| Authors |
: |
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| Document type |
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Article de périodique (Journal article) – Article de recherche
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| Abstract |
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We consider input constrained adaptive output feedback control for
exothermic chemical tubular reactor with axial dispersion. we use a non linear
distributed parameter model with boundary control for both the evolution of the
temperature and concentration. Our objective is the set point control of the output
i.e, the temperature of the reaction. Practical consideration lead us to work in the
presence of input constraints. we apply a λ-tracking controller, we show that for
all initial temperature and under a simple feasibility assumptions that the tracking
error tends asymptotically to a ball centred at the reference temperature and of
arbitrary prescribed radius λ |
| Access type |
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Accès restreint |
| Publication date |
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2007 |
| Language |
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Anglais |
| Journal information |
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"International Journal of Tomography & Statistics" - Vol. 6, no. S07, p. 80-85 (2007) |
| Peer reviewed |
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yes |
| Publisher |
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Centre for Environment, Social and Economic Research (CESER) Publications |
| issn |
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0972-9976 |
| e-issn |
: |
0973-7294 |
| Publication status |
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Publié |
| Affiliations |
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Université d'El Jadida
- Département de Mathématiques
UCL
- FSA/MAPR - Département des sciences des matériaux et des procédés
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| Keywords |
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Adaptive control ; nonlinear distributed parameter models ; exothermic chemical reaction ; input saturations ; non isothermal tubular reactor
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| Links |
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