Optimization of a Catalytic Microreactor
Model ID: 4401
In this model, a solution is pumped through a catalytic bed where a solute species reacts as it gets in contact with the catalyst. The purpose of the model is to maximize the total reaction rate for a given total pressure difference across the bed by finding an optimal catalyst distribution. The distribution of the porous catalyst determines the total reaction rate in the bed. A large amount of catalyst results in a low flow rate through the bed while less catalyst gives a high flow rate but low conversion of the reactant.
|A 2D surface plot of the velocity field in the open channel.|