Conversion of organic solid waste to hydrogen and methane by two-stage fermentation system with reuse of methane fermenter effluent as diluting water in hydrogen fermentation

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dc.contributor.authorJung, Kyung-Wonko
dc.contributor.authorMoon, Chung-Manko
dc.contributor.authorCho, Si-Kyungko
dc.contributor.authorKim, Sang-Hyounko
dc.contributor.authorShin, Hang-Sikko
dc.contributor.authorKim, Dong-Hoonko
dc.date.accessioned2014-12-16-
dc.date.available2014-12-16-
dc.date.created2013-08-26-
dc.date.created2013-08-26-
dc.date.issued2013-07-
dc.identifier.citationBIORESOURCE TECHNOLOGY, v.139, pp.120 - 127-
dc.identifier.issn0960-8524-
dc.identifier.urihttp://hdl.handle.net/10203/192672-
dc.description.abstractIn this study, a two-stage system converting organic solid waste (food waste + sewage sludge) to H-2 and CH4 was operated. In the first stage of dark fermentative hydrogen production (DFHP), a recently proposed method that does not require external inoculum, was applied. In the second stage, anaerobic sequencing batch reactor (ASBR) and an up-flow anaerobic sludge blanket reactor (UASBr) were followed to treat H-2 fermenter effluent. (H-2 + CH4-ASBR) system showed better performance in terms of total biogas conversion (78.6%), while higher biogas production rate (2.03 L H-2/L-system/d, 1.96 L CH4/L-system/d) was achieved in (H-2 + CH4-UASBr) system. To reduce the alkali addition requirement in DFHP process, CH4 fermenter effluent was tested as a diluting water. Both the ASBR and UASBr effluent was effective to keep the pH above 6 without CH4 production. In case of using ASBR effluent, H-2 production dropped by 15%, but alkali addition requirement was reduced by 50%. (C) 2013 Elsevier Ltd. All rights reserved.-
dc.languageEnglish-
dc.publisherELSEVIER SCI LTD-
dc.subjectFOOD WASTE-
dc.subjectPERFORMANCE-
dc.subjectPH-
dc.titleConversion of organic solid waste to hydrogen and methane by two-stage fermentation system with reuse of methane fermenter effluent as diluting water in hydrogen fermentation-
dc.typeArticle-
dc.identifier.wosid000321163100018-
dc.identifier.scopusid2-s2.0-84877325439-
dc.type.rimsART-
dc.citation.volume139-
dc.citation.beginningpage120-
dc.citation.endingpage127-
dc.citation.publicationnameBIORESOURCE TECHNOLOGY-
dc.identifier.doi10.1016/j.biortech.2013.04.041-
dc.embargo.liftdate9999-12-31-
dc.embargo.terms9999-12-31-
dc.contributor.localauthorShin, Hang-Sik-
dc.contributor.nonIdAuthorKim, Sang-Hyoun-
dc.contributor.nonIdAuthorKim, Dong-Hoon-
dc.type.journalArticleArticle-
dc.subject.keywordAuthorTwo-stage system-
dc.subject.keywordAuthorFood waste-
dc.subject.keywordAuthorSewage sludge-
dc.subject.keywordAuthorAnaerobic sequencing batch reactor-
dc.subject.keywordAuthorUp-flow anaerobic sludge blanket-
dc.subject.keywordPlusFOOD WASTE-
dc.subject.keywordPlusPERFORMANCE-
dc.subject.keywordPlusPH-
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