Characteristics of methane reforming using gliding arc reactor
A gliding arc reformer was proposed to produce hydrogen-rich gas. The reformer has two reactors including a plasma reactor and a catalyst reactor. The reforming characteristics for each of the following variables were studied: O 2/C ratio, total gas flow rate, catalyst reactor temperature, reformer...
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| Veröffentlicht in: | Energy (Oxford) 2009-02, Vol.34 (2), p.172-177 |
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| creator | Yang, Yoon-Cheol Lee, Bong-Ju Chun, Young-Nam |
| description | A gliding arc reformer was proposed to produce hydrogen-rich gas. The reformer has two reactors including a plasma reactor and a catalyst reactor.
The reforming characteristics for each of the following variables were studied: O
2/C ratio, total gas flow rate, catalyst reactor temperature, reformer energy density, catalytic effect and CO
2 input concentration to simulate biogas.
Optimum conditions for producing H
2 from methane were also suggested. The conditions consisted of an O
2/C ratio of 0.64, a total gas flow rate of 14.2
L/min, a catalyst reactor temperature of 672
°C, a reformer energy density of 1.1
kJ/L and a steam flow ratio of 0.8. The maximum H
2 concentration of 41.1% was obtained under the optimum conditions. Also, methane conversion rate, H
2 yield and reformer thermal efficiencies were 67%, 54% and 35%, respectively. |
| doi_str_mv | 10.1016/j.energy.2008.11.006 |
| format | Article |
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The reforming characteristics for each of the following variables were studied: O
2/C ratio, total gas flow rate, catalyst reactor temperature, reformer energy density, catalytic effect and CO
2 input concentration to simulate biogas.
Optimum conditions for producing H
2 from methane were also suggested. The conditions consisted of an O
2/C ratio of 0.64, a total gas flow rate of 14.2
L/min, a catalyst reactor temperature of 672
°C, a reformer energy density of 1.1
kJ/L and a steam flow ratio of 0.8. The maximum H
2 concentration of 41.1% was obtained under the optimum conditions. Also, methane conversion rate, H
2 yield and reformer thermal efficiencies were 67%, 54% and 35%, respectively.</description><identifier>ISSN: 0360-5442</identifier><identifier>DOI: 10.1016/j.energy.2008.11.006</identifier><identifier>CODEN: ENEYDS</identifier><language>eng</language><publisher>Kidlington: Elsevier Ltd</publisher><subject>Alternative fuels. Production and utilization ; Applied sciences ; Biogas reforming ; Biomass ; Energy ; Exact sciences and technology ; Fuels ; Gliding arc plasma ; Hydrogen ; Hydrogen production ; Methane reforming ; Natural energy ; Partial oxidation</subject><ispartof>Energy (Oxford), 2009-02, Vol.34 (2), p.172-177</ispartof><rights>2008</rights><rights>2009 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c433t-7c6d055c615a657d31356d9641a9e6dce421939eb23f60caec3b2716c4c5ca013</citedby><cites>FETCH-LOGICAL-c433t-7c6d055c615a657d31356d9641a9e6dce421939eb23f60caec3b2716c4c5ca013</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://dx.doi.org/10.1016/j.energy.2008.11.006$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,780,784,3548,27922,27923,45993</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=21231309$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Yang, Yoon-Cheol</creatorcontrib><creatorcontrib>Lee, Bong-Ju</creatorcontrib><creatorcontrib>Chun, Young-Nam</creatorcontrib><title>Characteristics of methane reforming using gliding arc reactor</title><title>Energy (Oxford)</title><description>A gliding arc reformer was proposed to produce hydrogen-rich gas. The reformer has two reactors including a plasma reactor and a catalyst reactor.
The reforming characteristics for each of the following variables were studied: O
2/C ratio, total gas flow rate, catalyst reactor temperature, reformer energy density, catalytic effect and CO
2 input concentration to simulate biogas.
Optimum conditions for producing H
2 from methane were also suggested. The conditions consisted of an O
2/C ratio of 0.64, a total gas flow rate of 14.2
L/min, a catalyst reactor temperature of 672
°C, a reformer energy density of 1.1
kJ/L and a steam flow ratio of 0.8. The maximum H
2 concentration of 41.1% was obtained under the optimum conditions. Also, methane conversion rate, H
2 yield and reformer thermal efficiencies were 67%, 54% and 35%, respectively.</description><subject>Alternative fuels. Production and utilization</subject><subject>Applied sciences</subject><subject>Biogas reforming</subject><subject>Biomass</subject><subject>Energy</subject><subject>Exact sciences and technology</subject><subject>Fuels</subject><subject>Gliding arc plasma</subject><subject>Hydrogen</subject><subject>Hydrogen production</subject><subject>Methane reforming</subject><subject>Natural energy</subject><subject>Partial oxidation</subject><issn>0360-5442</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2009</creationdate><recordtype>article</recordtype><recordid>eNp9UMtOwzAQ9AEkSuEPOOQCt4bdOHabSyVU8ZIqcYGz5W42ras8ip0i9e9xlIojl53DzuzOjBB3CCkC6sd9yi377SnNABYpYgqgL8QEpIaZyvPsSlyHsAcAtSiKiViudtZb6tm70DsKSVclDfc723Liuep849ptcgzD3NauHNB6irso6vyNuKxsHfj2jFPx9fL8uXqbrT9e31dP6xnlUvazOekSlCKNymo1LyVKpctC52gL1iVxnmEhC95kstJAlklusjlqykmRBZRT8TDePfju-8ihN40LxHUdfXbHYKRERA15JOYjkXwXQkxgDt411p8MghkKMnszFmSGggyiiQVF2f35vg1k68rbllz402aYRctQRN5y5HEM--PYm0COW-LSeabelJ37_9EvMl5_hA</recordid><startdate>20090201</startdate><enddate>20090201</enddate><creator>Yang, Yoon-Cheol</creator><creator>Lee, Bong-Ju</creator><creator>Chun, Young-Nam</creator><general>Elsevier Ltd</general><general>Elsevier</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7SP</scope><scope>7TB</scope><scope>8FD</scope><scope>F28</scope><scope>FR3</scope><scope>KR7</scope><scope>L7M</scope></search><sort><creationdate>20090201</creationdate><title>Characteristics of methane reforming using gliding arc reactor</title><author>Yang, Yoon-Cheol ; Lee, Bong-Ju ; Chun, Young-Nam</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c433t-7c6d055c615a657d31356d9641a9e6dce421939eb23f60caec3b2716c4c5ca013</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>Biogas reforming</topic><topic>Biomass</topic><topic>Energy</topic><topic>Exact sciences and technology</topic><topic>Fuels</topic><topic>Gliding arc plasma</topic><topic>Hydrogen</topic><topic>Hydrogen production</topic><topic>Methane reforming</topic><topic>Natural energy</topic><topic>Partial oxidation</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Yang, Yoon-Cheol</creatorcontrib><creatorcontrib>Lee, Bong-Ju</creatorcontrib><creatorcontrib>Chun, Young-Nam</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Electronics & Communications Abstracts</collection><collection>Mechanical & Transportation Engineering Abstracts</collection><collection>Technology Research Database</collection><collection>ANTE: Abstracts in New Technology & Engineering</collection><collection>Engineering Research Database</collection><collection>Civil Engineering Abstracts</collection><collection>Advanced Technologies Database with Aerospace</collection><jtitle>Energy (Oxford)</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Yang, Yoon-Cheol</au><au>Lee, Bong-Ju</au><au>Chun, Young-Nam</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Characteristics of methane reforming using gliding arc reactor</atitle><jtitle>Energy (Oxford)</jtitle><date>2009-02-01</date><risdate>2009</risdate><volume>34</volume><issue>2</issue><spage>172</spage><epage>177</epage><pages>172-177</pages><issn>0360-5442</issn><coden>ENEYDS</coden><abstract>A gliding arc reformer was proposed to produce hydrogen-rich gas. The reformer has two reactors including a plasma reactor and a catalyst reactor.
The reforming characteristics for each of the following variables were studied: O
2/C ratio, total gas flow rate, catalyst reactor temperature, reformer energy density, catalytic effect and CO
2 input concentration to simulate biogas.
Optimum conditions for producing H
2 from methane were also suggested. The conditions consisted of an O
2/C ratio of 0.64, a total gas flow rate of 14.2
L/min, a catalyst reactor temperature of 672
°C, a reformer energy density of 1.1
kJ/L and a steam flow ratio of 0.8. The maximum H
2 concentration of 41.1% was obtained under the optimum conditions. Also, methane conversion rate, H
2 yield and reformer thermal efficiencies were 67%, 54% and 35%, respectively.</abstract><cop>Kidlington</cop><pub>Elsevier Ltd</pub><doi>10.1016/j.energy.2008.11.006</doi><tpages>6</tpages></addata></record> |
| fulltext | fulltext |
| identifier | ISSN: 0360-5442 |
| ispartof | Energy (Oxford), 2009-02, Vol.34 (2), p.172-177 |
| issn | 0360-5442 |
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| source | ScienceDirect Journals (5 years ago - present) |
| subjects | Alternative fuels. Production and utilization Applied sciences Biogas reforming Biomass Energy Exact sciences and technology Fuels Gliding arc plasma Hydrogen Hydrogen production Methane reforming Natural energy Partial oxidation |
| title | Characteristics of methane reforming using gliding arc reactor |
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