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Studies on the steam CO2 reforming of methane over ordered mesoporous nickel-magnesium-alumina catalysts

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dc.contributor.authorKim, Hyun-Jin-
dc.contributor.authorYang, Eun-Hyeok-
dc.contributor.authorNoh, Young Su-
dc.contributor.authorHong, Gi Hoon-
dc.contributor.authorPark, Ji In-
dc.contributor.authorShin, Seol A.-
dc.contributor.authorLee, Kwan-Young-
dc.contributor.authorMoon, Dong Ju-
dc.date.accessioned2021-09-02T15:08:24Z-
dc.date.available2021-09-02T15:08:24Z-
dc.date.created2021-06-16-
dc.date.issued2018-02-
dc.identifier.issn0922-6168-
dc.identifier.urihttps://scholar.korea.ac.kr/handle/2021.sw.korea/77424-
dc.description.abstractOrdered mesoporous materials have received much attention because of their high surface area and ordered pore structure. The Mg-promoted ordered mesoporous nickel-alumina catalysts (M-Mg (x) NA), which were prepared using the evaporation induced self-assembly method, were investigated in the Steam CO2 Reforming (SCR) of methane. The fresh and spent catalysts were characterized by various analytical techniques such as N-2 physisorption, small-angle X-ray scattering, X-ray diffraction, temperature-programmed reduction, thermogravimetric analysis, transmission electron microscopy and CO2-temperature programmed desorption analysis. We have found that the M-Mg (x) NA catalyst has a larger surface area and a narrower pore size distribution than the Ni/Al2O3 catalyst (NA); furthermore, the M-Mg (x) NA catalyst exhibits high catalytic stability under the tested conditions of 600 A degrees C, 1 bar and feed molar ratio of CH4:CO2:H2O = 1:1:1. We consider that the ordered mesoporosity prevents the nickel particles from sintering because of the confinement effect and decreases the particle size in the SCR reaction. Thus, the Mg-promoted ordered mesoporous nickel-alumina catalyst shows enhanced resistance to carbon formation during the steam CO2 reforming of methane.-
dc.languageEnglish-
dc.language.isoen-
dc.publisherSPRINGER-
dc.subjectCARBON-DIOXIDE-
dc.subjectSYNTHESIS GAS-
dc.subjectPARTIAL OXIDATION-
dc.subjectHYDROGEN-PRODUCTION-
dc.subjectCH4-
dc.subjectSYNGAS-
dc.subjectSILICA-
dc.subjectSBA-15-
dc.subjectLA-
dc.subjectPERFORMANCE-
dc.titleStudies on the steam CO2 reforming of methane over ordered mesoporous nickel-magnesium-alumina catalysts-
dc.typeArticle-
dc.contributor.affiliatedAuthorLee, Kwan-Young-
dc.identifier.doi10.1007/s11164-017-3156-4-
dc.identifier.scopusid2-s2.0-85030679378-
dc.identifier.wosid000422905700024-
dc.identifier.bibliographicCitationRESEARCH ON CHEMICAL INTERMEDIATES, v.44, no.2, pp.1131 - 1148-
dc.relation.isPartOfRESEARCH ON CHEMICAL INTERMEDIATES-
dc.citation.titleRESEARCH ON CHEMICAL INTERMEDIATES-
dc.citation.volume44-
dc.citation.number2-
dc.citation.startPage1131-
dc.citation.endPage1148-
dc.type.rimsART-
dc.type.docTypeArticle-
dc.description.journalClass1-
dc.description.journalRegisteredClassscie-
dc.description.journalRegisteredClassscopus-
dc.relation.journalResearchAreaChemistry-
dc.relation.journalWebOfScienceCategoryChemistry, Multidisciplinary-
dc.subject.keywordPlusCARBON-DIOXIDE-
dc.subject.keywordPlusSYNTHESIS GAS-
dc.subject.keywordPlusPARTIAL OXIDATION-
dc.subject.keywordPlusHYDROGEN-PRODUCTION-
dc.subject.keywordPlusCH4-
dc.subject.keywordPlusSYNGAS-
dc.subject.keywordPlusSILICA-
dc.subject.keywordPlusSBA-15-
dc.subject.keywordPlusLA-
dc.subject.keywordPlusPERFORMANCE-
dc.subject.keywordAuthorHydrogen-
dc.subject.keywordAuthorSteam CO2 reforming of methane-
dc.subject.keywordAuthorSynthesis gas-
dc.subject.keywordAuthorNi support catalysts-
dc.subject.keywordAuthorMesoporous material-
dc.subject.keywordAuthorGas to liquid-
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