Please use this identifier to cite or link to this item: http://nopr.niscpr.res.in/handle/123456789/26387
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dc.contributor.authorChaudhari, Parmesh K-
dc.contributor.authorSaini, Pradeep K-
dc.contributor.authorChand, Shri-
dc.date.accessioned2014-02-04T10:52:13Z-
dc.date.available2014-02-04T10:52:13Z-
dc.date.issued2002-10-
dc.identifier.issn0975-1084 (Online); 0022-4456 (Print)-
dc.identifier.urihttp://hdl.handle.net/123456789/26387-
dc.description810-816en_US
dc.description.abstractThe toluene disproportionation reaction was carried out using ZSM-5 as well as Y- zeolite catalysts after ion exchange with active metals Ni, Pb,and Cr. The reaction was carried out under atmospheric pressure. The effect of type of cation used for ion exchange, silica- alumina ratio, type of zeolite, and particle size were also studied. The percent p-xylene yield (which is the most desirable product), was found to increase after ion-exchange with active cations. A maximum p -xylene yield of 2.3 percent was obtained with Cr HZSM-5 (SAR-19) at 600C and 1 atmos pressure.en_US
dc.language.isoen_USen_US
dc.publisherNISCAIR-CSIR, Indiaen_US
dc.rights CC Attribution-Noncommercial-No Derivative Works 2.5 Indiaen_US
dc.sourceJSIR Vol.61(10) [October 2002]en_US
dc.titleComparative Performance of Ion-exchanged ZSM-5 and Y -Zeolite Catalysts for Toluene Disproportionation Reactionen_US
dc.typeArticleen_US
Appears in Collections:JSIR Vol.61(10) [October 2002]

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