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dc.contributor.authorRaj, K Joseph Antony-
dc.contributor.authorDayalan, A-
dc.contributor.authorVijayaraghavan, V R-
dc.date.accessioned2010-01-04T11:15:33Z-
dc.date.available2010-01-04T11:15:33Z-
dc.date.issued2006-07-
dc.identifier.issn0975-0991 (Online); 0971-457X (Print)-
dc.identifier.urihttp://hdl.handle.net/123456789/7049-
dc.description329-333en_US
dc.description.abstractMethylation of toluene with methanol in the vapour phase has been studied over MnAPO-11 and ZAPO-11. The reactions were carried out in a fixed bed reactor in the temperature range of 250-400ºC. p-Xylene is produced in greater concentrations than the other products. The selectivity for p-xylene is a function of acidity, specific surface area of the catalyst, reaction temperature and toluene to methanol ratio. ZAPO-11 was found to be more active than MnAPO-11. Maximum conversion (25.8%) was observed at 400ºC over ZAPO-11. The selectivity to p-xylene was found to increase with time on stream possibly due to partial reduction in the pore size of the catalyst by coke depositionen_US
dc.language.isoen_USen_US
dc.publisherCSIRen_US
dc.relation.ispartofseriesC12P5/00, C02F11/04en_US
dc.sourceIJCT Vol.13(4) [July 2006]en_US
dc.subjectMethylationen_US
dc.subjectAlPO-11en_US
dc.subjectXyleneen_US
dc.subjectTolueneen_US
dc.subjectMolecular sievesen_US
dc.titleMethylation of toluene over MnAPO-11 and ZAPO-11en_US
dc.typeArticleen_US
Appears in Collections:IJCT Vol.13(4) [July 2006]

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