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Simulation and design of fluid-catalytic cracking riser-type reactors

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dc.contributor.author Theologos, KN en
dc.contributor.author Nikou, ID en
dc.contributor.author Lygeros, AI en
dc.contributor.author Markatos, NC en
dc.date.accessioned 2014-03-01T01:12:16Z
dc.date.available 2014-03-01T01:12:16Z
dc.date.issued 1996 en
dc.identifier.issn 0098-1354 en
dc.identifier.uri https://dspace.lib.ntua.gr/xmlui/handle/123456789/12044
dc.subject Computation Fluid Dynamics en
dc.subject Heat Transfer en
dc.subject Primary Production en
dc.subject Reaction Kinetics en
dc.subject Two Phase Flow en
dc.subject Fluid Catalytic Cracking en
dc.subject.classification Computer Science, Interdisciplinary Applications en
dc.subject.classification Engineering, Chemical en
dc.subject.other Catalytic cracking en
dc.subject.other Chemical reactions en
dc.subject.other Computational fluid dynamics en
dc.subject.other Design en
dc.subject.other Heat transfer en
dc.subject.other Nozzles en
dc.subject.other Simulation en
dc.subject.other Two phase flow en
dc.subject.other Feed injection operating nozzles en
dc.subject.other Fluid-catalytic cracking en
dc.subject.other Riser-type reactor en
dc.subject.other Chemical reactors en
dc.title Simulation and design of fluid-catalytic cracking riser-type reactors en
heal.type journalArticle en
heal.identifier.primary 10.1016/0098-1354(96)00134-2 en
heal.identifier.secondary http://dx.doi.org/10.1016/0098-1354(96)00134-2 en
heal.language English en
heal.publicationDate 1996 en
heal.abstract Two-phase flow, heat transfer and reaction in Fluid Catalytic Cracking riser-type reactors is studied using 3-D Computational Fluid Dynamics techniques. A model already presented in the literature (Theologos and Markatos, 1993) is further developed to incorporate a detailed 10-lump reaction kinetics scheme and account for feedstock gradual vaporization inside the reactor. A design study is carried out to illustrate that developed model is capable of predicting feed injector geometry effects on overall reactor performance. It is predicted that, by increasing the number of feed injection operating nozzles at the bottom of the reactor, selectivity to primary products is improved. en
heal.publisher PERGAMON-ELSEVIER SCIENCE LTD en
heal.journalName Computers and Chemical Engineering en
dc.identifier.doi 10.1016/0098-1354(96)00134-2 en
dc.identifier.isi ISI:A1996UR30900126 en
dc.identifier.volume 20 en
dc.identifier.issue SUPPL.1 en
dc.identifier.spage S757 en
dc.identifier.epage S762 en


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