Continuous biohydrogen production in a CSTR using starch as a substrate

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dc.contributor.authorArooj, Muhammad Farhanko
dc.contributor.authorHan, Sun-Keeko
dc.contributor.authorKim, Sang-Hyounko
dc.contributor.authorKim, Dong-Hoonko
dc.contributor.authorShin, Hang-Sikko
dc.date.accessioned2008-09-05-
dc.date.available2008-09-05-
dc.date.created2012-02-06-
dc.date.created2012-02-06-
dc.date.issued2008-04-
dc.identifier.citationINTERNATIONAL JOURNAL OF HYDROGEN ENERGY, v.33, no.13, pp.3289 - 3294-
dc.identifier.issn0360-3199-
dc.identifier.urihttp://hdl.handle.net/10203/7309-
dc.description.abstractThere are few reports on continuous biohydrogen production from biopolymers like starch, because most previous studies on continuous operation were performed using simple hydrolysates such as glucose and sucrose. This study was, therefore, carried out to investigate continuous biohydrogen production in an anaerobic continuous stirred-tank reactor (CSTR) using corn starch as a substrate for 158 days. The reactor was seeded with mixed community sludge from an anaerobic digester at a local wastewater treatment facility. Volatile fatty acids (VFA) profile supported the fact that butyrate to acetate (B/A) ratio was the most important parameter to justify hydrogen yield at various hydraulic retention times (HRT). Maximum hydrogen yield of 0.92mol H-2/mol glucose(added) Was observed at 12 h HRT with the highest B/A ratio of 4.3. Also, estimation modeling to quantify homoacetogenism was conducted and H-2-consuming acetate production at various HRTs was estimated. Estimation modeling revealed that at short HRTs of 9, 6 and 4h, acetate concentration plays a trivial role. Therefore, butyrate concentration alone instead of butyrate to acetate ratio (B/A) justifies the trend of H-2 yield at short HRTs. (C) 2008 International Association for Hydrogen Energy. Published by Elsevier Ltd. All rights reserved.-
dc.description.sponsorshipThis work was supported by Grant no. M1-0203-00-0063 by National Research Laboratory Program of Korean Ministry of Science and Technology.en
dc.languageEnglish-
dc.language.isoen_USen
dc.publisherPERGAMON-ELSEVIER SCIENCE LTD-
dc.subjectFERMENTATIVE HYDROGEN-PRODUCTION-
dc.subjectORGANIC FRACTION-
dc.subjectOPTIMIZATION-
dc.subjectGLUCOSE-
dc.subjectREACTOR-
dc.subjectPH-
dc.titleContinuous biohydrogen production in a CSTR using starch as a substrate-
dc.typeArticle-
dc.identifier.wosid000258518000005-
dc.identifier.scopusid2-s2.0-47049085416-
dc.type.rimsART-
dc.citation.volume33-
dc.citation.issue13-
dc.citation.beginningpage3289-
dc.citation.endingpage3294-
dc.citation.publicationnameINTERNATIONAL JOURNAL OF HYDROGEN ENERGY-
dc.identifier.doi10.1016/j.ijhydene.2008.04.022-
dc.embargo.liftdate9999-12-31-
dc.embargo.terms9999-12-31-
dc.contributor.localauthorShin, Hang-Sik-
dc.type.journalArticleArticle-
dc.subject.keywordAuthorcontinuous stirred-tank reactor-
dc.subject.keywordAuthorhydraulic retention time-
dc.subject.keywordAuthorcorn starch-
dc.subject.keywordAuthorvolatile fatty acids-
dc.subject.keywordAuthorhomoacetogenism-
dc.subject.keywordPlusFERMENTATIVE HYDROGEN-PRODUCTION-
dc.subject.keywordPlusORGANIC FRACTION-
dc.subject.keywordPlusOPTIMIZATION-
dc.subject.keywordPlusGLUCOSE-
dc.subject.keywordPlusREACTOR-
dc.subject.keywordPlusPH-
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