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Performance of CoMoS catalysts supported on nanoporous carbon in the hydrodesulfurization of dibenzothiophene and 4,6-dimethyldibenzothiophene

DC Field Value Language
dc.contributor.authorLee, Jung Joon-
dc.contributor.authorHan, Sang Jin-
dc.contributor.authorKim, Heeyeon-
dc.contributor.authorKoh, Jae Hyun-
dc.contributor.authorHyeon, Taeghwan-
dc.contributor.authorMoon, Sang Heup-
dc.date.accessioned2020-04-27T13:42:26Z-
dc.date.available2020-04-27T13:42:26Z-
dc.date.created2020-03-20-
dc.date.created2020-03-20-
dc.date.issued2003-11-
dc.identifier.citationCatalysis Today, Vol.86 No.1-4, pp.141-149-
dc.identifier.issn0920-5861-
dc.identifier.other92954-
dc.identifier.urihttps://hdl.handle.net/10371/166072-
dc.description.abstractA new type of nanoporous carbon with a large surface area and mesoporosity was prepared and used as a support for a hydrodesulfurization (HDS) catalyst. The overall activity of CoMoS catalysts for the HDS of dibenzothiophene (DBT) and 4,6-dimethyldibenzothiophene (4,6-DMDBT) is affected by the type of support used for preparing the catalyst and decreases in the order of CoMo/(nanoporous carbon) > CoMo/(activated carbon) > CoMo/Al2O3. The surface area of activated carbon is the largest among these three types of supports but is significantly lowered after metal loading during the preparation of the catalyst. On the other hand, the surface areas of the other two supports are largely preserved after metal loading. The intrinsic activity of the catalysts, estimated by dividing the overall HDS rate by the amount of NO adsorbed on the catalyst, shows a trend that is different from that for the overall activity, and follows the order of CoMo/(nanoporous carbon) approximate to CoMo/Al2O3 > CoMo/(activated carbon). The low intrinsic activity of CoMo/(activated carbon) compared to that of the other two catalysts, particularly in the case of 4,6-DMDBT HDS, is obtained because the diffusion of reactants into the catalyst pores is significantly limited. This is not observed with other catalysts supported on nanoporous carbon and alumina. From the results of this study, we conclude that nanoporous carbon is a promising support for HDS catalysts, compared to conventional supports such as alumina and activated carbon, because it has a large surface area and a high mesoporosity, both of which are beneficial to the preparation of highly dispersed metal catalysts without significant pore blocking due to the dispersed metal particles. (C) 2003 Elsevier B.V. All rights reserved.-
dc.language영어-
dc.publisherElsevier BV-
dc.titlePerformance of CoMoS catalysts supported on nanoporous carbon in the hydrodesulfurization of dibenzothiophene and 4,6-dimethyldibenzothiophene-
dc.typeArticle-
dc.contributor.AlternativeAuthor문상흡-
dc.contributor.AlternativeAuthor현택환-
dc.identifier.doi10.1016/S0920-5861(03)00408-5-
dc.citation.journaltitleCatalysis Today-
dc.identifier.wosid000186414400011-
dc.identifier.scopusid2-s2.0-0141929347-
dc.citation.endpage149-
dc.citation.number1-4-
dc.citation.startpage141-
dc.citation.volume86-
dc.identifier.sci000186414400011-
dc.description.isOpenAccessN-
dc.contributor.affiliatedAuthorHyeon, Taeghwan-
dc.contributor.affiliatedAuthorMoon, Sang Heup-
dc.type.docTypeArticle-
dc.description.journalClass1-
dc.subject.keywordPlusFLUORINATED HYDROTREATMENT CATALYSTS-
dc.subject.keywordPlusMETHYL-SUBSTITUTED DIBENZOTHIOPHENES-
dc.subject.keywordPlusMOLYBDENUM SULFIDE CATALYSTS-
dc.subject.keywordPlusGAMMA-ALUMINA CATALYSTS-
dc.subject.keywordPlusCO-MO CATALYSTS-
dc.subject.keywordPlusACTIVATED CARBON-
dc.subject.keywordPlusREACTIVITY-
dc.subject.keywordPlusMECHANISM-
dc.subject.keywordPlusSURFACE-
dc.subject.keywordPlusSILICA-
dc.subject.keywordAuthorhydrodesulfurization-
dc.subject.keywordAuthor4,6-dimethyldibenzothiophene-
dc.subject.keywordAuthordibenzothiophene-
dc.subject.keywordAuthornanoporous carbon-
dc.subject.keywordAuthordiffusion limitation-
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  • School of Chemical and Biological Engineering
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