Hydrogen-rich gas from catalytic steam gasification of biomass in a fixed bed reactor: Influence of particle size on gasification performance
The catalytic steam gasification of biomass was carried out in a lab-scale fixed bed reactor in order to evaluate the effects of particle size at different bed temperatures on the gasification performance. The bed temperature was varied from 600 to 900 °C and the biomass was separated into five diff...
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| Veröffentlicht in: | International journal of hydrogen energy 2009-02, Vol.34 (3), p.1260-1264 |
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| container_end_page | 1264 |
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| container_title | International journal of hydrogen energy |
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| creator | Luo, Siyi Xiao, Bo Guo, Xianjun Hu, Zhiquan Liu, Shiming He, Maoyun |
| description | The catalytic steam gasification of biomass was carried out in a lab-scale fixed bed reactor in order to evaluate the effects of particle size at different bed temperatures on the gasification performance. The bed temperature was varied from 600 to 900
°C and the biomass was separated into five different size fractions (below 0.075
mm, 0.075–0.15
mm, 0.15–0.3
mm, 0.3–0.6
mm and 0.6–1.2
mm). The results show that with decreasing particle size, the dry gas yield, carbon conversion efficiency and H
2 yield increased, and the content of char and tar decreased. And the differences due to particle sizes in gasification performance practically disappear as the higher temperature bound is approached. Hydrogen and carbon monoxide contents in the produced gas increase with decreasing particle size at 900
°C, reaching to 51.2% and 22.4%, respectively. |
| doi_str_mv | 10.1016/j.ijhydene.2008.10.088 |
| format | Article |
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°C and the biomass was separated into five different size fractions (below 0.075
mm, 0.075–0.15
mm, 0.15–0.3
mm, 0.3–0.6
mm and 0.6–1.2
mm). The results show that with decreasing particle size, the dry gas yield, carbon conversion efficiency and H
2 yield increased, and the content of char and tar decreased. And the differences due to particle sizes in gasification performance practically disappear as the higher temperature bound is approached. Hydrogen and carbon monoxide contents in the produced gas increase with decreasing particle size at 900
°C, reaching to 51.2% and 22.4%, respectively.</description><identifier>ISSN: 0360-3199</identifier><identifier>EISSN: 1879-3487</identifier><identifier>DOI: 10.1016/j.ijhydene.2008.10.088</identifier><identifier>CODEN: IJHEDX</identifier><language>eng</language><publisher>Kidlington: Elsevier Ltd</publisher><subject>Alternative fuels. Production and utilization ; Applied sciences ; Biomass ; Carbon ; Carbon monoxide ; Catalysis ; Catalysts ; Energy ; Exact sciences and technology ; Fuels ; Gasification ; Hydrogen ; Hydrogen-rich gas ; Particle size ; Reactors ; Steam gasification</subject><ispartof>International journal of hydrogen energy, 2009-02, Vol.34 (3), p.1260-1264</ispartof><rights>2008</rights><rights>2009 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c481t-296c3fb21ffee112f791b24374545c42e7b2c8878b95127075d866de83d833643</citedby></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://dx.doi.org/10.1016/j.ijhydene.2008.10.088$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,780,784,3549,27923,27924,45994</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=21140010$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Luo, Siyi</creatorcontrib><creatorcontrib>Xiao, Bo</creatorcontrib><creatorcontrib>Guo, Xianjun</creatorcontrib><creatorcontrib>Hu, Zhiquan</creatorcontrib><creatorcontrib>Liu, Shiming</creatorcontrib><creatorcontrib>He, Maoyun</creatorcontrib><title>Hydrogen-rich gas from catalytic steam gasification of biomass in a fixed bed reactor: Influence of particle size on gasification performance</title><title>International journal of hydrogen energy</title><description>The catalytic steam gasification of biomass was carried out in a lab-scale fixed bed reactor in order to evaluate the effects of particle size at different bed temperatures on the gasification performance. The bed temperature was varied from 600 to 900
°C and the biomass was separated into five different size fractions (below 0.075
mm, 0.075–0.15
mm, 0.15–0.3
mm, 0.3–0.6
mm and 0.6–1.2
mm). The results show that with decreasing particle size, the dry gas yield, carbon conversion efficiency and H
2 yield increased, and the content of char and tar decreased. And the differences due to particle sizes in gasification performance practically disappear as the higher temperature bound is approached. Hydrogen and carbon monoxide contents in the produced gas increase with decreasing particle size at 900
°C, reaching to 51.2% and 22.4%, respectively.</description><subject>Alternative fuels. Production and utilization</subject><subject>Applied sciences</subject><subject>Biomass</subject><subject>Carbon</subject><subject>Carbon monoxide</subject><subject>Catalysis</subject><subject>Catalysts</subject><subject>Energy</subject><subject>Exact sciences and technology</subject><subject>Fuels</subject><subject>Gasification</subject><subject>Hydrogen</subject><subject>Hydrogen-rich gas</subject><subject>Particle size</subject><subject>Reactors</subject><subject>Steam gasification</subject><issn>0360-3199</issn><issn>1879-3487</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2009</creationdate><recordtype>article</recordtype><recordid>eNqFkU1uFDEQRi0EEkPgCsgblFUP_pu2nVWiKJBIkdjA2nK7y0mNutuD3RNlOARnyFk4GW5NQGLFwrL0-VWV6pmQ95ytOePtx-0at_eHHiZYC8ZMDdfMmBdkxY22jVRGvyQrJlvWSG7ta_KmlC1jXDNlV-Tn9aHP6Q6mJmO4p3e-0JjTSIOf_XCYMdAygx-XB4xYU0wTTfHXU4dp9KVQnKinER-hp109GXyYUz6jN1Mc9jAFqDTd-VxbDUAL_qjB9G-7HeSY8ugr_Ja8in4o8O75PiHfPl19vbxubr98vrm8uG2CMnxuhG2DjJ3gMQJwLqK2vBNKarVRm6AE6E4EY7Tp7IYLzfSmN23bg5G9kbJV8oScHvvucvq-hzK7EUuAYfATpH1xtoptreSiku2RDDmVkiG6XcbR54PjzC3-3db98e8W_0te_dfCD88jfAl-iLnuh-VvteBc1V9glTs_clD3fUDIrgRcxPWYIcyuT_i_Ub8Bas6hoQ</recordid><startdate>20090201</startdate><enddate>20090201</enddate><creator>Luo, Siyi</creator><creator>Xiao, Bo</creator><creator>Guo, Xianjun</creator><creator>Hu, Zhiquan</creator><creator>Liu, Shiming</creator><creator>He, Maoyun</creator><general>Elsevier Ltd</general><general>Elsevier</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7SP</scope><scope>8FD</scope><scope>L7M</scope></search><sort><creationdate>20090201</creationdate><title>Hydrogen-rich gas from catalytic steam gasification of biomass in a fixed bed reactor: Influence of particle size on gasification performance</title><author>Luo, Siyi ; Xiao, Bo ; Guo, Xianjun ; Hu, Zhiquan ; Liu, Shiming ; He, Maoyun</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c481t-296c3fb21ffee112f791b24374545c42e7b2c8878b95127075d866de83d833643</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2009</creationdate><topic>Alternative fuels. Production and utilization</topic><topic>Applied sciences</topic><topic>Biomass</topic><topic>Carbon</topic><topic>Carbon monoxide</topic><topic>Catalysis</topic><topic>Catalysts</topic><topic>Energy</topic><topic>Exact sciences and technology</topic><topic>Fuels</topic><topic>Gasification</topic><topic>Hydrogen</topic><topic>Hydrogen-rich gas</topic><topic>Particle size</topic><topic>Reactors</topic><topic>Steam gasification</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Luo, Siyi</creatorcontrib><creatorcontrib>Xiao, Bo</creatorcontrib><creatorcontrib>Guo, Xianjun</creatorcontrib><creatorcontrib>Hu, Zhiquan</creatorcontrib><creatorcontrib>Liu, Shiming</creatorcontrib><creatorcontrib>He, Maoyun</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Electronics & Communications Abstracts</collection><collection>Technology Research Database</collection><collection>Advanced Technologies Database with Aerospace</collection><jtitle>International journal of hydrogen energy</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Luo, Siyi</au><au>Xiao, Bo</au><au>Guo, Xianjun</au><au>Hu, Zhiquan</au><au>Liu, Shiming</au><au>He, Maoyun</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Hydrogen-rich gas from catalytic steam gasification of biomass in a fixed bed reactor: Influence of particle size on gasification performance</atitle><jtitle>International journal of hydrogen energy</jtitle><date>2009-02-01</date><risdate>2009</risdate><volume>34</volume><issue>3</issue><spage>1260</spage><epage>1264</epage><pages>1260-1264</pages><issn>0360-3199</issn><eissn>1879-3487</eissn><coden>IJHEDX</coden><abstract>The catalytic steam gasification of biomass was carried out in a lab-scale fixed bed reactor in order to evaluate the effects of particle size at different bed temperatures on the gasification performance. The bed temperature was varied from 600 to 900
°C and the biomass was separated into five different size fractions (below 0.075
mm, 0.075–0.15
mm, 0.15–0.3
mm, 0.3–0.6
mm and 0.6–1.2
mm). The results show that with decreasing particle size, the dry gas yield, carbon conversion efficiency and H
2 yield increased, and the content of char and tar decreased. And the differences due to particle sizes in gasification performance practically disappear as the higher temperature bound is approached. Hydrogen and carbon monoxide contents in the produced gas increase with decreasing particle size at 900
°C, reaching to 51.2% and 22.4%, respectively.</abstract><cop>Kidlington</cop><pub>Elsevier Ltd</pub><doi>10.1016/j.ijhydene.2008.10.088</doi><tpages>5</tpages></addata></record> |
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| ispartof | International journal of hydrogen energy, 2009-02, Vol.34 (3), p.1260-1264 |
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| language | eng |
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| source | Elsevier ScienceDirect Journals Complete - AutoHoldings |
| subjects | Alternative fuels. Production and utilization Applied sciences Biomass Carbon Carbon monoxide Catalysis Catalysts Energy Exact sciences and technology Fuels Gasification Hydrogen Hydrogen-rich gas Particle size Reactors Steam gasification |
| title | Hydrogen-rich gas from catalytic steam gasification of biomass in a fixed bed reactor: Influence of particle size on gasification performance |
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