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Comparison of Amberchrom-CG161C and Dowex99 as the adsorbent of a four-zone simulated moving bed process for removal of acetic acid from biomass hydrolyzate

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dc.contributor.authorNam, Hee-Geun-
dc.contributor.authorJo, Se-Hee-
dc.contributor.authorMun, Sungyong-
dc.date.accessioned2022-07-16T18:53:48Z-
dc.date.available2022-07-16T18:53:48Z-
dc.date.created2021-05-12-
dc.date.issued2011-10-
dc.identifier.issn1359-5113-
dc.identifier.urihttps://scholarworks.bwise.kr/hanyang/handle/2021.sw.hanyang/167487-
dc.description.abstractOne of the important steps in the application of biomass to producing sugars, which can be converted into bio-ethanol and other valuable chemicals by fermentation, is to hydrolyze the biomass components by sulfuric acid. It was reported that such a hydrolysis entailed the generation of acetic acid, which has been recognized as a key impurity to be surely removed from the biomass hydrolyzate for ensuring high fermentability of the hydrolyzed sugars. Regarding such a removal task, there has been a previous application of a simulated moving bed (SMB) process based on the Dowex99 adsorbent, whose performance, however, was limited by low selectivity between acetic acid and sugars. To overcome such a limitation, another adsorbent alternative to Dowex99 was searched in this study. It was found that Amberchrom-CG161C allowed higher selectivity between acetic acid and sugars than Dowex99. To investigate the relative superiority of Amberchrom-CG161C over Dowex99 as the adsorbent of an SMB process for removing acetic acid from the biomass hydrolyzate, the two SMB processes based on Amberchrom-CG161C and Dowex99 were optimized using the SMB optimization tool based on standing wave design (SWD) method. The optimization results revealed that the Amberchrom-CG161C SMB outperformed the Dowex99 SMB by a wide margin.-
dc.language영어-
dc.language.isoen-
dc.publisherELSEVIER SCI LTD-
dc.titleComparison of Amberchrom-CG161C and Dowex99 as the adsorbent of a four-zone simulated moving bed process for removal of acetic acid from biomass hydrolyzate-
dc.typeArticle-
dc.contributor.affiliatedAuthorMun, Sungyong-
dc.identifier.doi10.1016/j.procbio.2011.08.004-
dc.identifier.scopusid2-s2.0-80052725534-
dc.identifier.wosid000295913700021-
dc.identifier.bibliographicCitationPROCESS BIOCHEMISTRY, v.46, no.10, pp.2044 - 2053-
dc.relation.isPartOfPROCESS BIOCHEMISTRY-
dc.citation.titlePROCESS BIOCHEMISTRY-
dc.citation.volume46-
dc.citation.number10-
dc.citation.startPage2044-
dc.citation.endPage2053-
dc.type.rimsART-
dc.type.docTypeArticle-
dc.description.journalClass1-
dc.description.isOpenAccessN-
dc.description.journalRegisteredClassscie-
dc.description.journalRegisteredClassscopus-
dc.relation.journalResearchAreaBiochemistry & Molecular Biology-
dc.relation.journalResearchAreaBiotechnology & Applied Microbiology-
dc.relation.journalResearchAreaEngineering-
dc.relation.journalWebOfScienceCategoryBiochemistry & Molecular Biology-
dc.relation.journalWebOfScienceCategoryBiotechnology & Applied Microbiology-
dc.relation.journalWebOfScienceCategoryEngineering, Chemical-
dc.subject.keywordPlusSTANDING-WAVE DESIGN-
dc.subject.keywordPlusLINEAR-SYSTEMS-
dc.subject.keywordPlusCHROMATOGRAPHY-
dc.subject.keywordPlusSEPARATION-
dc.subject.keywordPlusSMB-
dc.subject.keywordPlusFERMENTATION-
dc.subject.keywordPlusENANTIOMERS-
dc.subject.keywordPlusDIFFUSION-
dc.subject.keywordPlusRECOVERY-
dc.subject.keywordPlusETHANOL-
dc.subject.keywordAuthorBiomass hydrolyzate-
dc.subject.keywordAuthorSugar recovery-
dc.subject.keywordAuthorDowex99-
dc.subject.keywordAuthorAmberchrom-CG161C-
dc.subject.keywordAuthorSimulated moving bed-
dc.subject.keywordAuthorStanding wave design-
dc.identifier.urlhttps://www.sciencedirect.com/science/article/pii/S1359511311002790?via%3Dihub-
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