Please use this identifier to cite or link to this item: http://nopr.niscair.res.in/handle/123456789/1152
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dc.contributor.author(Bose), S Das-
dc.contributor.authorSaha, R K-
dc.contributor.authorGupta, P Sen-
dc.date.accessioned2008-04-24T07:20:51Z-
dc.date.available2008-04-24T07:20:51Z-
dc.date.issued2007-09-
dc.identifier.issn0971–457X-
dc.identifier.urihttp://hdl.handle.net/123456789/1152-
dc.description473-480en_US
dc.description.abstractFluidized bed catalytic cracking is an important secondary process in a modern refinery. Unlike in western countries Indian refineries are often operated in distillate mode requiring design modifications and changes in operating conditions. Riser hydrodynamics together with cracking kinetics are often very useful to simulate the performance of FCC riser reactor and accurately predict conversion of the process. The present paper reports the experimental data on hydrodynamics of a FCC riser including its pressure and voidage profiles along the riser length in a cold model of the FCC unit assembly. Effects of some operating variables on the riser hydrodynamics have been reported.en_US
dc.language.isoen_USen_US
dc.publisherCSIRen_US
dc.relation.ispartofseriesC10G32/00en_US
dc.sourceIJCT Vol.14(5) [September 2007]en_US
dc.subjectFCC riseren_US
dc.subjectHydrodynamicsen_US
dc.subjectPressure and voidage profilesen_US
dc.subjectConversionen_US
dc.titleFCC riser hydrodynamics: Effect of some operating variablesen_US
dc.typeArticleen_US
Appears in Collections:IJCT Vol.14(5) [September 2007]

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