Bioethanol production from micro-algae, Schizocytrium sp., using hydrothermal treatment and biological conversion
DC Field | Value | Language |
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dc.contributor.author | Kim, Jung Kon | - |
dc.contributor.author | Um, Byung-Hwan | - |
dc.contributor.author | Kim, Tae Hyun | - |
dc.date.accessioned | 2021-06-23T08:06:16Z | - |
dc.date.available | 2021-06-23T08:06:16Z | - |
dc.date.created | 2021-01-21 | - |
dc.date.issued | 2012-02 | - |
dc.identifier.issn | 0256-1115 | - |
dc.identifier.uri | https://scholarworks.bwise.kr/erica/handle/2021.sw.erica/33863 | - |
dc.description.abstract | Hydrothermal fractionation for micro-algae, Schizocytrium sp., was investigated to separate sugars, lipids, and proteins. This fractionation process produced protein-rich solid cake and liquid hydrolysates, which contained oligomeric sugars and lipids. Oligomeric sugars and lipids were easily separated by liquid-liquid separation. Sugars in the separated hydrolyzate were determined to be mainly D-glucose and L-galactose. Fractionation conditions were optimized by response surface methodology (RSM). Optimal conditions were found to be 115.5 degrees C of reaction temperature, 46.7 min of reaction time, and 25% (w/w) of solid loading. The model predicted that maximum oligomeric sugar yield (based on untreated micro-algae weight), which can be recovered by hydrothermal fractionation at the optimum conditions, was 19.4 wt% (based on the total biomass weight). Experimental results were in agreement with the model prediction of 16.6 wt%. Production of bioethanol using micro-algae-induced glucan and E. coli KO11 was tested with SSF (simultaneous saccharification and fermentation), which resulted in 11.8 g-ethanol/l was produced from 25.7 g/l of glucose; i.e. the theoretical maximum ethanol yield based on glucan in hydrolyzate was 89.8%. | - |
dc.language | 영어 | - |
dc.language.iso | en | - |
dc.publisher | KOREAN INST CHEM ENGINEERS+ | - |
dc.title | Bioethanol production from micro-algae, Schizocytrium sp., using hydrothermal treatment and biological conversion | - |
dc.type | Article | - |
dc.contributor.affiliatedAuthor | Kim, Tae Hyun | - |
dc.identifier.doi | 10.1007/s11814-011-0169-3 | - |
dc.identifier.scopusid | 2-s2.0-84856496883 | - |
dc.identifier.wosid | 000299648500012 | - |
dc.identifier.bibliographicCitation | KOREAN JOURNAL OF CHEMICAL ENGINEERING, v.29, no.2, pp.209 - 214 | - |
dc.relation.isPartOf | KOREAN JOURNAL OF CHEMICAL ENGINEERING | - |
dc.citation.title | KOREAN JOURNAL OF CHEMICAL ENGINEERING | - |
dc.citation.volume | 29 | - |
dc.citation.number | 2 | - |
dc.citation.startPage | 209 | - |
dc.citation.endPage | 214 | - |
dc.type.rims | ART | - |
dc.type.docType | Article | - |
dc.description.journalClass | 1 | - |
dc.description.isOpenAccess | N | - |
dc.description.journalRegisteredClass | scie | - |
dc.description.journalRegisteredClass | scopus | - |
dc.description.journalRegisteredClass | kci | - |
dc.relation.journalResearchArea | Chemistry | - |
dc.relation.journalResearchArea | Engineering | - |
dc.relation.journalWebOfScienceCategory | Chemistry, Multidisciplinary | - |
dc.relation.journalWebOfScienceCategory | Engineering, Chemical | - |
dc.subject.keywordPlus | RESPONSE-SURFACE METHODOLOGY | - |
dc.subject.keywordPlus | ETHANOL-PRODUCTION | - |
dc.subject.keywordPlus | CORN STOVER | - |
dc.subject.keywordPlus | ALKALINE PROTEASE | - |
dc.subject.keywordPlus | ZYMOMONAS-MOBILIS | - |
dc.subject.keywordPlus | LIPID PRODUCTION | - |
dc.subject.keywordPlus | AQUEOUS AMMONIA | - |
dc.subject.keywordPlus | PAPER SLUDGE | - |
dc.subject.keywordPlus | OPTIMIZATION | - |
dc.subject.keywordPlus | FERMENTATION | - |
dc.subject.keywordAuthor | Biofuel | - |
dc.subject.keywordAuthor | Simultaneous Saccharification and Fermentation (SSF) | - |
dc.subject.keywordAuthor | Fractionation | - |
dc.subject.keywordAuthor | KO11 | - |
dc.subject.keywordAuthor | Hot Water | - |
dc.subject.keywordAuthor | Schizochytrium sp. | - |
dc.identifier.url | https://link.springer.com/article/10.1007%2Fs11814-011-0169-3 | - |
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