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Please use this identifier to cite or link to this item: http://eprint.iitd.ac.in/handle/2074/841

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DC FieldValueLanguage
dc.contributor.authorKundua, Arunabha-
dc.contributor.authorSaroha, Anil K-
dc.contributor.authorNigama, K D P-
dc.date.accessioned2005-09-17T07:12:54Z-
dc.date.available2005-09-17T07:12:54Z-
dc.date.issued2001-
dc.identifier.citationChemical Engineering Science, 56(21-22), 5963–5967en
dc.identifier.urihttp://eprint.iitd.ac.in/dspace/handle/2074/841-
dc.description.abstractLiquid distribution plays an important role in determining the reactor performance in a trickle-bed reactor. Radial liquid distribution was studied in a trickle-bed reactor with five different shapes and sizes of catalyst packing in a uniformly distributed liquid inlet. The liquid tends to flow preferentially along the existing filaments where the porosity is high. The introduction of gas flow into the liquid–solid system smoothens the liquid distribution to some extent due to the competition between liquid and gas phases for the interstitial pore space.en
dc.format.extent361324 bytes-
dc.format.mimetypeapplication/pdf-
dc.language.isoenen
dc.subjectTrickle-bed reactoren
dc.subjectCatalyst packingen
dc.subjectLiquid distributionen
dc.subjectUniform distributoren
dc.subjectWall fiowen
dc.subjectSphericity factoren
dc.titleLiquid distribution studies in trickle-bed reactorsen
dc.typeArticleen
Appears in Collections:Chemical Engineering

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