Abstract
In this work, the optimization of a monolith reactor 3-dimensional model is carried out, for a first order reaction, isothermal conditions and fully developed laminar flow. The obtained results are consistent with the optimal reactor design obtained under plug flow conditions, namely a maximum conversion reactor features maximum channel width, minimum hydraulic diameter, and maximum fluid velocity determined by an upper bound that is a function of the channel’s width, height, and the capital cost to compression cost ratio.
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