Abstract:A spatiotemporal metabolic model of a representative syngas bubble-column reactor was applied to design and evaluate dynamic matrix control (DMC) schemes for regulation of the desired by-product ethanol and the undesired by-product acetate. This model was used to develop linear step response models for controller design and also served as the process in closed-loop simulations. A 2 2 DMC scheme with manipulation of the liquid and gas feed flows to the column provided a superior performance to proportional inte… Show more
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