Hydrogen-rich gas from catalytic steam gasification of biomass in a fixed bed reactor: Influence of temperature and steam 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 temperatures and the ratio of steam to biomass ( S/ B) on the gasification performance. The bed temperature was varied from 600 to 900 and the S/ B from 0 to 2.80. The res...
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| Veröffentlicht in: | International journal of hydrogen energy 2009-03, Vol.34 (5), p.2191-2194 |
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| container_issue | 5 |
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| container_title | International journal of hydrogen energy |
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| creator | Luo, Siyi Xiao, Bo Hu, Zhiquan Liu, Shiming Guo, Xianjun 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 temperatures and the ratio of steam to biomass (
S/
B) on the gasification performance. The bed temperature was varied from 600 to 900 and the
S/
B from 0 to 2.80. The results show that higher temperature contributes to more hydrogen production.
The introduction of steam improves the dry gas yield and carbon conversion efficiency. But excessive steam will lower hydrogen content and degrade fuel gas quality. As
S/
B are 2.10, the hydrogen content reach the maximum, up to 52.7%. |
| doi_str_mv | 10.1016/j.ijhydene.2008.12.075 |
| format | Article |
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S/
B) on the gasification performance. The bed temperature was varied from 600 to 900 and the
S/
B from 0 to 2.80. The results show that higher temperature contributes to more hydrogen production.
The introduction of steam improves the dry gas yield and carbon conversion efficiency. But excessive steam will lower hydrogen content and degrade fuel gas quality. As
S/
B are 2.10, the hydrogen content reach the maximum, up to 52.7%.</description><identifier>ISSN: 0360-3199</identifier><identifier>EISSN: 1879-3487</identifier><identifier>DOI: 10.1016/j.ijhydene.2008.12.075</identifier><identifier>CODEN: IJHEDX</identifier><language>eng</language><publisher>Kidlington: Elsevier Ltd</publisher><subject>Alternative fuels. Production and utilization ; Applied sciences ; Biomass ; Carbon ; Catalysis ; Catalysts ; Conversion ; Drying ; Energy ; Exact sciences and technology ; Fuels ; Gasification ; Hydrogen ; Hydrogen-rich gas ; Reactors ; Steam gasification</subject><ispartof>International journal of hydrogen energy, 2009-03, Vol.34 (5), p.2191-2194</ispartof><rights>2009</rights><rights>2009 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c416t-c2218652b2e18e0dafad886c01722d145df4a6431ca5595d9a4eceb2f77a050e3</citedby></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://www.sciencedirect.com/science/article/pii/S0360319909000196$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,776,780,3537,27901,27902,65306</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=21299565$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Luo, Siyi</creatorcontrib><creatorcontrib>Xiao, Bo</creatorcontrib><creatorcontrib>Hu, Zhiquan</creatorcontrib><creatorcontrib>Liu, Shiming</creatorcontrib><creatorcontrib>Guo, Xianjun</creatorcontrib><creatorcontrib>He, Maoyun</creatorcontrib><title>Hydrogen-rich gas from catalytic steam gasification of biomass in a fixed bed reactor: Influence of temperature and steam 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 temperatures and the ratio of steam to biomass (
S/
B) on the gasification performance. The bed temperature was varied from 600 to 900 and the
S/
B from 0 to 2.80. The results show that higher temperature contributes to more hydrogen production.
The introduction of steam improves the dry gas yield and carbon conversion efficiency. But excessive steam will lower hydrogen content and degrade fuel gas quality. As
S/
B are 2.10, the hydrogen content reach the maximum, up to 52.7%.</description><subject>Alternative fuels. Production and utilization</subject><subject>Applied sciences</subject><subject>Biomass</subject><subject>Carbon</subject><subject>Catalysis</subject><subject>Catalysts</subject><subject>Conversion</subject><subject>Drying</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>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>eNqFkcFu1DAURSNEJYaWX0DeILFJ8HMSO2EFqlpaqRIbWFtv7OfWoyQebA9ifoQ139Ivw9EUJFYsLEt-596n61tVr4E3wEG-2zV-93C0tFAjOB8aEA1X_bNqA4Ma67Yb1PNqw1vJ6xbG8UX1MqUd56B4N26qnzdHG8M9LXX05oHdY2IuhpkZzDgdszcsZcJ5HXjny6sPCwuObX2YMSXmF4bM-R9k2bacSGhyiO_Z7eKmAy2GVjjTvKeI-RCJ4WIff508i9M_toVxIc5YVBfVmcMp0aun-7z6en315fKmvvv86fby411tOpC5NkLAIHuxFQQDcYsO7TBIU9IJYaHrretQdi0Y7PuxtyN2ZGgrnFLIe07tefX25LuP4duBUtazT4amCRcKh6RBKmgVQKcKKk-oiSGlSE7vo58xHjVwvRahd_pPEXotQoPQpYgifPO0A5PBycUS0Ke_agFiHHu5ch9OHJXA3z1FnYxfv9D6SCZrG_z_Vv0GsGamHw</recordid><startdate>20090301</startdate><enddate>20090301</enddate><creator>Luo, Siyi</creator><creator>Xiao, Bo</creator><creator>Hu, Zhiquan</creator><creator>Liu, Shiming</creator><creator>Guo, Xianjun</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>20090301</creationdate><title>Hydrogen-rich gas from catalytic steam gasification of biomass in a fixed bed reactor: Influence of temperature and steam on gasification performance</title><author>Luo, Siyi ; Xiao, Bo ; Hu, Zhiquan ; Liu, Shiming ; Guo, Xianjun ; He, Maoyun</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c416t-c2218652b2e18e0dafad886c01722d145df4a6431ca5595d9a4eceb2f77a050e3</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>Catalysis</topic><topic>Catalysts</topic><topic>Conversion</topic><topic>Drying</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>Reactors</topic><topic>Steam gasification</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Luo, Siyi</creatorcontrib><creatorcontrib>Xiao, Bo</creatorcontrib><creatorcontrib>Hu, Zhiquan</creatorcontrib><creatorcontrib>Liu, Shiming</creatorcontrib><creatorcontrib>Guo, Xianjun</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>Hu, Zhiquan</au><au>Liu, Shiming</au><au>Guo, Xianjun</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 temperature and steam on gasification performance</atitle><jtitle>International journal of hydrogen energy</jtitle><date>2009-03-01</date><risdate>2009</risdate><volume>34</volume><issue>5</issue><spage>2191</spage><epage>2194</epage><pages>2191-2194</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 temperatures and the ratio of steam to biomass (
S/
B) on the gasification performance. The bed temperature was varied from 600 to 900 and the
S/
B from 0 to 2.80. The results show that higher temperature contributes to more hydrogen production.
The introduction of steam improves the dry gas yield and carbon conversion efficiency. But excessive steam will lower hydrogen content and degrade fuel gas quality. As
S/
B are 2.10, the hydrogen content reach the maximum, up to 52.7%.</abstract><cop>Kidlington</cop><pub>Elsevier Ltd</pub><doi>10.1016/j.ijhydene.2008.12.075</doi><tpages>4</tpages></addata></record> |
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| identifier | ISSN: 0360-3199 |
| ispartof | International journal of hydrogen energy, 2009-03, Vol.34 (5), p.2191-2194 |
| issn | 0360-3199 1879-3487 |
| language | eng |
| recordid | cdi_proquest_miscellaneous_1671371147 |
| source | ScienceDirect Journals (5 years ago - present) |
| subjects | Alternative fuels. Production and utilization Applied sciences Biomass Carbon Catalysis Catalysts Conversion Drying Energy Exact sciences and technology Fuels Gasification Hydrogen Hydrogen-rich gas Reactors Steam gasification |
| title | Hydrogen-rich gas from catalytic steam gasification of biomass in a fixed bed reactor: Influence of temperature and steam on gasification performance |
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