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dc.contributor.authorKim, Yun Tae-
dc.contributor.authorUm, Ji Hyun-
dc.contributor.authorKim, Sung Ho-
dc.contributor.authorLim, Tae-Hoon-
dc.contributor.authorLee, Ho-In-
dc.date.accessioned2024-01-20T18:34:40Z-
dc.date.available2024-01-20T18:34:40Z-
dc.date.created2021-09-05-
dc.date.issued2010-08-20-
dc.identifier.issn0926-860X-
dc.identifier.urihttps://pubs.kist.re.kr/handle/201004/131167-
dc.description.abstractAutothermal reforming, which is a combined process of steam reforming and partial oxidation reforming, has excellent coke resistance and high efficiency in reforming reactions. Octane autothermal reforming was carried out over Ni-supported catalysts. The catalysts were prepared by normal precipitation and promoters were added by impregnation. The formation of NiO-MgO solid solution was accomplished during calcination of the Ni/MgO catalyst at 900 degrees C, resulting in loss of the active Ni metal and very low catalytic activity. Therefore, all catalysts were treated by a reduction process without calcination in order to prevent the formation of NiO-MgO solid solution. Among Ni/MgO catalysts combined with various promoters such as Ag, Cr, and Cu, Ni-Cr/MgO catalyst showed the most desirable characteristics in the aspects of its activity, stability, and resistance to carbon deposition. We found an optimal condition for octane autothermal reforming when steam-to-carbon ratio and oxygen-to-carbon ratio were 1.5 and 0.5, respectively. (C) 2010 Elsevier B.V. All rights reserved.-
dc.languageEnglish-
dc.publisherELSEVIER SCIENCE BV-
dc.subjectHYDROGEN-PRODUCTION-
dc.subjectCOKE FORMATION-
dc.subjectPREFERENTIAL OXIDATION-
dc.subjectNICKEL-CATALYSTS-
dc.subjectMETHANE-
dc.subjectMGO-
dc.subjectCO2-
dc.subjectNIO-
dc.subjectCARBONATE-
dc.subjectMECHANISM-
dc.titleEffect of promoter on Ni/MgO catalyst in C8H18 autothermal reforming in solid oxide fuel cell system-
dc.typeArticle-
dc.identifier.doi10.1016/j.apcata.2010.05.054-
dc.description.journalClass1-
dc.identifier.bibliographicCitationAPPLIED CATALYSIS A-GENERAL, v.384, no.1-2, pp.10 - 17-
dc.citation.titleAPPLIED CATALYSIS A-GENERAL-
dc.citation.volume384-
dc.citation.number1-2-
dc.citation.startPage10-
dc.citation.endPage17-
dc.description.journalRegisteredClassscie-
dc.description.journalRegisteredClassscopus-
dc.identifier.wosid000281179700002-
dc.identifier.scopusid2-s2.0-77955579531-
dc.relation.journalWebOfScienceCategoryChemistry, Physical-
dc.relation.journalWebOfScienceCategoryEnvironmental Sciences-
dc.relation.journalResearchAreaChemistry-
dc.relation.journalResearchAreaEnvironmental Sciences & Ecology-
dc.type.docTypeArticle-
dc.subject.keywordPlusHYDROGEN-PRODUCTION-
dc.subject.keywordPlusCOKE FORMATION-
dc.subject.keywordPlusPREFERENTIAL OXIDATION-
dc.subject.keywordPlusNICKEL-CATALYSTS-
dc.subject.keywordPlusMETHANE-
dc.subject.keywordPlusMGO-
dc.subject.keywordPlusCO2-
dc.subject.keywordPlusNIO-
dc.subject.keywordPlusCARBONATE-
dc.subject.keywordPlusMECHANISM-
dc.subject.keywordAuthorOctane autothermal reforming-
dc.subject.keywordAuthorCarbon deposition-
dc.subject.keywordAuthorNi/MgO-
dc.subject.keywordAuthorCr promoter-
dc.subject.keywordAuthorNiO-MgO solid solution-
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