Abstract
A new model for catalytic reaction in fluidized beds is developed. This model called the “Bubble Assemblage Model” is based on multiple bubbles of varying sizes with interchange of gas taking place between the bubble phase and the emulsion phase. Since the model needs no adjustable parameters, it is believed that the model is useful for study in scale-ups. The model proposed is also convenient for computer simulations. Experimental data from various investigators were used to test the validity of this model. It was found that the conversions predicted using this model agree reasonably well with the actual performance of the fluidized beds.
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