the combustion process.
Discrepancies among the models in predicting the dynamics behaviour of the bed and the bubble formation are, however, observed.
Here, we illustrate this method using 420 500 μm glass ballotini and examine the behaviour of the bed for different quantities of fluidized material.
The fluidization index, bed expansion, torque and visual behaviour of the bed are determined as a function of air velocity, bed height and moisture content of the starch, stirrer type and speed and vibration frequency and amplitude.
The unusual mating behaviour of the bed bug, with traumatic insemination, gives new insights to their chemical communication systems.
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The behaviour of the beds tested at hot flow conditions is compared with that of identical beds tested at ambient conditions using toluene as liquid feed and the effect of liquid-phase properties is discussed.
The dynamic behaviour of the adsorption bed was evaluated by performing breakthrough experiments.
For many carbons it is now possible to discuss the instantaneous voltage behaviour of the GAC bed under these conditions.
The new model is able to predict with great accuracy the behaviour of the fixed bed reactor and represents an interesting tool for scale-up and process design.
Granules with different characteristics (yield stress and initial porosity) are studied, and the relationship between the single-granule properties and the global compression behaviour of the granule bed is investigated.
The boundary conditions on the walls are found to have a large influence on the segregation behaviour of the fluidised bed, where no-slip conditions result in unrealistic flow patterns.
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