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Biodiesel production by enzymatic process using Jatropha oil and waste soybean oil

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dc.contributor.authorLee, Ja Hyun-
dc.contributor.authorKim, Sung Bong-
dc.contributor.authorYoo, Hah Young-
dc.contributor.authorSuh, Young Joon-
dc.contributor.authorKang, Gyung Bo-
dc.contributor.authorJang, Woo In-
dc.contributor.authorKang, Jongwon-
dc.contributor.authorPark, Chulhwan-
dc.contributor.authorKim, Seung Wook-
dc.date.accessioned2021-09-06T00:28:05Z-
dc.date.available2021-09-06T00:28:05Z-
dc.date.created2021-06-14-
dc.date.issued2013-07-
dc.identifier.issn1226-8372-
dc.identifier.urihttps://scholar.korea.ac.kr/handle/2021.sw.korea/102930-
dc.description.abstractIn this study, non-edible Jatropha oil and postcooking waste soybean oil were utilized for enzymatic biodiesel production. The process was optimized by using a statistical method. In addition, a novel continuous process using co-immobilized Rhizopus oryzae and Candida rugosa lipases was developed. The optimum conditions for the batch process were determined to be a reaction temperature of 45oC, an agitation speed of 250 rpm, 10 wt% of water, and 20% of immobilized lipases. A conversion of about 98% at 4 h could be achieved for biodiesel production using Jatropha oil, while a conversion of about 97% at 4 h was achieved from waste soybean oil. A packed bed reactor charged with co-immobilized lipases was employed for continuous biodiesel production from Jatropha and waste soybean oil. The reactor consisted of a jacketed glass column (ID 25 mm x 130 mm), in which a temperature of 45A degrees C was maintained by water circulation. A maximum conversion of about 80% in 24 h at a flow rate of 0.8 mL/ min was achieved with the continuous process, whereas in the two-stage continuous process, a conversion of about 90% in 72 h was attained at a flow rate of 0.1 mL/min.-
dc.languageEnglish-
dc.language.isoen-
dc.publisherKOREAN SOC BIOTECHNOLOGY & BIOENGINEERING-
dc.subjectPACKED-BED REACTOR-
dc.subjectFREE FATTY-ACIDS-
dc.subjectRHIZOPUS-ORYZAE-
dc.subjectCANDIDA-RUGOSA-
dc.subjectOPTIMIZATION-
dc.subjectPRETREATMENT-
dc.subjectCONVERSION-
dc.subjectMIXTURE-
dc.subjectLIPASE-
dc.titleBiodiesel production by enzymatic process using Jatropha oil and waste soybean oil-
dc.typeArticle-
dc.contributor.affiliatedAuthorKim, Seung Wook-
dc.identifier.doi10.1007/s12257-012-0805-8-
dc.identifier.scopusid2-s2.0-84882566996-
dc.identifier.wosid000323244600010-
dc.identifier.bibliographicCitationBIOTECHNOLOGY AND BIOPROCESS ENGINEERING, v.18, no.4, pp.703 - 708-
dc.relation.isPartOfBIOTECHNOLOGY AND BIOPROCESS ENGINEERING-
dc.citation.titleBIOTECHNOLOGY AND BIOPROCESS ENGINEERING-
dc.citation.volume18-
dc.citation.number4-
dc.citation.startPage703-
dc.citation.endPage708-
dc.type.rimsART-
dc.type.docTypeArticle-
dc.identifier.kciidART001799190-
dc.description.journalClass1-
dc.description.journalRegisteredClassscie-
dc.description.journalRegisteredClassscopus-
dc.description.journalRegisteredClasskci-
dc.relation.journalResearchAreaBiotechnology & Applied Microbiology-
dc.relation.journalWebOfScienceCategoryBiotechnology & Applied Microbiology-
dc.subject.keywordPlusPACKED-BED REACTOR-
dc.subject.keywordPlusFREE FATTY-ACIDS-
dc.subject.keywordPlusRHIZOPUS-ORYZAE-
dc.subject.keywordPlusCANDIDA-RUGOSA-
dc.subject.keywordPlusOPTIMIZATION-
dc.subject.keywordPlusPRETREATMENT-
dc.subject.keywordPlusCONVERSION-
dc.subject.keywordPlusMIXTURE-
dc.subject.keywordPlusLIPASE-
dc.subject.keywordAuthorbiodiesel-
dc.subject.keywordAuthorcontinuous process-
dc.subject.keywordAuthorlipase-
dc.subject.keywordAuthorresponse surface methodology-
dc.subject.keywordAuthoroptimization-
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