Bioethanol production from corn stover using aqueous ammonia pretreatment and two-phase simultaneous saccharification and fermentation (TPSSF)
DC Field | Value | Language |
---|---|---|
dc.contributor.author | Li, Xuan | - |
dc.contributor.author | Kim, Tae Hyun | - |
dc.contributor.author | Nghiem, Nhuan P. | - |
dc.date.accessioned | 2021-06-23T13:02:41Z | - |
dc.date.available | 2021-06-23T13:02:41Z | - |
dc.date.created | 2021-01-21 | - |
dc.date.issued | 2010-08 | - |
dc.identifier.issn | 0960-8524 | - |
dc.identifier.uri | https://scholarworks.bwise.kr/erica/handle/2021.sw.erica/39627 | - |
dc.description.abstract | An integrated bioconversion process was developed to convert corn stover derived pentose and hexose to ethanol effectively. In this study, corn stover was pretreated by soaking in aqueous ammonia (SAA), which retained glucan (similar to 100%) and xylan (>80%) in the solids. The pretreated carbohydrates-rich corn stover was converted to ethanol via two-phase simultaneous saccharification and fermentation (TPSSF). This single-reactor process employed sequential simultaneous saccharification and fermentation (SSF), i.e. pentose conversion using recombinant Escherichia coli KO11 in the first phase, followed by hexose conversion with Saccharomyces cerevisiae D5A in the second phase. In the first phase, 88% of xylan digestibility was achieved through the synergistic action of xylanase and endo-glucanase with minimal glucan hydrolysis (10.5%). Overall, the TPSSF using 12-h SAA-treated corn stover resulted in the highest ethanol concentration (22.3 g/L), which was equivalent to 84% of the theoretical ethanol yield based on the total carbohydrates (glucan + xylan) in the untreated corn stover. (C) 2010 Elsevier Ltd. All rights reserved. | - |
dc.language | 영어 | - |
dc.language.iso | en | - |
dc.publisher | ELSEVIER SCI LTD | - |
dc.title | Bioethanol production from corn stover using aqueous ammonia pretreatment and two-phase simultaneous saccharification and fermentation (TPSSF) | - |
dc.type | Article | - |
dc.contributor.affiliatedAuthor | Kim, Tae Hyun | - |
dc.identifier.doi | 10.1016/j.biortech.2010.03.015 | - |
dc.identifier.scopusid | 2-s2.0-77951092628 | - |
dc.identifier.wosid | 000278035900025 | - |
dc.identifier.bibliographicCitation | BIORESOURCE TECHNOLOGY, v.101, no.15, pp.5910 - 5916 | - |
dc.relation.isPartOf | BIORESOURCE TECHNOLOGY | - |
dc.citation.title | BIORESOURCE TECHNOLOGY | - |
dc.citation.volume | 101 | - |
dc.citation.number | 15 | - |
dc.citation.startPage | 5910 | - |
dc.citation.endPage | 5916 | - |
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.relation.journalResearchArea | Agriculture | - |
dc.relation.journalResearchArea | Biotechnology & Applied Microbiology | - |
dc.relation.journalResearchArea | Energy & Fuels | - |
dc.relation.journalWebOfScienceCategory | Agricultural Engineering | - |
dc.relation.journalWebOfScienceCategory | Biotechnology & Applied Microbiology | - |
dc.relation.journalWebOfScienceCategory | Energy & Fuels | - |
dc.subject.keywordPlus | XYLOSE FERMENTATION | - |
dc.subject.keywordPlus | SOAKING | - |
dc.subject.keywordPlus | PATHWAY | - |
dc.subject.keywordAuthor | Integrated bioconversion process | - |
dc.subject.keywordAuthor | Bioethanol | - |
dc.subject.keywordAuthor | Soaking in aqueous ammonia (SAA) | - |
dc.subject.keywordAuthor | KO11 | - |
dc.subject.keywordAuthor | D5A yeast | - |
dc.identifier.url | https://www.sciencedirect.com/science/article/pii/S0960852410004694?via%3Dihub | - |
Items in ScholarWorks are protected by copyright, with all rights reserved, unless otherwise indicated.
55 Hanyangdeahak-ro, Sangnok-gu, Ansan, Gyeonggi-do, 15588, Korea+82-31-400-4269 sweetbrain@hanyang.ac.kr
COPYRIGHT © 2021 HANYANG UNIVERSITY. ALL RIGHTS RESERVED.
Certain data included herein are derived from the © Web of Science of Clarivate Analytics. All rights reserved.
You may not copy or re-distribute this material in whole or in part without the prior written consent of Clarivate Analytics.