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Advanced modeling of riser-type catalytic cracking reactors

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dc.contributor.author Dewachtere, NV en
dc.contributor.author Froment, GF en
dc.contributor.author Vasalos, I en
dc.contributor.author Markatos, N en
dc.contributor.author Skandalis, N en
dc.date.accessioned 2014-03-01T01:12:36Z
dc.date.available 2014-03-01T01:12:36Z
dc.date.issued 1997 en
dc.identifier.issn 13594311 en
dc.identifier.uri https://dspace.lib.ntua.gr/xmlui/handle/123456789/12156
dc.subject Computational fluid dynamics en
dc.subject Energy efficiency en
dc.subject FCC en
dc.subject Riser simulation en
dc.subject Single-event kinetic modeling en
dc.subject.other Computational fluid dynamics en
dc.subject.other Energy efficiency en
dc.subject.other Feedstocks en
dc.subject.other Fluid catalytic cracking en
dc.subject.other Gas chromatography en
dc.subject.other Gas oils en
dc.subject.other Hydrodynamics en
dc.subject.other Liquid chromatography en
dc.subject.other Mass spectrometry en
dc.subject.other Mathematical models en
dc.subject.other Vaporization en
dc.subject.other Catalytic cracking reactors en
dc.subject.other Single event kinetic modeling en
dc.subject.other Chemical reactors en
dc.title Advanced modeling of riser-type catalytic cracking reactors en
heal.type journalArticle en
heal.identifier.primary 10.1016/S1359-4311(96)00074-9 en
heal.identifier.secondary http://dx.doi.org/10.1016/S1359-4311(96)00074-9 en
heal.publicationDate 1997 en
heal.abstract Various aspects of the advanced modeling of riser-type catalytic cracking reactors are discussed in this paper. A new kinetic modeling approach for the catalytic cracking process is introduced, based on carbenium ion chemistry. Single-event kinetic modeling leads to kinetic parameters which are truly invariant of the gas oil feedstock composition. Since the new kinetic modeling approach requires a detailed analysis of the gas oil feedstock, the characterization of heavy petroleum fractions by means of liquid chromatography and GC-MS analysis is briefly discussed. A three-dimensional (3-D) mathematical model for the simulation of a riser reactor is introduced, using computational fluid dynamics techniques. The model includes a detailed hydrodynamic model. Special attention is devoted to the modeling of the inlet zone of the riser, where the gas oil feedstock is vaporized. The 3-D riser model is validated against experimental data from an industrial riser reactor. © European Communities 1997. Published by Elsevier Science Ltd. en
heal.journalName Applied Thermal Engineering en
dc.identifier.doi 10.1016/S1359-4311(96)00074-9 en
dc.identifier.volume 17 en
dc.identifier.issue 8-10 en
dc.identifier.spage 837 en
dc.identifier.epage 844 en


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