Effect of Internal Filtration on Slurry Reactor Performance
In slurry bubble column reactors, generally small particles (
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| Veröffentlicht in: | Industrial & engineering chemistry research 1999-01, Vol.38 (1), p.98-107 |
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| container_title | Industrial & engineering chemistry research |
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| creator | Huizenga, Piet Kuipers, Johannes A. M van Swaaij, Wim P. M |
| description | In slurry bubble column reactors, generally small particles ( |
| doi_str_mv | 10.1021/ie980294l |
| format | Article |
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Experimentally observed drops in conversion rate on an increase of permeate flux can mainly be attributed to reduced bulk reactivity caused by cake formation. Chemical reaction in the cake itself increased the conversion rate significantly in the case where a large fraction of the catalyst moved into the cake at high permeate fluxes. Our calculations revealed that hot-spot formation in the cake does not occur for a large number of systems of practical relevance including the present one.</description><identifier>ISSN: 0888-5885</identifier><identifier>EISSN: 1520-5045</identifier><identifier>DOI: 10.1021/ie980294l</identifier><identifier>CODEN: IECRED</identifier><language>eng</language><publisher>Washington, DC: American Chemical Society</publisher><subject>Applied sciences ; Chemical engineering ; Exact sciences and technology ; Reactors</subject><ispartof>Industrial & engineering chemistry research, 1999-01, Vol.38 (1), p.98-107</ispartof><rights>Copyright © 1999 American Chemical Society</rights><rights>1999 INIST-CNRS</rights><lds50>peer_reviewed</lds50><oa>free_for_read</oa><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-a462t-2c72b47acc465a5f51c0daeff8135c23bd5e429d027d62331066c1691054e69b3</citedby><cites>FETCH-LOGICAL-a462t-2c72b47acc465a5f51c0daeff8135c23bd5e429d027d62331066c1691054e69b3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://pubs.acs.org/doi/pdf/10.1021/ie980294l$$EPDF$$P50$$Gacs$$H</linktopdf><linktohtml>$$Uhttps://pubs.acs.org/doi/10.1021/ie980294l$$EHTML$$P50$$Gacs$$H</linktohtml><link.rule.ids>314,780,784,2765,27076,27924,27925,56738,56788</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=1632208$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Huizenga, Piet</creatorcontrib><creatorcontrib>Kuipers, Johannes A. 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For this purpose the hydrogenation of α-methylstyrene on Pd/Al2O3 powdered catalyst has been performed in a small-scale reactor. Experimentally observed drops in conversion rate on an increase of permeate flux can mainly be attributed to reduced bulk reactivity caused by cake formation. Chemical reaction in the cake itself increased the conversion rate significantly in the case where a large fraction of the catalyst moved into the cake at high permeate fluxes. 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| ispartof | Industrial & engineering chemistry research, 1999-01, Vol.38 (1), p.98-107 |
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| language | eng |
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| source | American Chemical Society Journals |
| subjects | Applied sciences Chemical engineering Exact sciences and technology Reactors |
| title | Effect of Internal Filtration on Slurry Reactor Performance |
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