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dc.contributor.authorEigenberger, Gerhartde
dc.contributor.authorNieken, Ulrichde
dc.date.accessioned2010-04-08de
dc.date.accessioned2016-03-31T07:52:42Z-
dc.date.available2010-04-08de
dc.date.available2016-03-31T07:52:42Z-
dc.date.issued1994de
dc.identifier.other321898400de
dc.identifier.urihttp://nbn-resolving.de/urn:nbn:de:bsz:93-opus-51802de
dc.identifier.urihttp://elib.uni-stuttgart.de/handle/11682/1885-
dc.identifier.urihttp://dx.doi.org/10.18419/opus-1868-
dc.description.abstractIntegration of regenerative heat exchange into a catalyst bed enables auto-thermal operation of catalytic purification of polluted air with a low content of combustible pollutants. Concentrations corresponding to an adiabatic temperature rise of less than 20°C can be handled without introduction of additional fuel. For higher concentrations, a technique involving side-stream withdrawal allows utilization of the total heat of combustion at the highest reactor temperature. Heat recovery by integrated heat exchange gives rise to an unusual behavior of the reactor. Based upon an analogy to fixed-bed reactors with integrated countercurrent heat exchange, simple equations are derived for reactor design and operation. Substantial reduction in pressure loss and in the volume of the packed bed can be obtained by replacing conventional catalyst packings by monolithic catalysts. The corresponding relationships are briefly discussed.en
dc.language.isoende
dc.rightsinfo:eu-repo/semantics/openAccessde
dc.subject.classificationKatalysator , Abluftreinigungde
dc.subject.ddc660de
dc.titleCatalytic cleaning of polluted air : reaction engineering problems and new solutionsen
dc.typearticlede
dc.date.updated2014-10-16de
ubs.fakultaetFakultät Energie-, Verfahrens- und Biotechnikde
ubs.institutInstitut für Chemische Verfahrenstechnikde
ubs.opusid5180de
ubs.publikation.sourceInternational chemical engineering 34 (1994), S. 4-16de
ubs.publikation.typZeitschriftenartikelde
Enthalten in den Sammlungen:04 Fakultät Energie-, Verfahrens- und Biotechnik

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