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dc.contributor.authorKim, YL-
dc.contributor.authorChung, SJ-
dc.contributor.authorKim, JD-
dc.contributor.authorLim, JS-
dc.contributor.authorLee, YW-
dc.contributor.authorYi, SC-
dc.date.accessioned2024-01-21T10:08:20Z-
dc.date.available2024-01-21T10:08:20Z-
dc.date.created2021-09-05-
dc.date.issued2002-09-
dc.identifier.issn0133-1736-
dc.identifier.urihttps://pubs.kist.re.kr/handle/201004/139259-
dc.description.abstractIn sub- and supercritical water, partial oxidation of p-xylene was performed in a batch reactor without a catalyst at 240-500degreesC, 220-300 bar. The loaded amount of hydrogen peroxide was set to 0-100% of the theoretically required oxygen amount. Conversion of p-xylene was reached over 99% within 15-20 min. In sub- and supercritical water, we propose two parallel pathways and major products that consist of p-tolualdehyde, p-toluic acid, terephthalic acid, toluene and benzaldehyde. Yields of major products in subcritical conditions were higher than in a supercritical conditions.-
dc.languageEnglish-
dc.publisherAKADEMIAI KIADO-
dc.titleUncatalyzed partial oxidation of p-xylene in sub- and supercritical water-
dc.typeArticle-
dc.identifier.doi10.1023/A:1020331517408-
dc.description.journalClass1-
dc.identifier.bibliographicCitationREACTION KINETICS AND CATALYSIS LETTERS, v.77, no.1, pp.35 - 42-
dc.citation.titleREACTION KINETICS AND CATALYSIS LETTERS-
dc.citation.volume77-
dc.citation.number1-
dc.citation.startPage35-
dc.citation.endPage42-
dc.description.journalRegisteredClassscie-
dc.description.journalRegisteredClassscopus-
dc.identifier.wosid000178165000005-
dc.identifier.scopusid2-s2.0-0036025808-
dc.relation.journalWebOfScienceCategoryChemistry, Physical-
dc.relation.journalResearchAreaChemistry-
dc.type.docTypeArticle-
dc.subject.keywordAuthorp-xylene-
dc.subject.keywordAuthorpartial oxidation-
dc.subject.keywordAuthorsub- and supercritical water-
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