Please use this identifier to cite or link to this item: http://nopr.niscpr.res.in/handle/123456789/2873
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dc.contributor.authorJoshi, Chintan K-
dc.contributor.authorParikh, Parimal A-
dc.date.accessioned2009-01-28T09:13:18Z-
dc.date.available2009-01-28T09:13:18Z-
dc.date.issued2008-11-
dc.identifier.issn0971–457X-
dc.identifier.urihttp://hdl.handle.net/123456789/2873-
dc.description572-575en_US
dc.description.abstractHydrogenation of 1-octene was carried out in a monolithic stirred reactor. A cordierite monolith with HZSM-5 washcoat, impregnated with Pd was used as catalyst. The reactions were conducted between 50-65ºC and 250-400 psi hydrogen pressure. The effects of temperature and pressure on conversion and selectivity were measured. Major part of 1-octene was converted to n-octane and some isomers of octene were formed. However, at higher operating condition they were converted to n-octane. The experiments proved that the monolithic reactor is an attractive alternative reactor.en_US
dc.language.isoen_USen_US
dc.publisherCSIRen_US
dc.sourceIJCT Vol.15(6) [November 2008]en_US
dc.subjectMultiphase reactoren_US
dc.subjectPd/HZSM-5 monolith catalysten_US
dc.subjectHydrogenationen_US
dc.titleApplication of monolithic stirred reactor in hydrogenation reactionen_US
dc.typeArticleen_US
Appears in Collections:IJCT Vol.15(6) [November 2008]

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