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Growth medium sterilization using decomposition of peracetic acid for more cost-efficient production of omega-3 fatty acids by Aurantiochytrium

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dc.contributor.authorCho, Chang-Ho-
dc.contributor.authorShin, Won-Sub-
dc.contributor.authorWoo, Do-Wook-
dc.contributor.authorKwon, Jong-Hee-
dc.date.accessioned2022-12-26T17:01:37Z-
dc.date.available2022-12-26T17:01:37Z-
dc.date.issued2018-06-
dc.identifier.issn1615-7591-
dc.identifier.issn1615-7605-
dc.identifier.urihttps://scholarworks.gnu.ac.kr/handle/sw.gnu/11604-
dc.description.abstractAurantiochytrium can produce significant amounts of omega-3 fatty acids, specifically docosahexaenoic acid and docosapentaenoic acid. Use of a glucose-based medium for heterotrophic growth is needed to achieve a high growth rate and production of abundant lipids. However, heat sterilization for reliable cultivation is not appropriate to heat-sensitive materials and causes a conversion of glucose via browning (Maillard) reactions. Thus, the present study investigated the use of a direct degradation of Peracetic acid (PAA) for omega-3 production by Aurantiochytrium. Polymer-based bioreactor and glucose-containing media were chemically co-sterilized by 0.04% PAA and neutralized through a reaction with ferric ion (III) in HEPES buffer. Mono-cultivation was achieved without the need for washing steps and filtration, thereby avoiding the heat-induced degradation and dehydration of glucose. Use of chemically sterilized and neutralized medium, rather than heat-sterilized medium, led to a twofold faster growth rate and greater productivity of omega-3 fatty acids.-
dc.format.extent7-
dc.language영어-
dc.language.isoENG-
dc.publisherSPRINGER-
dc.titleGrowth medium sterilization using decomposition of peracetic acid for more cost-efficient production of omega-3 fatty acids by Aurantiochytrium-
dc.typeArticle-
dc.publisher.location미국-
dc.identifier.doi10.1007/s00449-018-1914-3-
dc.identifier.scopusid2-s2.0-85045025239-
dc.identifier.wosid000432600500006-
dc.identifier.bibliographicCitationBIOPROCESS AND BIOSYSTEMS ENGINEERING, v.41, no.6, pp 803 - 809-
dc.citation.titleBIOPROCESS AND BIOSYSTEMS ENGINEERING-
dc.citation.volume41-
dc.citation.number6-
dc.citation.startPage803-
dc.citation.endPage809-
dc.type.docTypeArticle-
dc.description.isOpenAccessN-
dc.description.journalRegisteredClasssci-
dc.description.journalRegisteredClassscie-
dc.description.journalRegisteredClassscopus-
dc.relation.journalResearchAreaBiotechnology & Applied Microbiology-
dc.relation.journalResearchAreaEngineering-
dc.relation.journalWebOfScienceCategoryBiotechnology & Applied Microbiology-
dc.relation.journalWebOfScienceCategoryEngineering, Chemical-
dc.subject.keywordPlusDOCOSAHEXAENOIC ACID-
dc.subject.keywordPlusBIODIESEL-
dc.subject.keywordPlusGLYCEROL-
dc.subject.keywordPlusWATER-
dc.subject.keywordAuthorAurantiochytrium-
dc.subject.keywordAuthorChemical sterilization-
dc.subject.keywordAuthorPeracetic acid-
dc.subject.keywordAuthorOmega-3-
dc.subject.keywordAuthorMaillard reaction-
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