A Comparative Study of MPC-Based Control Configurations of an Industrial Bioreactor to Produce Ethanol

Romo Hernandez, Aaron;Hernandez-Escoto, Hector;et.al.
(2011) A Comparative Study of MPC-Based Control Configurations of an Industrial Bioreactor to Produce Ethanol — ISBN: [978-0-444-53895-6], p. 828-832, published

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  • Romo Hernandez, AaronUCLouvain
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  • Hernandez-Escoto, HectorUniversidad de Guanajuato
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  • et. al.
Abstract
For a class of continuous stirred tank bioreactors to produce ethanol at large scale, this work evaluates suitable control configurations in a model predictive control framework. The study makes several assumptions, including a non-square plant, a distinction between control and output variables, and the possible sets of available outputs. Since the outputs are obtained in a discrete form, also the effect of the sampling interval was evaluated. Operational-feasible configurations are discussed. Herein, it is highlighted that a conventional configuration of one input-one control variable driven by one output, is the best to maintain all the three states around their nominal values.
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Romo Hernandez, A., Hernandez-Escoto, H., & et al. (2011). A Comparative Study of MPC-Based Control Configurations of an Industrial Bioreactor to Produce Ethanol. In Aarón Romo-Hernández, SalvadorHernández, Arturo Sánchez, Héctor Hernández-Escoto (ed.), A Comparative Study of MPC-Based Control Configurations of an Industrial Bioreactor to Produce Ethanol (p. p. 828-832). E.N. Pistikopoulos, M.C. Georgiadis, A.C. Kokossis. https://doi.org/10.1016/B978-0-444-53711-9.50166-8