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The first attempt at continuous-mode separation of racemic and meso-2,3-butanediol with high purities using a simulated-moving-bed process

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dc.contributor.authorLee, Chung-Gi-
dc.contributor.authorSong, Ye Jin-
dc.contributor.authorLee, Ki Bong-
dc.contributor.authorMun, Sungyong-
dc.date.accessioned2021-08-31T19:40:54Z-
dc.date.available2021-08-31T19:40:54Z-
dc.date.created2021-06-19-
dc.date.issued2019-12-25-
dc.identifier.issn1226-086X-
dc.identifier.urihttps://scholar.korea.ac.kr/handle/2021.sw.korea/60877-
dc.description.abstractTo maximize the industrial value of biologically produced 2,3-butanediol (BD), it is essential to separate BD into its stereoisomeric fractions, meso-BD and racemic-BD. To address such issue, a highly efficient BD-isomer separation process based on a simulated-moving-bed (SMB) mode was developed in this study. As a first step for this task, the competitive adsorption behaviors of meso-BD and racemic-BD on a properly selected adsorbent were investigated, and their relevant isotherm parameters were determined using inverse method. The determined isotherm parameters were then applied to the design of the BD-isomer separation process based on an SMB mode, which was carried out in such a way that both BD isomers could be separated with high purities and little losses in a continuous countercurrent mode. The performance of the designed SMB process for the targeted separation was experimentally investigated. It was confirmed from the experimental results that the BD-isomer separation SMB process, which was developed in this study for the first time, could be effective in the continuous-mode separation of meso-BD and racemic-BD with the purities higher than 99.9% and 97% respectively while maintaining their losses below 1%. The results of this study are expected to pave the way for establishing a highly economical process for a large-scale production of meso-BD and racemic-BD with high purities. (C) 2019 The Korean Society of Industrial and Engineering Chemistry. Published by Elsevier B.V. All rights reserved.-
dc.languageEnglish-
dc.language.isoen-
dc.publisherELSEVIER SCIENCE INC-
dc.subjectSTANDING-WAVE DESIGN-
dc.subject2,3-BUTANEDIOL PRODUCTION-
dc.subjectENANTIOMERS-
dc.subjectFERMENTATION-
dc.subjectOPTIMIZATION-
dc.subjectSMB-
dc.subjectSTRATEGIES-
dc.subjectRECOVERY-
dc.subjectREACTOR-
dc.subjectUNITS-
dc.titleThe first attempt at continuous-mode separation of racemic and meso-2,3-butanediol with high purities using a simulated-moving-bed process-
dc.typeArticle-
dc.contributor.affiliatedAuthorLee, Ki Bong-
dc.identifier.doi10.1016/j.jiec.2019.08.046-
dc.identifier.scopusid2-s2.0-85071476886-
dc.identifier.wosid000501658800076-
dc.identifier.bibliographicCitationJOURNAL OF INDUSTRIAL AND ENGINEERING CHEMISTRY, v.80, pp.677 - 685-
dc.relation.isPartOfJOURNAL OF INDUSTRIAL AND ENGINEERING CHEMISTRY-
dc.citation.titleJOURNAL OF INDUSTRIAL AND ENGINEERING CHEMISTRY-
dc.citation.volume80-
dc.citation.startPage677-
dc.citation.endPage685-
dc.type.rimsART-
dc.type.docTypeArticle-
dc.identifier.kciidART002542444-
dc.description.journalClass1-
dc.description.journalRegisteredClassscie-
dc.description.journalRegisteredClassscopus-
dc.description.journalRegisteredClasskci-
dc.relation.journalResearchAreaChemistry-
dc.relation.journalResearchAreaEngineering-
dc.relation.journalWebOfScienceCategoryChemistry, Multidisciplinary-
dc.relation.journalWebOfScienceCategoryEngineering, Chemical-
dc.subject.keywordPlusSTANDING-WAVE DESIGN-
dc.subject.keywordPlus2,3-BUTANEDIOL PRODUCTION-
dc.subject.keywordPlusENANTIOMERS-
dc.subject.keywordPlusFERMENTATION-
dc.subject.keywordPlusOPTIMIZATION-
dc.subject.keywordPlusSMB-
dc.subject.keywordPlusSTRATEGIES-
dc.subject.keywordPlusRECOVERY-
dc.subject.keywordPlusREACTOR-
dc.subject.keywordPlusUNITS-
dc.subject.keywordAuthorSimulated moving bed-
dc.subject.keywordAuthor2,3-Butanediol isomers-
dc.subject.keywordAuthorMeso-2,3-Butanediol-
dc.subject.keywordAuthorContinuous separation-
dc.subject.keywordAuthorProcess design-
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