Intrinsic kinetics of hydrogenation of benzene on nickel catalysts supported on kieselguhr

Marangozis, JK; Mantzouranis, BG; Sophos, AN

dc.contributor.author	Marangozis, JK	en
dc.contributor.author	Mantzouranis, BG	en
dc.contributor.author	Sophos, AN	en
dc.date.accessioned	2014-03-01T01:05:46Z
dc.date.available	2014-03-01T01:05:46Z
dc.date.issued	1979	en
dc.identifier.issn	0196-4321	en
dc.identifier.uri	https://dspace.lib.ntua.gr/xmlui/handle/123456789/8975
dc.relation.uri	http://www.scopus.com/inward/record.url?eid=2-s2.0-33646310103&partnerID=40&md5=8a7dbe88c55a3faf668c81639fb51b89	en
dc.subject.classification	Engineering, Chemical	en
dc.subject.classification	Engineering, Industrial	en
dc.title	Intrinsic kinetics of hydrogenation of benzene on nickel catalysts supported on kieselguhr	en
heal.type	journalArticle	en
heal.language	English	en
heal.publicationDate	1979	en
heal.abstract	Intrinsic rates of benzene hydrogenation have been measured on a commercial Ni/kieselguhr catalyst. The rates have been correlated according to the power law, rB = k·pH20.32·pB0.21, and also according to the model rB = [kKB·pB/(1+ KB·pB)][pH2/(pH2 + pB)], which postulates reaction between hydrogen gas and adsorbed benzene molecules. The apparatus was an isothermal, tubular, differential reactor. Temperature was varied from 67 to 90°C, hydrogen partial pressure between 1000 and 3000 torr, and benzene partial pressure from 70 to 286 torr. Specific reaction rates k and adsorption parameters KB have been correlated by the Arrhenius law. © 1979 American Chemical Society.	en
heal.publisher	AMER CHEMICAL SOC	en
heal.journalName	Industrial and Engineering Chemistry Product Research and Development	en
dc.identifier.isi	ISI:A1979GJ78800012	en
dc.identifier.volume	18	en
dc.identifier.issue	1	en
dc.identifier.spage	61	en
dc.identifier.epage	63	en