Nonlinear predictive control for the concentrations profile regulation under unknown reaction disturbances in a fuel cell anode gas channel

In this work, a nonlinear model predictive control (NMPC) strategy is proposed to regulate the concentrations of the different gas species inside a Proton Exchange Membrane Fuel Cell (PEMFC) anode gas channel. The purpose of the regulation relies on the rejection of the unmeasurable perturbations th...

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Detalles Bibliográficos
Autores: Luna Pacho, Julio Alberto, Ocampo-Martínez, Carlos|||0000-0001-9251-6044, Serra, Maria|||0000-0002-9885-8093
Tipo de recurso: artículo
Fecha de publicación:2015
País:España
Institución:Universitat Politècnica de Catalunya (UPC)
Repositorio:UPCommons. Portal del coneixement obert de la UPC
Idioma:inglés
OAI Identifier:oai:upcommons.upc.edu:2117/27120
Acceso en línea:https://hdl.handle.net/2117/27120
https://dx.doi.org/10.1016/j.jpowsour.2015.02.033
Access Level:acceso abierto
Palabra clave:PEM fuel cell systems
control nonlinearities
observability
power system control
predictive control. Concentration regulation
distributed model
NMPC
fuel cell control
fuel cell observation
Piles de combustible -- Control electrònic
Àrees temàtiques de la UPC::Informàtica::Automàtica i control
Descripción
Sumario:In this work, a nonlinear model predictive control (NMPC) strategy is proposed to regulate the concentrations of the different gas species inside a Proton Exchange Membrane Fuel Cell (PEMFC) anode gas channel. The purpose of the regulation relies on the rejection of the unmeasurable perturbations that affect the system: the hydrogen reaction and water transport terms. The model of the anode channel is derived from the discretisation of the partial differential equations that define the nonlinear dynamics of the system, taking into account spatial variations along the channel. Forward and backward discretisations of the distributed model are employed to take advantage of the boundary conditions of the problem. A linear observer is designed and implemented to perform output-feedback control of the plant. This information is fed to the controller to regulate the states towards their desired values. Simulation results are presented to show the performance of the proposed control method over a given case study. Different cost functions are compared and the one with minimum state-regulation error is identified. Suitable dynamic responses are obtained facing the different considered disturbances.