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Hydrosilylation-based UV-curable polydimethylsiloxane pervaporation membranes for n-butanol recovery

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dc.contributor.authorLee, Ju Yeon-
dc.contributor.authorHwang, Seon Oh-
dc.contributor.authorKim, Hyung-Ju-
dc.contributor.authorHong, Do-Young-
dc.contributor.authorLee, Jong Suk-
dc.contributor.authorLee, Jung-Hyun-
dc.date.accessioned2021-09-01T21:17:19Z-
dc.date.available2021-09-01T21:17:19Z-
dc.date.created2021-06-19-
dc.date.issued2019-01-31-
dc.identifier.issn1383-5866-
dc.identifier.urihttps://scholar.korea.ac.kr/handle/2021.sw.korea/68228-
dc.description.abstractUV-cured polydimethylsiloxane (PDMS) pervaporation membranes (pristine and mixed matrix membranes (MMMs) containing silicalite-1 particles) were fabricated by using a new class of hydrosilylation-based UV-curable PDMS to facilitate the manufacturing process as well as to enhance performance for n-butanol recovery. Unlike the pristine (heat- and UV-cured) PDMS membranes which showed no discernible difference in their morphology, the UV-cured MMM exhibited a more loosely-packed structure with a rougher surface due to the protuberant features compared to the conventional heat-cured MMM. It was attributed presumably to the different curing mechanisms as well as the different compositions and chemical structures of the PDMS used. Importantly, the UV-cured MMM exhibited a higher permeate flux with a similar separation factor compared to the heat-cured counterpart. Our UV-cured MMM further enhanced separation performance at the elevated temperature with the highest flux of similar to 1,520 g m(2) h(-1) and separation factor of similar to 19.8 at 60 degrees C. This flux enhancement of the UV-cured MMM was explained by its unique morphology (higher surface roughness and loosely-packed structure) and more pronounced temperature-dependent diffusivity enhancement. Our proposed strategy could provide a more efficient and commercially viable route to fabricate highly permeable PDMS-based pervaporation membranes for efficient butanol recovery in the bio-butanol production process.-
dc.languageEnglish-
dc.language.isoen-
dc.publisherELSEVIER SCIENCE BV-
dc.subjectDILUTE AQUEOUS-SOLUTIONS-
dc.subjectMIXED MATRIX MEMBRANES-
dc.subjectPERMSELECTIVE PERVAPORATION-
dc.subjectAGRICULTURAL RESIDUES-
dc.subjectCOMPOSITE MEMBRANES-
dc.subjectBIOFUEL PRODUCTION-
dc.subjectHYBRID MEMBRANES-
dc.subjectABE FERMENTATION-
dc.subjectETHANOL ABE-
dc.subjectSEPARATION-
dc.titleHydrosilylation-based UV-curable polydimethylsiloxane pervaporation membranes for n-butanol recovery-
dc.typeArticle-
dc.contributor.affiliatedAuthorLee, Jung-Hyun-
dc.identifier.doi10.1016/j.seppur.2018.07.045-
dc.identifier.scopusid2-s2.0-85050346709-
dc.identifier.wosid000449133600043-
dc.identifier.bibliographicCitationSEPARATION AND PURIFICATION TECHNOLOGY, v.209, pp.383 - 391-
dc.relation.isPartOfSEPARATION AND PURIFICATION TECHNOLOGY-
dc.citation.titleSEPARATION AND PURIFICATION TECHNOLOGY-
dc.citation.volume209-
dc.citation.startPage383-
dc.citation.endPage391-
dc.type.rimsART-
dc.type.docTypeArticle-
dc.description.journalClass1-
dc.description.journalRegisteredClassscie-
dc.description.journalRegisteredClassscopus-
dc.relation.journalResearchAreaEngineering-
dc.relation.journalWebOfScienceCategoryEngineering, Chemical-
dc.subject.keywordPlusDILUTE AQUEOUS-SOLUTIONS-
dc.subject.keywordPlusMIXED MATRIX MEMBRANES-
dc.subject.keywordPlusPERMSELECTIVE PERVAPORATION-
dc.subject.keywordPlusAGRICULTURAL RESIDUES-
dc.subject.keywordPlusCOMPOSITE MEMBRANES-
dc.subject.keywordPlusBIOFUEL PRODUCTION-
dc.subject.keywordPlusHYBRID MEMBRANES-
dc.subject.keywordPlusABE FERMENTATION-
dc.subject.keywordPlusETHANOL ABE-
dc.subject.keywordPlusSEPARATION-
dc.subject.keywordAuthorPolydimethylsiloxane-
dc.subject.keywordAuthorPervaporation membrane-
dc.subject.keywordAuthorMixed matrix membrane-
dc.subject.keywordAuthorUV-curing-
dc.subject.keywordAuthorButanol recovery-
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