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Hydrogenation of levulinic acid with and without external hydrogen over Ni/SBA-15 catalyst

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dc.contributor.authorVarkolu, Mohan-
dc.contributor.authorBathula, Hari Babu-
dc.contributor.authorSuh, Young-Woong-
dc.contributor.authorBurri, David Raju-
dc.contributor.authorKamaraju, Seetha Rama Rao-
dc.date.accessioned2022-07-11T13:15:50Z-
dc.date.available2022-07-11T13:15:50Z-
dc.date.created2021-05-11-
dc.date.issued2018-09-
dc.identifier.issn2190-5525-
dc.identifier.urihttps://scholarworks.bwise.kr/hanyang/handle/2021.sw.hanyang/149473-
dc.description.abstractA series of Ni/SBA-15 catalysts were prepared by impregnation method for the hydrogenation of levulinic acid (LA) to -valerolactone in a fixed bed reactor at atmospheric pressure. The catalysts were characterized by XRD, TPR, AAS, Pulse chemisorption, SEM-EDAX, TEM, BET Surface area and XPS. The catalyst 30wt% Ni/SBA-15 exhibited excellent catalytic performance (97% yield) at 250 degrees C due to the presence of superior number of active surface Ni species. While 30wt% Ni/SiO2 catalyst showed lower catalytic activity (87% yield) at about similar conversion. The co-feeding of formic acid (FA) and water (impurities) with levulinic acid was also evaluated over 30wt% Ni/SBA-15 which yielded excellent levulinic acid conversion. The noteworthy results were obtained at a molar ratio of FA/LA=5. The constant catalytic activity during 10h experiment with an external H-2 flow has showed the sturdiness of the Ni/SBA-15 catalyst.On the other hand, a slight decrease in conversion as well as yield during the time-on-stream in the absence of external H-2 flow was attributed to the accumulation of carbon species on the catalyst surface.-
dc.language영어-
dc.language.isoen-
dc.publisherSPRINGER HEIDELBERG-
dc.titleHydrogenation of levulinic acid with and without external hydrogen over Ni/SBA-15 catalyst-
dc.typeArticle-
dc.contributor.affiliatedAuthorSuh, Young-Woong-
dc.identifier.doi10.1007/s13203-018-0203-z-
dc.identifier.wosid000443264000003-
dc.identifier.bibliographicCitationAPPLIED PETROCHEMICAL RESEARCH, v.8, no.3, pp.153 - 162-
dc.relation.isPartOfAPPLIED PETROCHEMICAL RESEARCH-
dc.citation.titleAPPLIED PETROCHEMICAL RESEARCH-
dc.citation.volume8-
dc.citation.number3-
dc.citation.startPage153-
dc.citation.endPage162-
dc.type.rimsART-
dc.type.docTypeArticle-
dc.description.journalClass1-
dc.description.isOpenAccessY-
dc.relation.journalResearchAreaEngineering-
dc.relation.journalWebOfScienceCategoryEngineering, Chemical-
dc.subject.keywordPlusSUPPORTED NICKEL-CATALYSTS-
dc.subject.keywordPlusGAMMA-VALEROLACTONE-
dc.subject.keywordPlusMESOPOROUS SILICA-
dc.subject.keywordPlusFORMIC-ACID-
dc.subject.keywordPlusTRANSPORTATION FUELS-
dc.subject.keywordPlusPHASE HYDROGENATION-
dc.subject.keywordPlusSURFACE-AREA-
dc.subject.keywordPlusNI CATALYSTS-
dc.subject.keywordPlusBIOMASS-
dc.subject.keywordPlusCONVERSION-
dc.subject.keywordAuthorHydrogenation-
dc.subject.keywordAuthorLevulinic acid-
dc.subject.keywordAuthorgamma-Valerolactone-
dc.subject.keywordAuthorWith external H-2-
dc.subject.keywordAuthorWithout external H-2-
dc.subject.keywordAuthor30wt% Ni-
dc.subject.keywordAuthorSBA-15-
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