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Cited 28 time in webofscience Cited 31 time in scopus
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dc.contributor.authorHAM, SW-
dc.contributor.authorCHOI, H-
dc.contributor.authorNAM, IS-
dc.contributor.authorKIM, YG-
dc.date.accessioned2016-03-31T14:30:10Z-
dc.date.available2016-03-31T14:30:10Z-
dc.date.created2009-03-20-
dc.date.issued1995-05-
dc.identifier.issn0888-5885-
dc.identifier.other1995-OAK-0000009131-
dc.identifier.urihttps://oasis.postech.ac.kr/handle/2014.oak/21794-
dc.description.abstractDeactivation of copper ion-exchanged mordenite (CuHM) catalysts with different copper contents by SO2 for NO reduction with NH3 was examined in a fixed bed flow reactor. A larger amount of deactivating agent deposits on the catalyst surface with the increase of copper contents under the same operating conditions. The deactivating agents deposited on the copper-exchanged mordenite catalysts were mainly (NH4)(2)SO4 and/or NH4HSO4 from the results of thermal analyses such as thermogravimetric analysis (TGA), differential thermal analysis (DTA), and temperature-programmed desorption (TPD). The formation of the ammonium salts largely depends on the reaction temperature and SO3 concentration generated from SO2 oxidation which is a reaction catalyzed primarily by copper ions on the catalyst surface. The catalytic activity and surface area of the deactivated catalysts are well-correlated with the sulfur content deposited on the catalyst surface, depending upon the reaction temperatures and its catalyst copper contents.-
dc.description.statementofresponsibilityX-
dc.languageEnglish-
dc.publisherAMER CHEMICAL SOC-
dc.relation.isPartOfINDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH-
dc.subjectSELECTIVE CATALYTIC REDUCTION-
dc.subjectVANADIA ALUMINA CATALYST-
dc.subjectNITRIC-OXIDE-
dc.subjectAMMONIA-
dc.subjectZEOLITE-
dc.subjectDEACTIVATION-
dc.subjectGASES-
dc.subjectCOKE-
dc.subjectSO2-
dc.titleEFFECT OF COPPER CONTENTS OIL SULFUR POISONING OF COPPER ION-EXCHANGED MORDENITE FOR NO REDUCTION BY NH3-
dc.typeArticle-
dc.contributor.college환경공학부-
dc.identifier.doi10.1021/ie00044a014-
dc.author.googleHAM, SW-
dc.author.googleCHOI, H-
dc.author.googleNAM, IS-
dc.author.googleKIM, YG-
dc.relation.volume34-
dc.relation.issue5-
dc.relation.startpage1616-
dc.relation.lastpage1623-
dc.contributor.id10069683-
dc.relation.journalINDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH-
dc.relation.indexSCI급, SCOPUS 등재논문-
dc.relation.sciSCI-
dc.collections.nameJournal Papers-
dc.type.rimsART-
dc.identifier.bibliographicCitationINDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, v.34, no.5, pp.1616 - 1623-
dc.identifier.wosidA1995QX50500014-
dc.date.tcdate2019-01-01-
dc.citation.endPage1623-
dc.citation.number5-
dc.citation.startPage1616-
dc.citation.titleINDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH-
dc.citation.volume34-
dc.contributor.affiliatedAuthorNAM, IS-
dc.identifier.scopusid2-s2.0-0000692933-
dc.description.journalClass1-
dc.description.journalClass1-
dc.description.wostc27-
dc.type.docTypeArticle-
dc.subject.keywordPlusSELECTIVE CATALYTIC REDUCTION-
dc.subject.keywordPlusVANADIA ALUMINA CATALYST-
dc.subject.keywordPlusNITRIC-OXIDE-
dc.subject.keywordPlusAMMONIA-
dc.subject.keywordPlusZEOLITE-
dc.subject.keywordPlusDEACTIVATION-
dc.subject.keywordPlusGASES-
dc.subject.keywordPlusCOKE-
dc.subject.keywordPlusSO2-
dc.relation.journalWebOfScienceCategoryEngineering, Chemical-
dc.description.journalRegisteredClassscie-
dc.description.journalRegisteredClassscopus-
dc.relation.journalResearchAreaEngineering-

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