Syngas production by autothermal reforming of methane on supported platinum catalysts
The performance of supported platinum catalysts on the autothermal reforming of methane was evaluated. The effect of the calcination temperature of the CeZrO 2 support and of the reaction conditions (reaction temperature, presence of CO 2 in the feedstock, and H 2O/CH 4 molar ratio) was studied. The...
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| Veröffentlicht in: | Applied catalysis. A, General General, 2008, Vol.334 (1), p.259-267 |
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| creator | Ruiz, Juan A.C. Passos, Fabio B. Bueno, José M.C. Souza-Aguiar, Eduardo F. Mattos, Lisiane V. Noronha, Fabio B. |
| description | The performance of supported platinum catalysts on the autothermal reforming of methane was evaluated. The effect of the calcination temperature of the CeZrO
2 support and of the reaction conditions (reaction temperature, presence of CO
2 in the feedstock, and H
2O/CH
4 molar ratio) was studied. The catalysts were characterized by BET, XRD, and OSC analyses and the reaction mechanism was determined by TPSR experiments. The TPSR analyses indicate that autothermal reforming of methane proceeds through a two-step mechanism (indirect mechanism) over all catalysts studied. The Pt/Ce
0.75Zr
0.25O
2 catalyst presented the best stability, which depends not only on the amount of oxygen vacancies of the support but also on the metal particle size. The higher reducibility and oxygen storage/release capacity of Pt/Ce
0.75Zr
0.25O
2 catalyst promote the mechanism of continuous removal of carbonaceous deposits from the active sites, which takes place at the metal-support interfacial perimeter. The water also participates in this mechanism, favouring the carbon removal of metal particle. Furthermore, the reaction conditions influenced significantly the behaviour of Pt/Ce
0.75Zr
0.25O
2 catalysts. The increase of H
2O/CH
4 molar ratio had a beneficial effect on the methane conversion and on the H
2/CO molar ratio. However, the increase of the reaction temperature had an opposite effect. Both the methane conversion and H
2/CO molar ratio decreased with the increasing of reaction temperature. Moreover, the addition of CO
2 to feedstock increased the initial methane conversion, but decreased the stability of the catalyst.
The performance of supported Pt catalysts on the autothermal reforming of methane was evaluated under different reaction conditions. The TPSR analyses indicate that autothermal reforming of methane proceeds through a two-step mechanism over all catalysts studied. The Pt/Ce
0.75Zr
0.25O
2 catalyst presented the best stability, which depends not only on the amount of oxygen vacancies of the support but also on the metal particle size.
▪ |
| doi_str_mv | 10.1016/j.apcata.2007.10.011 |
| format | Article |
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2 support and of the reaction conditions (reaction temperature, presence of CO
2 in the feedstock, and H
2O/CH
4 molar ratio) was studied. The catalysts were characterized by BET, XRD, and OSC analyses and the reaction mechanism was determined by TPSR experiments. The TPSR analyses indicate that autothermal reforming of methane proceeds through a two-step mechanism (indirect mechanism) over all catalysts studied. The Pt/Ce
0.75Zr
0.25O
2 catalyst presented the best stability, which depends not only on the amount of oxygen vacancies of the support but also on the metal particle size. The higher reducibility and oxygen storage/release capacity of Pt/Ce
0.75Zr
0.25O
2 catalyst promote the mechanism of continuous removal of carbonaceous deposits from the active sites, which takes place at the metal-support interfacial perimeter. The water also participates in this mechanism, favouring the carbon removal of metal particle. Furthermore, the reaction conditions influenced significantly the behaviour of Pt/Ce
0.75Zr
0.25O
2 catalysts. The increase of H
2O/CH
4 molar ratio had a beneficial effect on the methane conversion and on the H
2/CO molar ratio. However, the increase of the reaction temperature had an opposite effect. Both the methane conversion and H
2/CO molar ratio decreased with the increasing of reaction temperature. Moreover, the addition of CO
2 to feedstock increased the initial methane conversion, but decreased the stability of the catalyst.
The performance of supported Pt catalysts on the autothermal reforming of methane was evaluated under different reaction conditions. The TPSR analyses indicate that autothermal reforming of methane proceeds through a two-step mechanism over all catalysts studied. The Pt/Ce
0.75Zr
0.25O
2 catalyst presented the best stability, which depends not only on the amount of oxygen vacancies of the support but also on the metal particle size.
▪</description><identifier>ISSN: 0926-860X</identifier><identifier>EISSN: 1873-3875</identifier><identifier>DOI: 10.1016/j.apcata.2007.10.011</identifier><language>eng</language><publisher>Amsterdam: Elsevier B.V</publisher><subject>Autothermal reforming (ATR) ; Catalysis ; Chemistry ; Exact sciences and technology ; General and physical chemistry ; GTL technology ; Natural gas ; Pt/CeZrO 2 catalysts ; Synthesis gas ; Theory of reactions, general kinetics. Catalysis. Nomenclature, chemical documentation, computer chemistry</subject><ispartof>Applied catalysis. A, General, 2008, Vol.334 (1), p.259-267</ispartof><rights>2007 Elsevier B.V.</rights><rights>2008 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c404t-ccdf85206c10217c7036b8e7aa83ba5915a278f78fefc037c3c8a902bc1668933</citedby></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://dx.doi.org/10.1016/j.apcata.2007.10.011$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,780,784,3550,4024,27923,27924,27925,45995</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=19971848$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Ruiz, Juan A.C.</creatorcontrib><creatorcontrib>Passos, Fabio B.</creatorcontrib><creatorcontrib>Bueno, José M.C.</creatorcontrib><creatorcontrib>Souza-Aguiar, Eduardo F.</creatorcontrib><creatorcontrib>Mattos, Lisiane V.</creatorcontrib><creatorcontrib>Noronha, Fabio B.</creatorcontrib><title>Syngas production by autothermal reforming of methane on supported platinum catalysts</title><title>Applied catalysis. A, General</title><description>The performance of supported platinum catalysts on the autothermal reforming of methane was evaluated. The effect of the calcination temperature of the CeZrO
2 support and of the reaction conditions (reaction temperature, presence of CO
2 in the feedstock, and H
2O/CH
4 molar ratio) was studied. The catalysts were characterized by BET, XRD, and OSC analyses and the reaction mechanism was determined by TPSR experiments. The TPSR analyses indicate that autothermal reforming of methane proceeds through a two-step mechanism (indirect mechanism) over all catalysts studied. The Pt/Ce
0.75Zr
0.25O
2 catalyst presented the best stability, which depends not only on the amount of oxygen vacancies of the support but also on the metal particle size. The higher reducibility and oxygen storage/release capacity of Pt/Ce
0.75Zr
0.25O
2 catalyst promote the mechanism of continuous removal of carbonaceous deposits from the active sites, which takes place at the metal-support interfacial perimeter. The water also participates in this mechanism, favouring the carbon removal of metal particle. Furthermore, the reaction conditions influenced significantly the behaviour of Pt/Ce
0.75Zr
0.25O
2 catalysts. The increase of H
2O/CH
4 molar ratio had a beneficial effect on the methane conversion and on the H
2/CO molar ratio. However, the increase of the reaction temperature had an opposite effect. Both the methane conversion and H
2/CO molar ratio decreased with the increasing of reaction temperature. Moreover, the addition of CO
2 to feedstock increased the initial methane conversion, but decreased the stability of the catalyst.
The performance of supported Pt catalysts on the autothermal reforming of methane was evaluated under different reaction conditions. The TPSR analyses indicate that autothermal reforming of methane proceeds through a two-step mechanism over all catalysts studied. The Pt/Ce
0.75Zr
0.25O
2 catalyst presented the best stability, which depends not only on the amount of oxygen vacancies of the support but also on the metal particle size.
▪</description><subject>Autothermal reforming (ATR)</subject><subject>Catalysis</subject><subject>Chemistry</subject><subject>Exact sciences and technology</subject><subject>General and physical chemistry</subject><subject>GTL technology</subject><subject>Natural gas</subject><subject>Pt/CeZrO 2 catalysts</subject><subject>Synthesis gas</subject><subject>Theory of reactions, general kinetics. Catalysis. Nomenclature, chemical documentation, computer chemistry</subject><issn>0926-860X</issn><issn>1873-3875</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2008</creationdate><recordtype>article</recordtype><recordid>eNp9kEFr3DAQhUVoINsk_yAHXdqbnZFlW_KlUELTFhZyaBdyE7NjOdFiW64kF_bfR8sGeisMDAzfzLz3GLsTUAoQ7f2hxIUwYVkBqDwqQYgLthFayUJq1XxgG-iqttAtPF-xjzEeAKCqu2bDdr-O8wtGvgTfr5Scn_n-yHFNPr3aMOHIgx18mNz8wv3AJ5tecbY8Y3FdFh-S7fkyYnLzOvGThvEYU7xhlwOO0d6-92u2e_z2--FHsX36_vPh67agGupUEPWDbipoSUAlFCmQ7V5bhajlHptONFgpPeSyA4FUJEljB9WeRNvqTspr9vl8N8v_s9qYzOQi2XHMGv0ajRSdqBuoM1ifQQo-xmzJLMFNGI5GgDllaA7mnKE5ZXia5gzz2qf3-xgJxyHgTC7-2-06JXStM_flzNls9q-zwURydibbu2Apmd67_z96A6meirs</recordid><startdate>2008</startdate><enddate>2008</enddate><creator>Ruiz, Juan A.C.</creator><creator>Passos, Fabio B.</creator><creator>Bueno, José M.C.</creator><creator>Souza-Aguiar, Eduardo F.</creator><creator>Mattos, Lisiane V.</creator><creator>Noronha, Fabio B.</creator><general>Elsevier B.V</general><general>Elsevier</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7SR</scope><scope>7U5</scope><scope>8BQ</scope><scope>8FD</scope><scope>JG9</scope><scope>L7M</scope></search><sort><creationdate>2008</creationdate><title>Syngas production by autothermal reforming of methane on supported platinum catalysts</title><author>Ruiz, Juan A.C. ; Passos, Fabio B. ; Bueno, José M.C. ; Souza-Aguiar, Eduardo F. ; Mattos, Lisiane V. ; Noronha, Fabio B.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c404t-ccdf85206c10217c7036b8e7aa83ba5915a278f78fefc037c3c8a902bc1668933</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2008</creationdate><topic>Autothermal reforming (ATR)</topic><topic>Catalysis</topic><topic>Chemistry</topic><topic>Exact sciences and technology</topic><topic>General and physical chemistry</topic><topic>GTL technology</topic><topic>Natural gas</topic><topic>Pt/CeZrO 2 catalysts</topic><topic>Synthesis gas</topic><topic>Theory of reactions, general kinetics. Catalysis. Nomenclature, chemical documentation, computer chemistry</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Ruiz, Juan A.C.</creatorcontrib><creatorcontrib>Passos, Fabio B.</creatorcontrib><creatorcontrib>Bueno, José M.C.</creatorcontrib><creatorcontrib>Souza-Aguiar, Eduardo F.</creatorcontrib><creatorcontrib>Mattos, Lisiane V.</creatorcontrib><creatorcontrib>Noronha, Fabio B.</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Engineered Materials Abstracts</collection><collection>Solid State and Superconductivity Abstracts</collection><collection>METADEX</collection><collection>Technology Research Database</collection><collection>Materials Research Database</collection><collection>Advanced Technologies Database with Aerospace</collection><jtitle>Applied catalysis. A, General</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Ruiz, Juan A.C.</au><au>Passos, Fabio B.</au><au>Bueno, José M.C.</au><au>Souza-Aguiar, Eduardo F.</au><au>Mattos, Lisiane V.</au><au>Noronha, Fabio B.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Syngas production by autothermal reforming of methane on supported platinum catalysts</atitle><jtitle>Applied catalysis. A, General</jtitle><date>2008</date><risdate>2008</risdate><volume>334</volume><issue>1</issue><spage>259</spage><epage>267</epage><pages>259-267</pages><issn>0926-860X</issn><eissn>1873-3875</eissn><abstract>The performance of supported platinum catalysts on the autothermal reforming of methane was evaluated. The effect of the calcination temperature of the CeZrO
2 support and of the reaction conditions (reaction temperature, presence of CO
2 in the feedstock, and H
2O/CH
4 molar ratio) was studied. The catalysts were characterized by BET, XRD, and OSC analyses and the reaction mechanism was determined by TPSR experiments. The TPSR analyses indicate that autothermal reforming of methane proceeds through a two-step mechanism (indirect mechanism) over all catalysts studied. The Pt/Ce
0.75Zr
0.25O
2 catalyst presented the best stability, which depends not only on the amount of oxygen vacancies of the support but also on the metal particle size. The higher reducibility and oxygen storage/release capacity of Pt/Ce
0.75Zr
0.25O
2 catalyst promote the mechanism of continuous removal of carbonaceous deposits from the active sites, which takes place at the metal-support interfacial perimeter. The water also participates in this mechanism, favouring the carbon removal of metal particle. Furthermore, the reaction conditions influenced significantly the behaviour of Pt/Ce
0.75Zr
0.25O
2 catalysts. The increase of H
2O/CH
4 molar ratio had a beneficial effect on the methane conversion and on the H
2/CO molar ratio. However, the increase of the reaction temperature had an opposite effect. Both the methane conversion and H
2/CO molar ratio decreased with the increasing of reaction temperature. Moreover, the addition of CO
2 to feedstock increased the initial methane conversion, but decreased the stability of the catalyst.
The performance of supported Pt catalysts on the autothermal reforming of methane was evaluated under different reaction conditions. The TPSR analyses indicate that autothermal reforming of methane proceeds through a two-step mechanism over all catalysts studied. The Pt/Ce
0.75Zr
0.25O
2 catalyst presented the best stability, which depends not only on the amount of oxygen vacancies of the support but also on the metal particle size.
▪</abstract><cop>Amsterdam</cop><pub>Elsevier B.V</pub><doi>10.1016/j.apcata.2007.10.011</doi><tpages>9</tpages></addata></record> |
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| source | ScienceDirect Journals (5 years ago - present) |
| subjects | Autothermal reforming (ATR) Catalysis Chemistry Exact sciences and technology General and physical chemistry GTL technology Natural gas Pt/CeZrO 2 catalysts Synthesis gas Theory of reactions, general kinetics. Catalysis. Nomenclature, chemical documentation, computer chemistry |
| title | Syngas production by autothermal reforming of methane on supported platinum catalysts |
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