Innovative two-stage fermentation system converting organic solid waste to hydrogen and methane유기성 고형폐기물을 수소 및 메탄으로 전환하는 혁신적인 이단 발효 공정

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dc.contributor.advisorShin, Hang-Sik-
dc.contributor.advisor신항식-
dc.contributor.authorKim, Dong-Hoon-
dc.contributor.author김동훈-
dc.date.accessioned2011-12-13T02:23:33Z-
dc.date.available2011-12-13T02:23:33Z-
dc.date.issued2008-
dc.identifier.urihttp://library.kaist.ac.kr/search/detail/view.do?bibCtrlNo=295255&flag=dissertation-
dc.identifier.urihttp://hdl.handle.net/10203/30594-
dc.description학위논문(박사) - 한국과학기술원 : 건설및환경공학과, 2008.2, [ xiv, 166 p. ]-
dc.description.abstractHydrogen is regarded as the most promising future energy carrier because of its environmentally friendly aspect and high energy yield. Conventional physico-chemical methods for $H_2$ are energy intensive and generate green house gases; thus interest in biohydrogen has increased substantially. Among various biological ways, dark fermentation is considered to be practically applicable since its production rate is fast and could degrade organic solid waste such as food waste and sewage sludge. However, as there is a limitation of waste degradation and energy recovery in $H_2$ fermentation, second stage process such as $CH_4$ fermentation should be followed. Therefore, the main objective of this work was to develop an innovative two-stage fermentation system converting organic solid waste to $H_2$ and $CH_4$. Firstly, continuous pilot-scale $H_2$ fermenter treating food waste was operated at various C/N ratios. Although stable $H_2$ production was achieved after 45 d of start-up, $H_2$ yield was limited to 0.53 mol $H_2/mol$ hexose_{added} which is equivalent to 2.43% of total energy content in the food waste. Moreover, increase of C/N ratio decreased the $H_2$ yield, and alkaline shock treatment was not a permanent method recovering the performance. In order to overcome the limited performance of current $H_2$ fermentation method treating organic solid waste, an innovative method named ‘$H_2$ fermentation of food waste without adding external inoculum’ was suggested. This method was found to be feasible if proper pretreatments were applied by inhibiting LAB activity. Especially, the heat treatment (90\degC for 20min) was the most effective method and $H_2$ production was increased with the pretreatment heating temperature increase. Optimal substrate concentration was 30 g Carbo. COD/L and the decrease of $H_2$ yield at higher substrate concentration was due to product inhibition. Scaled-up fermenter (3 L) where heat-treated food waste was added showed a clear...eng
dc.languageeng-
dc.publisher한국과학기술원-
dc.subjectContinuous pilot-scale hydrogen production-
dc.subjectIntrinsic inoculum-
dc.subjecttwo-stage fermentation system-
dc.subject파일럿 스케일의 연속 수소 발효-
dc.subject무식종-
dc.subject이단 발효-
dc.subjectContinuous pilot-scale hydrogen production-
dc.subjectIntrinsic inoculum-
dc.subjecttwo-stage fermentation system-
dc.subject파일럿 스케일의 연속 수소 발효-
dc.subject무식종-
dc.subject이단 발효-
dc.titleInnovative two-stage fermentation system converting organic solid waste to hydrogen and methane-
dc.title.alternative유기성 고형폐기물을 수소 및 메탄으로 전환하는 혁신적인 이단 발효 공정-
dc.typeThesis(Ph.D)-
dc.identifier.CNRN295255/325007 -
dc.description.department한국과학기술원 : 건설및환경공학과, -
dc.identifier.uid020045025-
dc.contributor.localauthorShin, Hang-Sik-
dc.contributor.localauthor신항식-
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