Fluidized Bed Catalytic Reactor with Consecutive Reactions

5 Fluidized Bed Catalytic Reactor with Consecutive Reactions 

The procedure used in the previous section to develop a mathematical model for a catalytic bubbling fluidized bed reactor with a simple reaction A — B can be extended to develop a model for the practically important consecutive reaction A —U B C, where B is the desired product. 

M = temperature measurment PC = proportional controller j = input feed temperature 

Ym = set point which is usually the middle saddle type steady state temperature. 

Using the usual assumptions, we obtain the following dimensionless unsteady-state material and energy balance equations for the dense (emulsion) phase of the bubbling fluidized bed  

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Numerical Treatment of the Steady-State and Dynamical Cases of the Bubbling Fluidized Bed Catalytic Reactor with Consecutive Reactions... 

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