Full metadata record
DC Field | Value | Language |
---|---|---|
dc.contributor.author | 상병인 | - |
dc.date.accessioned | 2018-03-15T12:58:25Z | - |
dc.date.available | 2018-03-15T12:58:25Z | - |
dc.date.issued | 2014-01 | - |
dc.identifier.citation | International Journal of Hydrogen Energy, Vol 39, No 3, 16 January 2014, Pages 1262-1273 | en_US |
dc.identifier.issn | 0360-3199 | - |
dc.identifier.uri | https://www.sciencedirect.com/science/article/pii/S0360319913026542 | - |
dc.identifier.uri | http://hdl.handle.net/20.500.11754/47485 | - |
dc.description.abstract | A comparative gasification study between pure glycerol and two different kinds of crude glycerol is conducted in supercritical water under various operating parameters to investigate the effect of different compositions in crude glycerol on the gasification behaviors. Among various types of impurities in the crude glycerol, fatty acid methyl esters (FAMEs) exhibit a negative effect on the gas yield and gasification efficiency of crude glycerol in a batch apparatus due to the enhanced tar/char formation. At 650 degrees C and 5 wt%, gasification in a continuous apparatus exhibits H-2 yields of 26.44 and 35.85 mmol/g feed in 1 min for both types of crude glycerol, which could not be achieved by the batch system even with the reaction time extended up to 120 min. A shorter duration in the non-supercritical state may be the dominant parameter that leads to complete conversion of FAMEs and total gasification of crude glycerol using the continuous system. Crown Copyright (C) 2013, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved. | en_US |
dc.description.sponsorship | This project was supported by the Korea Ministry of the Environment as a “Converging Technology Project.” Additional support from the Basic Science Research Program through the National Research Foundation of Korea Grant funded by the Ministry of Science, ICT & Future Planning (2013R1A1A2061020) was appreciated. | en_US |
dc.language.iso | en | en_US |
dc.publisher | PERGAMON-ELSEVIER SCIENCE LTD, THE BOULEVARD, LANGFORD LANE, KIDLINGTON, OXFORD OX5 1GB, ENGLAND | en_US |
dc.subject | Hydrogen | en_US |
dc.subject | Crude glycerol | en_US |
dc.subject | Supercritical water | en_US |
dc.subject | FAMEs | en_US |
dc.subject | Batch system | en_US |
dc.subject | Continuous system | en_US |
dc.subject | HOT COMPRESSED WATER | en_US |
dc.subject | BIOMASS GASIFICATION | en_US |
dc.subject | HYDROGEN-PRODUCTION | en_US |
dc.subject | BIODIESEL PRODUCTION | en_US |
dc.subject | MODEL COMPOUNDS | en_US |
dc.subject | COKE FORMATION | en_US |
dc.subject | HEATING RATE | en_US |
dc.subject | GLUCOSE | en_US |
dc.subject | PYROLYSIS | en_US |
dc.subject | PRODUCTS | en_US |
dc.title | Hydrothermal gasification of pure and crude glycerol in supercritical water: A comparative study | en_US |
dc.type | Article | en_US |
dc.relation.no | 3 | - |
dc.relation.volume | 39 | - |
dc.identifier.doi | 10.1016/j.ijhydene.2013.10.139 | - |
dc.relation.page | 1262-1273 | - |
dc.relation.journal | INTERNATIONAL JOURNAL OF HYDROGEN ENERGY | - |
dc.contributor.googleauthor | Dianningrum, Laras W. | - |
dc.contributor.googleauthor | Choi, Haemin | - |
dc.contributor.googleauthor | Kim, Yunje | - |
dc.contributor.googleauthor | Jung, Kwang-Deog | - |
dc.contributor.googleauthor | Susanti, Ratna F. | - |
dc.contributor.googleauthor | Kim, Jaehoon | - |
dc.contributor.googleauthor | Sang, Byung-In | - |
dc.relation.code | 2014031541 | - |
dc.sector.campus | S | - |
dc.sector.daehak | COLLEGE OF ENGINEERING[S] | - |
dc.sector.department | DEPARTMENT OF CHEMICAL ENGINEERING | - |
dc.identifier.pid | biosang | - |
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