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Experimental and simulation studies for reaction enhancement of catalytic CF4 hydrolysis by consecutive HF removal using a multi-stage catalyst-adsorbent reactor

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dc.contributor.authorHan, Jae-Yun-
dc.contributor.authorKim, Chang-Hyun-
dc.contributor.authorLee, Boreum-
dc.contributor.authorJeong, Seonju-
dc.contributor.authorLim, Hankwon-
dc.contributor.authorLee, Kwan-Young-
dc.contributor.authorRyi, Shin-Kun-
dc.date.accessioned2021-09-02T22:21:58Z-
dc.date.available2021-09-02T22:21:58Z-
dc.date.created2021-06-16-
dc.date.issued2017-12-
dc.identifier.issn2152-3878-
dc.identifier.urihttps://scholar.korea.ac.kr/handle/2021.sw.korea/81346-
dc.description.abstractIn this paper, a multi-stage catalyst-adsorbent reactor consisting of a series of catalyst and adsorbent beds is proposed for an effective tetrafluoromethane (CF4) abatement and conversion of corrosive hydrogen fluoride (HF) to CaF2, a useful chemical. Experimentally, enhanced CF4 conversions were observed in multi-stage catalyst-adsorbent reactors compared to a zero-stage reactor (catalyst bed only) confirming sorption-enhanced CF4 hydrolysis due to selective removal of HF during reaction. In addition, some useful design guidelines to select the number of stages and a proper time to replace adsorbents are presented. To develop a process simulation model to represent experimental data, Aspen HYSYS (R), a commercial process simulator, was used providing a proper model to match experimental data quite reasonably. Based on experimental and simulative studies, a three- or four-stage catalyst-adsorbent reactor is recommended for CF4 abatement considering both reactor performance and capital/operating expenditures. (c) 2017 Society of Chemical Industry and John Wiley & Sons, Ltd.-
dc.languageEnglish-
dc.language.isoen-
dc.publisherWILEY PERIODICALS, INC-
dc.subjectDECOMPOSITION-
dc.subjectCOMBUSTION-
dc.subjectABATEMENT-
dc.titleExperimental and simulation studies for reaction enhancement of catalytic CF4 hydrolysis by consecutive HF removal using a multi-stage catalyst-adsorbent reactor-
dc.typeArticle-
dc.contributor.affiliatedAuthorLee, Kwan-Young-
dc.identifier.doi10.1002/ghg.1742-
dc.identifier.scopusid2-s2.0-85037660521-
dc.identifier.wosid000417761600014-
dc.identifier.bibliographicCitationGREENHOUSE GASES-SCIENCE AND TECHNOLOGY, v.7, no.6, pp.1141 - 1149-
dc.relation.isPartOfGREENHOUSE GASES-SCIENCE AND TECHNOLOGY-
dc.citation.titleGREENHOUSE GASES-SCIENCE AND TECHNOLOGY-
dc.citation.volume7-
dc.citation.number6-
dc.citation.startPage1141-
dc.citation.endPage1149-
dc.type.rimsART-
dc.type.docTypeArticle-
dc.description.journalClass1-
dc.description.journalRegisteredClassscie-
dc.description.journalRegisteredClassscopus-
dc.relation.journalResearchAreaEnergy & Fuels-
dc.relation.journalResearchAreaEngineering-
dc.relation.journalResearchAreaEnvironmental Sciences & Ecology-
dc.relation.journalWebOfScienceCategoryEnergy & Fuels-
dc.relation.journalWebOfScienceCategoryEngineering, Environmental-
dc.relation.journalWebOfScienceCategoryEnvironmental Sciences-
dc.subject.keywordPlusDECOMPOSITION-
dc.subject.keywordPlusCOMBUSTION-
dc.subject.keywordPlusABATEMENT-
dc.subject.keywordAuthorPFCs-
dc.subject.keywordAuthorCF4 hydrolysis-
dc.subject.keywordAuthorcalcium hydroxide-
dc.subject.keywordAuthorCaF2-
dc.subject.keywordAuthorprocess simulation-
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