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dc.contributor.authorEigenberger, Gerhartde
dc.contributor.authorSchuler, Hansde
dc.date.accessioned2009-12-18de
dc.date.accessioned2016-03-31T07:52:36Z-
dc.date.available2009-12-18de
dc.date.available2016-03-31T07:52:36Z-
dc.date.issued1989de
dc.identifier.other318572672de
dc.identifier.urihttp://nbn-resolving.de/urn:nbn:de:bsz:93-opus-48985de
dc.identifier.urihttp://elib.uni-stuttgart.de/handle/11682/1866-
dc.identifier.urihttp://dx.doi.org/10.18419/opus-1849-
dc.description.abstractStable operation of a chemical reactor and stability (in the stability-theory sense) of a chemical process are not necessarily synonymous concepts. Thus, appropriate control can permit reliable operation at an unstable operating point, while even global stability does not necessarily rule out a runaway reaction, e.g., when a strongly exothermlc reaction has a pronounced parametric sensitivity. The concepts of stability and parametric sensitivity are explained in relation to strongly exothermic reactions in stirred-tank and tubular reactors. The conventional view of reaction engineering and the theory of thermal explosions, commonly used in safety engineering, are considered in detail. Practical problems of safe reaction engineering are discussed in relationship to the control of batch and semibatch reactors and to the behavior of tube-bundle reactors.en
dc.language.isoende
dc.rightsinfo:eu-repo/semantics/openAccessde
dc.subject.classificationChemischer Reaktor , Stabilität , Sicherheitstechnikde
dc.subject.ddc660de
dc.titleReactor stability and safe reaction engineeringen
dc.typearticlede
dc.date.updated2014-10-16de
ubs.fakultaetFakultät Energie-, Verfahrens- und Biotechnikde
ubs.fakultaetFakultätsübergreifend / Sonstige Einrichtungde
ubs.institutInstitut für Chemische Verfahrenstechnikde
ubs.institutSonstige Einrichtungde
ubs.opusid4898de
ubs.publikation.sourceInternational chemical engineering 29 (1989), S. 12-25de
ubs.publikation.typZeitschriftenartikelde
Enthalten in den Sammlungen:04 Fakultät Energie-, Verfahrens- und Biotechnik

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