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dc.contributor.authorZeng, Wenhao-
dc.contributor.authorShim, Jaehee-
dc.contributor.authorLi, Jiajia-
dc.contributor.authorKim, Jinseong-
dc.contributor.authorBaik, Hionsuck-
dc.contributor.authorLi, Liangqing-
dc.contributor.authorLee, Kwan-Young-
dc.contributor.authorChoi, Jungkyu-
dc.date.accessioned2025-09-30T07:01:56Z-
dc.date.available2025-09-30T07:01:56Z-
dc.date.created2025-09-30-
dc.date.issued2025-12-
dc.identifier.issn1383-5866-
dc.identifier.urihttps://pubs.kist.re.kr/handle/201004/153282-
dc.description.abstractThe development of robust, high-performance hydrocarbon (HC) trapping materials that can withstand harsh hydrothermal treatment (HT) at temperatures >= 800 degrees C remains a great challenge. In this study, to the best of our knowledge, we, for the first time, delicately removed framework Al from the BEA zeolite support (Si/Al ratio of ca. 18.1) using acids of varying strength and concentration prior to Cu impregnation. Use of moderately dealuminated BEA zeolites (Si/Al ratio: ca. 25-35) for Cu impregnation allowed for forming a sufficient amount of the active Cu species (both Cu+ ions inside for preferred HC adsorption and tiny CuO particles outside for effective HC oxidation). More importantly, the Cu-impregnated ones preserved these active Cu species as well as the original zeolite structure after HT. These features led to both excellent cold-start test (a simplified trap test for simulated HC emissions) activity and hydrothermal stability as desired for HC traps. In particular, the Cuimpregnated BEA zeolite with optimal pre-dealumination (treated with a 0.1 M oxalic acid solution) showed unprecedentedly marked HC removal ability (11.3 % of total HC removal efficiency vs. 0 % for the parent BEA zeolite-based counterpart) even after very harsh HT at 850 degrees C, bringing the HC traps closer to real-world applications.-
dc.languageEnglish-
dc.publisherPergamon Press Ltd.-
dc.titleA durable Cu-beta zeolite via simple yet controlled pre-removal of framework Al for hydrocarbon trapping-
dc.typeArticle-
dc.identifier.doi10.1016/j.seppur.2025.134802-
dc.description.journalClass1-
dc.identifier.bibliographicCitationSeparation and Purification Technology, v.378, no.Part 3-
dc.citation.titleSeparation and Purification Technology-
dc.citation.volume378-
dc.citation.numberPart 3-
dc.description.isOpenAccessN-
dc.description.journalRegisteredClassscie-
dc.description.journalRegisteredClassscopus-
dc.identifier.wosid001567738400004-
dc.identifier.scopusid2-s2.0-105013739924-
dc.relation.journalWebOfScienceCategoryEngineering, Chemical-
dc.relation.journalResearchAreaEngineering-
dc.type.docTypeArticle-
dc.subject.keywordPlusSELECTIVE CATALYTIC-REDUCTION-
dc.subject.keywordPlusPHYSICOCHEMICAL PROPERTIES-
dc.subject.keywordPlusHYDROTHERMAL STABILITY-
dc.subject.keywordPlusAUTOMOTIVE CATALYSIS-
dc.subject.keywordPlusCU-SSZ-13 CATALYST-
dc.subject.keywordPlusTHERMAL-STABILITY-
dc.subject.keywordPlusNH3-SCR REACTION-
dc.subject.keywordPlusDEALUMINATION-
dc.subject.keywordPlusNOX-
dc.subject.keywordPlusACID-
dc.subject.keywordAuthorAcid-assisted dealumination-
dc.subject.keywordAuthorCu-impregnated BEA zeolites-
dc.subject.keywordAuthorHydrothermal stability-
dc.subject.keywordAuthorHydrocarbon trap-
dc.subject.keywordAuthorCold-start test-
dc.subject.keywordAuthorAcid-assisted dealumination-
dc.subject.keywordAuthorCu-impregnated BEA zeolites-
dc.subject.keywordAuthorHydrothermal stability-
dc.subject.keywordAuthorHydrocarbon trap-
dc.subject.keywordAuthorCold-start test-
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