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Fluid Flow Characteristics of String Reactors Packed with Spherical Particles

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dc.contributor.author Vonortas, A en
dc.contributor.author Hipolito, A en
dc.contributor.author Rolland, M en
dc.contributor.author Boyer, C en
dc.contributor.author Papayannakos, N en
dc.date.accessioned 2014-03-01T01:35:45Z
dc.date.available 2014-03-01T01:35:45Z
dc.date.issued 2011 en
dc.identifier.issn 0930-7516 en
dc.identifier.uri https://dspace.lib.ntua.gr/xmlui/handle/123456789/21176
dc.subject Dispersion en
dc.subject Hydrodynamics en
dc.subject Multiphase flow en
dc.subject Multiphase reactors en
dc.subject String reactors en
dc.subject Structured beds en
dc.subject.classification Engineering, Chemical en
dc.subject.other Controlling parameters en
dc.subject.other Experimental conditions en
dc.subject.other Flow regimes en
dc.subject.other Fluid flow en
dc.subject.other Gas-to-liquid velocity en
dc.subject.other Liquid hold ups en
dc.subject.other Multi-phase reactor en
dc.subject.other Residence time distributions en
dc.subject.other Spherical particle en
dc.subject.other Spiral channel en
dc.subject.other Square channel en
dc.subject.other String reactors en
dc.subject.other Structured beds en
dc.subject.other Tube walls en
dc.subject.other Visual observations en
dc.subject.other Dispersions en
dc.subject.other Hydrodynamics en
dc.subject.other Liquids en
dc.subject.other Multiphase flow en
dc.subject.other Walls (structural partitions) en
dc.subject.other Fluid dynamics en
dc.title Fluid Flow Characteristics of String Reactors Packed with Spherical Particles en
heal.type journalArticle en
heal.identifier.primary 10.1002/ceat.201000165 en
heal.identifier.secondary http://dx.doi.org/10.1002/ceat.201000165 en
heal.language English en
heal.publicationDate 2011 en
heal.abstract A hydrodynamic investigation of three geometries of string pellet reactors filled with spheres was conducted. Two geometries were circular spiral channels, while the third was a straight horizontal square channel. Stimulus-response experiments provided data for residence time distribution analysis from which Pe numbers and liquid holdup were deduced. Flow regimes and transitions were determined from visual observations through the transparent tube wall. For the whole range of the experimental conditions applied in this work and for all reactors, the ratio of gas to liquid velocities, Vg/Vl, is a controlling parameter for Pe number, holdup, and pressure drop. Copyright © 2011 WILEY-VCH Verlag GmbH & Co. KGaA, Weinheim. en
heal.publisher WILEY-BLACKWELL en
heal.journalName Chemical Engineering and Technology en
dc.identifier.doi 10.1002/ceat.201000165 en
dc.identifier.isi ISI:000287786900006 en
dc.identifier.volume 34 en
dc.identifier.issue 2 en
dc.identifier.spage 208 en
dc.identifier.epage 216 en


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