Full metadata record
DC Field | Value | Language |
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dc.contributor.author | Brand, Steffen | - |
dc.contributor.author | Susanti, Ratna Frida | - |
dc.contributor.author | Kim, Seok Ki | - |
dc.contributor.author | Lee, Hong-shik | - |
dc.contributor.author | Kim, Jaehoon | - |
dc.contributor.author | Sang, Byung-In | - |
dc.date.accessioned | 2024-01-20T11:32:37Z | - |
dc.date.available | 2024-01-20T11:32:37Z | - |
dc.date.created | 2022-01-10 | - |
dc.date.issued | 2013-09-15 | - |
dc.identifier.issn | 0360-5442 | - |
dc.identifier.uri | https://pubs.kist.re.kr/handle/201004/127663 | - |
dc.description.abstract | In this study, the influence of various physical process parameters on the liquefaction of lignocellulosic biomass (pine wood) in supercritical ethanol was investigated. The parameters include reaction temperature (280-400 degrees C), initial nitrogen pressure (0.4-7.5 MPa), reaction time (0-240 min), and biomass-to-solvent ratio (0.06-0.25 g/g). The reaction temperature and residence time were found to have a more significant effect on biomass conversion and product yield than pressure and biomass-to-solvent ratio had; conversion in the range 34.0-98.1% and biocrude yield in the range 15.8-59.9 wt% were observed depending on the process parameters. Despite the absence of catalysts and external hydrogen source, solid biomass to liquid and gaseous products conversion of 98.1%, and a high biocrude yield of approximately 65.8 wt% were achieved at 400 degrees C, 120 min, and a biomass-to-solvent ratio of 0.06 g/g. Moreover, the biocrude contained considerably lower amounts of oxygen and higher amounts of carbon and hydrogen, resulting in a substantially higher heating value (>30 MJ/kg) as compared to raw feed-stock (20.4 MJ/kg). A comparison with sub- or supercritical water-based liquefaction revealed that supercritical ethanol produced biocrude with a lower molecular weight and much better yield. Finally, a new biomass liquefaction reaction mechanism associated with supercritical ethanol is proposed. Crown Copyright (C) 2013 Published by Elsevier Ltd. All rights reserved. | - |
dc.language | English | - |
dc.publisher | PERGAMON-ELSEVIER SCIENCE LTD | - |
dc.subject | PROMOTED H-DONATION | - |
dc.subject | COAL CONVERSION | - |
dc.subject | OIL PRODUCTS | - |
dc.subject | DONOR MEDIA | - |
dc.subject | WATER | - |
dc.subject | WOOD | - |
dc.subject | ALCOHOLS | - |
dc.subject | LIGNIN | - |
dc.subject | SOLVENTS | - |
dc.subject | SLUDGE | - |
dc.title | Supercritical ethanol as an enhanced medium for lignocellulosic biomass liquefaction: Influence of physical process parameters | - |
dc.type | Article | - |
dc.identifier.doi | 10.1016/j.energy.2013.06.049 | - |
dc.description.journalClass | 1 | - |
dc.identifier.bibliographicCitation | ENERGY, v.59, pp.173 - 182 | - |
dc.citation.title | ENERGY | - |
dc.citation.volume | 59 | - |
dc.citation.startPage | 173 | - |
dc.citation.endPage | 182 | - |
dc.description.journalRegisteredClass | scie | - |
dc.description.journalRegisteredClass | scopus | - |
dc.identifier.wosid | 000324787600017 | - |
dc.identifier.scopusid | 2-s2.0-84883277396 | - |
dc.relation.journalWebOfScienceCategory | Thermodynamics | - |
dc.relation.journalWebOfScienceCategory | Energy & Fuels | - |
dc.relation.journalResearchArea | Thermodynamics | - |
dc.relation.journalResearchArea | Energy & Fuels | - |
dc.type.docType | Article | - |
dc.subject.keywordPlus | PROMOTED H-DONATION | - |
dc.subject.keywordPlus | COAL CONVERSION | - |
dc.subject.keywordPlus | OIL PRODUCTS | - |
dc.subject.keywordPlus | DONOR MEDIA | - |
dc.subject.keywordPlus | WATER | - |
dc.subject.keywordPlus | WOOD | - |
dc.subject.keywordPlus | ALCOHOLS | - |
dc.subject.keywordPlus | LIGNIN | - |
dc.subject.keywordPlus | SOLVENTS | - |
dc.subject.keywordPlus | SLUDGE | - |
dc.subject.keywordAuthor | Supercritical ethanol | - |
dc.subject.keywordAuthor | Liquefaction | - |
dc.subject.keywordAuthor | Lignocellulosic biomass | - |
dc.subject.keywordAuthor | Biocrude | - |
dc.subject.keywordAuthor | Hydrogen donor | - |
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