Robust sliding mode‐based extremum‐seeking controller for reaction systems via uncertainty estimation approach

"This paper deals with the design of a robust sliding mode‐based extremum‐seeking controller aimed at the online optimization of a class of uncertain reaction systems. The design methodology is based on an input–output linearizing method with variable‐structure feedback, such that the closed‐lo...

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Detalles Bibliográficos
Autores: GERARDO LARA CISNEROS, ALEJANDRO RICARDO FEMAT FLORES, Denis Dochain
Tipo de recurso: artículo
Estado:Versión aceptada para publicación
Fecha de publicación:2017
País:México
Institución:Instituto Potosino de Investigación Científica y Tecnológica
Repositorio:Repositorio Institucional del IPICYT
OAI Identifier:oai:ipicyt.repositorioinstitucional.mx:1010/1655
Acceso en línea:http://ipicyt.repositorioinstitucional.mx/jspui/handle/1010/1655
Access Level:acceso abierto
Palabra clave:info:eu-repo/classification/Autor/Extremum-seeking control
info:eu-repo/classification/Autor/(Bio)chemical reactors
info:eu-repo/classification/Autor/Sliding mode control
info:eu-repo/classification/Autor/Uncertain reactionsystems
info:eu-repo/classification/cti/1
info:eu-repo/classification/cti/12
Descripción
Sumario:"This paper deals with the design of a robust sliding mode‐based extremum‐seeking controller aimed at the online optimization of a class of uncertain reaction systems. The design methodology is based on an input–output linearizing method with variable‐structure feedback, such that the closed‐loop system converges to a neighborhood of the optimal set point with sliding mode motion. In contrast with previous extremum‐seeking control algorithms, the control scheme includes a dynamic modelling‐error estimator to compensate for unknown terms related with model uncertainties and unmeasured disturbances. The proposed online optimization scheme does not make use of a dither signal or a gradient‐based optimization algorithm. Practical stabilizability for the closed‐loop system around to the unknown optimal set point is analyzed. Numerical experiments for two nonlinear processes illustrate the effectiveness of the proposed robust control scheme."