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dc.contributor.authorBrandstädter, Willi Michael*
dc.date.accessioned2021-02-11T22:14:44Z
dc.date.available2021-02-11T22:14:44Z
dc.date.issued2008*
dc.date.submitted2019-07-30 20:02:01*
dc.identifier35448*
dc.identifier.urihttps://directory.doabooks.org/handle/20.500.12854/55713
dc.description.abstractThe utilisation of the C4 streams of steamcrackers by converting raffinate II to maleic anhydride was studied. The oxidation reactions were investigated in a laboratory-scale fixed-bed reactor to determine reaction kinetics. The effects of pore diffusional resistance were investigated and explained. A two-dimensional pseudo-homogeneous reactor model was used for the simulation of a production-scale fixed-bed reactor. A flow scheme of the reactor section including a recycle was proposed.*
dc.languageEnglish*
dc.subjectTP155-156*
dc.subject.otherReaction Kinetics*
dc.subject.otherPartial Oxidation*
dc.subject.otherRaffinate II*
dc.subject.otherReactor Simulation*
dc.subject.otherMaleic Anhydride*
dc.titlePartial oxidation of Raffinate II and other mixtures of n-Butane and n-Butenes to maleic anhydride in a fixed-bed reactor*
dc.typebook
oapen.identifier.doi10.5445/KSP/1000007336*
oapen.relation.isPublishedBy68fffc18-8f7b-44fa-ac7e-0b7d7d979bd2*
virtual.oapen_relation_isPublishedBy.publisher_nameKIT Scientific Publishing
virtual.oapen_relation_isPublishedBy.publisher_websitehttp://www.ksp.kit.edu/
oapen.relation.isbn9783866441996*
oapen.pagesVI, 186 p.*


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