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dc.contributor.authorKremling, Andreasde
dc.contributor.authorAllgöwer, Frankde
dc.date.accessioned2011-03-30de
dc.date.accessioned2016-03-31T11:43:26Z-
dc.date.available2011-03-30de
dc.date.available2016-03-31T11:43:26Z-
dc.date.issued1994de
dc.identifier.other367352974de
dc.identifier.urihttp://nbn-resolving.de/urn:nbn:de:bsz:93-opus-62362de
dc.identifier.urihttp://elib.uni-stuttgart.de/handle/11682/7522-
dc.identifier.urihttp://dx.doi.org/10.18419/opus-7505-
dc.description.abstractCatalytic fixed bed reactors exhibit interesting control problems due to their nonlinear behaviour and their sensitivity to load changes and other disturbances. Because detailed nonlinear models of such reactors are too complex for use in controller design, a linear model description is identified here along with an appropriate structured uncertainty description. The controller is designed based on the μ-paradigm to guarantee robust stability and robust performance. A comparison with an H∞-optimal controller is also given. For the H∞-design the structured uncertainties are converted into a single multivariable unstructured uncertainty. As expected the H∞-controller can only achieve a much less demanding performance because of the conservatism of the unstructured uncertainty description. Experimental results involving a real reactor are given.en
dc.language.isoende
dc.rightsinfo:eu-repo/semantics/openAccessde
dc.subject.classificationNichtlineares dynamisches System , Chemische Verfahrenstechnik , Kontrollsystemde
dc.subject.ddc620de
dc.titleRobust control of a catalytic fixed bed reactoren
dc.typeconferenceObjectde
dc.date.updated2011-03-30de
ubs.fakultaetFakultätsübergreifend / Sonstige Einrichtungde
ubs.institutSonstige Einrichtungde
ubs.opusid6236de
ubs.publikation.sourceProceedings of the 33rd IEEE Conference on Decision and Control. Vol. 2. Piscataway, NJ : IEEE Service Center, 1994, S. 1098-1104de
ubs.publikation.typKonferenzbeitragde
Enthalten in den Sammlungen:15 Fakultätsübergreifend / Sonstige Einrichtung

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