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Hydrocracking of vacuum residue using NiWS(x) dispersed catalysts

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dc.contributor.authorHur, Young Gul-
dc.contributor.authorLee, Dae-Won-
dc.contributor.authorLee, Kwan-Young-
dc.date.accessioned2021-09-03T16:00:26Z-
dc.date.available2021-09-03T16:00:26Z-
dc.date.created2021-06-16-
dc.date.issued2016-12-01-
dc.identifier.issn0016-2361-
dc.identifier.urihttps://scholar.korea.ac.kr/handle/2021.sw.korea/86580-
dc.description.abstractIn this study, unsupported nickel-tungsten sulfide (NiWS(x)) particles, where x is the actual molar ratio of Ni/W (x = 0, 0.005, 0.01, 0.02), were prepared, characterized with XRD, XPS, TEM, and EDX elemental mapping, and applied as a dispersed catalyst for upgrading of extra-heavy oil into good-quality liquid products. The hydrocracking reaction of vacuum residue (VR) was carried out at 400 degrees C with an initial H-2 pressure of 70 bar. It was found that an increase in the Ni content increases the degree of sulfidation of tungsten, promotes formation of Ni-W-S phases, and enhances the overall catalytic activity. Among the NiWS(x) dispersed catalysts, the NiWS(0.02) catalyst showed the highest performance in total liquid product yield (87.0 wt.%), commercial fuel fraction yield (51.9 wt.%), API gravity value of liquid product (14.3 degrees), and sulfur removal conversion (86.5%). In addition, coke formation (4.0 wt.%) was efficiently suppressed, and the C-5-asphaltene conversion (81.8%) was significantly raised. (C) 2016 Elsevier Ltd. All rights reserved.-
dc.languageEnglish-
dc.language.isoen-
dc.publisherELSEVIER SCI LTD-
dc.subjectHYDROTREATING CATALYSTS-
dc.subjectHYDRODESULFURIZATION CATALYSTS-
dc.subjectSUPPORT-INTERACTION-
dc.subjectPROMOTED TUNGSTEN-
dc.subjectWS2 NANOCLUSTERS-
dc.subjectHEAVY PETROLEUM-
dc.subjectMODEL CATALYSTS-
dc.subjectACTIVE PHASE-
dc.subjectPART 1-
dc.subjectNICKEL-
dc.titleHydrocracking of vacuum residue using NiWS(x) dispersed catalysts-
dc.typeArticle-
dc.contributor.affiliatedAuthorLee, Kwan-Young-
dc.identifier.doi10.1016/j.fuel.2016.08.027-
dc.identifier.scopusid2-s2.0-84982150745-
dc.identifier.wosid000382248700079-
dc.identifier.bibliographicCitationFUEL, v.185, pp.794 - 803-
dc.relation.isPartOfFUEL-
dc.citation.titleFUEL-
dc.citation.volume185-
dc.citation.startPage794-
dc.citation.endPage803-
dc.type.rimsART-
dc.type.docTypeArticle-
dc.description.journalClass1-
dc.description.journalRegisteredClassscie-
dc.description.journalRegisteredClassscopus-
dc.relation.journalResearchAreaEnergy & Fuels-
dc.relation.journalResearchAreaEngineering-
dc.relation.journalWebOfScienceCategoryEnergy & Fuels-
dc.relation.journalWebOfScienceCategoryEngineering, Chemical-
dc.subject.keywordPlusHYDROTREATING CATALYSTS-
dc.subject.keywordPlusHYDRODESULFURIZATION CATALYSTS-
dc.subject.keywordPlusSUPPORT-INTERACTION-
dc.subject.keywordPlusPROMOTED TUNGSTEN-
dc.subject.keywordPlusWS2 NANOCLUSTERS-
dc.subject.keywordPlusHEAVY PETROLEUM-
dc.subject.keywordPlusMODEL CATALYSTS-
dc.subject.keywordPlusACTIVE PHASE-
dc.subject.keywordPlusPART 1-
dc.subject.keywordPlusNICKEL-
dc.subject.keywordAuthorVacuum residue-
dc.subject.keywordAuthorHydrotreating-
dc.subject.keywordAuthorHydrocracking-
dc.subject.keywordAuthorDispersed catalyst-
dc.subject.keywordAuthorNi-W-S catalyst-
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