FUEL REFORMER
PURPOSE:To enable high efficiency of reforming reaction and contrive a small- sized and compact apparatus, by providing the first gas flow passage filled with a reforming catalyst adjacent to the second gas flow passage filled with a CO conversion catalyst. CONSTITUTION:A raw material for reforming...
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| creator | AMANO YOSHIAKI OBATA ISAO HANZAWA AKIO |
| description | PURPOSE:To enable high efficiency of reforming reaction and contrive a small- sized and compact apparatus, by providing the first gas flow passage filled with a reforming catalyst adjacent to the second gas flow passage filled with a CO conversion catalyst. CONSTITUTION:A raw material for reforming is passed through a raw material inlet 7 and fed to a reforming catalyst layer 14. The raw material fed to the reforming catalyst layer 14 starts reforming reaction and is slowly reformed into a hydrogenenriched gas. Since the reforming reaction is endothermic reaction, heat absorption is carried out from the resultant reformed gas flowing through a CO conversion catalyst layer 15 and a combustion gas flowing through a heating layer 16. The reformed gas after completing the reforming reaction is fed to the CO conversion catalyst layer 15 to slowly carry out CO conversion reaction. The obtained gas is then led out of a reformed gas outlet 8. On the other hand, a fuel is passed through a fuel inlet 9, fed to a fuel device 12 and burned with air, passed through an air inlet 10 and fed thereto. |
| format | Patent |
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CONSTITUTION:A raw material for reforming is passed through a raw material inlet 7 and fed to a reforming catalyst layer 14. The raw material fed to the reforming catalyst layer 14 starts reforming reaction and is slowly reformed into a hydrogenenriched gas. Since the reforming reaction is endothermic reaction, heat absorption is carried out from the resultant reformed gas flowing through a CO conversion catalyst layer 15 and a combustion gas flowing through a heating layer 16. The reformed gas after completing the reforming reaction is fed to the CO conversion catalyst layer 15 to slowly carry out CO conversion reaction. The obtained gas is then led out of a reformed gas outlet 8. On the other hand, a fuel is passed through a fuel inlet 9, fed to a fuel device 12 and burned with air, passed through an air inlet 10 and fed thereto.</description><language>eng</language><subject>CHEMISTRY ; COMPOUNDS THEREOF ; FUELS ; INORGANIC CHEMISTRY ; LUBRICANTS ; METALLURGY ; NON-METALLIC ELEMENTS ; PEAT ; PETROLEUM, GAS OR COKE INDUSTRIES ; PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLEGASES CONTAINING CARBON MONOXIDE ; TECHNICAL GASES CONTAINING CARBON MONOXIDE</subject><creationdate>1989</creationdate><oa>free_for_read</oa><woscitedreferencessubscribed>false</woscitedreferencessubscribed></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=19890721&DB=EPODOC&CC=JP&NR=H01183401A$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,308,780,885,25564,76547</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=19890721&DB=EPODOC&CC=JP&NR=H01183401A$$EView_record_in_European_Patent_Office$$FView_record_in_$$GEuropean_Patent_Office$$Hfree_for_read</linktorsrc></links><search><creatorcontrib>AMANO YOSHIAKI</creatorcontrib><creatorcontrib>OBATA ISAO</creatorcontrib><creatorcontrib>HANZAWA AKIO</creatorcontrib><title>FUEL REFORMER</title><description>PURPOSE:To enable high efficiency of reforming reaction and contrive a small- sized and compact apparatus, by providing the first gas flow passage filled with a reforming catalyst adjacent to the second gas flow passage filled with a CO conversion catalyst. CONSTITUTION:A raw material for reforming is passed through a raw material inlet 7 and fed to a reforming catalyst layer 14. The raw material fed to the reforming catalyst layer 14 starts reforming reaction and is slowly reformed into a hydrogenenriched gas. Since the reforming reaction is endothermic reaction, heat absorption is carried out from the resultant reformed gas flowing through a CO conversion catalyst layer 15 and a combustion gas flowing through a heating layer 16. The reformed gas after completing the reforming reaction is fed to the CO conversion catalyst layer 15 to slowly carry out CO conversion reaction. The obtained gas is then led out of a reformed gas outlet 8. On the other hand, a fuel is passed through a fuel inlet 9, fed to a fuel device 12 and burned with air, passed through an air inlet 10 and fed thereto.</description><subject>CHEMISTRY</subject><subject>COMPOUNDS THEREOF</subject><subject>FUELS</subject><subject>INORGANIC CHEMISTRY</subject><subject>LUBRICANTS</subject><subject>METALLURGY</subject><subject>NON-METALLIC ELEMENTS</subject><subject>PEAT</subject><subject>PETROLEUM, GAS OR COKE INDUSTRIES</subject><subject>PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLEGASES CONTAINING CARBON MONOXIDE</subject><subject>TECHNICAL GASES CONTAINING CARBON MONOXIDE</subject><fulltext>true</fulltext><rsrctype>patent</rsrctype><creationdate>1989</creationdate><recordtype>patent</recordtype><sourceid>EVB</sourceid><recordid>eNrjZOB1C3X1UQhydfMP8nUN4mFgTUvMKU7lhdLcDIpuriHOHrqpBfnxqcUFicmpeakl8V4BHgaGhhbGJgaGjsbEqAEArlscyA</recordid><startdate>19890721</startdate><enddate>19890721</enddate><creator>AMANO YOSHIAKI</creator><creator>OBATA ISAO</creator><creator>HANZAWA AKIO</creator><scope>EVB</scope></search><sort><creationdate>19890721</creationdate><title>FUEL REFORMER</title><author>AMANO YOSHIAKI ; OBATA ISAO ; HANZAWA AKIO</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-epo_espacenet_JPH01183401A3</frbrgroupid><rsrctype>patents</rsrctype><prefilter>patents</prefilter><language>eng</language><creationdate>1989</creationdate><topic>CHEMISTRY</topic><topic>COMPOUNDS THEREOF</topic><topic>FUELS</topic><topic>INORGANIC CHEMISTRY</topic><topic>LUBRICANTS</topic><topic>METALLURGY</topic><topic>NON-METALLIC ELEMENTS</topic><topic>PEAT</topic><topic>PETROLEUM, GAS OR COKE INDUSTRIES</topic><topic>PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLEGASES CONTAINING CARBON MONOXIDE</topic><topic>TECHNICAL GASES CONTAINING CARBON MONOXIDE</topic><toplevel>online_resources</toplevel><creatorcontrib>AMANO YOSHIAKI</creatorcontrib><creatorcontrib>OBATA ISAO</creatorcontrib><creatorcontrib>HANZAWA AKIO</creatorcontrib><collection>esp@cenet</collection></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext_linktorsrc</fulltext></delivery><addata><au>AMANO YOSHIAKI</au><au>OBATA ISAO</au><au>HANZAWA AKIO</au><format>patent</format><genre>patent</genre><ristype>GEN</ristype><title>FUEL REFORMER</title><date>1989-07-21</date><risdate>1989</risdate><abstract>PURPOSE:To enable high efficiency of reforming reaction and contrive a small- sized and compact apparatus, by providing the first gas flow passage filled with a reforming catalyst adjacent to the second gas flow passage filled with a CO conversion catalyst. CONSTITUTION:A raw material for reforming is passed through a raw material inlet 7 and fed to a reforming catalyst layer 14. The raw material fed to the reforming catalyst layer 14 starts reforming reaction and is slowly reformed into a hydrogenenriched gas. Since the reforming reaction is endothermic reaction, heat absorption is carried out from the resultant reformed gas flowing through a CO conversion catalyst layer 15 and a combustion gas flowing through a heating layer 16. The reformed gas after completing the reforming reaction is fed to the CO conversion catalyst layer 15 to slowly carry out CO conversion reaction. The obtained gas is then led out of a reformed gas outlet 8. On the other hand, a fuel is passed through a fuel inlet 9, fed to a fuel device 12 and burned with air, passed through an air inlet 10 and fed thereto.</abstract><oa>free_for_read</oa></addata></record> |
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| language | eng |
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| subjects | CHEMISTRY COMPOUNDS THEREOF FUELS INORGANIC CHEMISTRY LUBRICANTS METALLURGY NON-METALLIC ELEMENTS PEAT PETROLEUM, GAS OR COKE INDUSTRIES PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLEGASES CONTAINING CARBON MONOXIDE TECHNICAL GASES CONTAINING CARBON MONOXIDE |
| title | FUEL REFORMER |
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