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dc.creatorArsenijević, Zorana
dc.creatorGrbić, Boško
dc.creatorRadić, Nenad
dc.creatorGrbavčić, Željko
dc.date.accessioned2019-01-30T17:14:31Z
dc.date.available2019-01-30T17:14:31Z
dc.date.issued2006
dc.identifier.issn1385-8947
dc.identifier.urihttp://cer.ihtm.bg.ac.rs/handle/123456789/263
dc.description.abstractInvestigations of catalytic incineration of ethylene oxide (ETO) over Pt/Al2O3 catalyst have been conducted on laboratory and pilot scale level. The measurements of the reaction rate conducted under gradientless conditions have been used to evaluate kinetics parameters valuable for reactor modeling. A reactor model is proposed which could a priori predict behavior of catalytic convertor under various operating conditions (inlet temperature, inlet pollutant concentration and space velocity) based on the kinetics parameters and mass and energy balances. The results show satisfactory agreement between predicted and experimental values of conversion and temperature profiles along the catalyst bed.en
dc.publisherElsevier Science Sa, Lausanne
dc.rightsrestrictedAccess
dc.sourceChemical Engineering Journal
dc.subjectPt/Al2O3 catalysten
dc.subjectethylene oxideen
dc.subjectcatalytic oxidationen
dc.subjectkineticsen
dc.subjectreactor modelen
dc.titleCatalytic incineration of ethylene oxide in the packed bed reactoren
dc.typearticle
dc.rights.licenseARR
dcterms.abstractГрбавциц, ЛБ; Aрсенијевић, Зорана; Грбић, Бошко; Радић, Ненад;
dc.citation.volume116
dc.citation.issue3
dc.citation.spage173
dc.citation.epage178
dc.citation.other116(3): 173-178
dc.citation.rankM21
dc.identifier.doi10.1016/j.cej.2005.11.007
dc.identifier.rcubConv_2351
dc.identifier.scopus2-s2.0-32144442001
dc.identifier.wos000235644200003
dc.type.versionpublishedVersion


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