Synthesis Gas Production by Catalytic Partial Oxidation of Propane on Mesoporous Nanocrystalline Ni/Al^sub 2^O^sub 3^ Catalysts
Propane partial oxidation to synthesis gas at various feed conditions was investigated over nickel catalysts supported on high surface area γ-alumina. The physicochemical characteristics of the calcined, reduced and spent samples were determined by TPR, BET, XRD, TPO and SEM analyses. The influences...
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description | Propane partial oxidation to synthesis gas at various feed conditions was investigated over nickel catalysts supported on high surface area γ-alumina. The physicochemical characteristics of the calcined, reduced and spent samples were determined by TPR, BET, XRD, TPO and SEM analyses. The influences of Ni content, reduction and reaction temperatures, gas hourly space velocity (GHSV) and feed ratio on the catalytic properties were investigated. The activity measurements revealed that the propane conversion had a direct relation with reaction temperature and nickel loading and increased with increasing of both these factors. However, there was an optimum value for nickel content and reaction temperature in which the H2 and CO yields were maximum. The 7.5 wt% Ni/Al2O3 exhibited high stability for 12 h without any decrease in activity. However, the selectivity declined gradually with reaction time due to carbon formation. The TPO analysis revealed that an increase in O2/C molar ratio from 0.25 to 0.75 caused a decrease in the amount of deposited carbon. Also, the amount of accumulated carbon slightly decreased with rising the reaction temperature. These results were confirmed by the SEM analysis and the filamentous carbon was observed on the catalyst surface. In addition, the increase in reduction temperature caused an increase in C3H8 conversion and H2/CO ratio. |
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The physicochemical characteristics of the calcined, reduced and spent samples were determined by TPR, BET, XRD, TPO and SEM analyses. The influences of Ni content, reduction and reaction temperatures, gas hourly space velocity (GHSV) and feed ratio on the catalytic properties were investigated. The activity measurements revealed that the propane conversion had a direct relation with reaction temperature and nickel loading and increased with increasing of both these factors. However, there was an optimum value for nickel content and reaction temperature in which the H2 and CO yields were maximum. The 7.5 wt% Ni/Al2O3 exhibited high stability for 12 h without any decrease in activity. However, the selectivity declined gradually with reaction time due to carbon formation. The TPO analysis revealed that an increase in O2/C molar ratio from 0.25 to 0.75 caused a decrease in the amount of deposited carbon. Also, the amount of accumulated carbon slightly decreased with rising the reaction temperature. These results were confirmed by the SEM analysis and the filamentous carbon was observed on the catalyst surface. In addition, the increase in reduction temperature caused an increase in C3H8 conversion and H2/CO ratio.</description><identifier>ISSN: 0926-860X</identifier><identifier>EISSN: 1873-3875</identifier><language>eng</language><publisher>Amsterdam: Elsevier Science SA</publisher><subject>Alumina ; Aluminum oxide ; Carbon ; Catalysts ; Catalytic converters ; Conversion ; Nickel ; Oxidation ; Propane ; Reaction time ; Reduction ; Synthesis gas ; Transitional aluminas</subject><ispartof>Applied catalysis. 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The physicochemical characteristics of the calcined, reduced and spent samples were determined by TPR, BET, XRD, TPO and SEM analyses. The influences of Ni content, reduction and reaction temperatures, gas hourly space velocity (GHSV) and feed ratio on the catalytic properties were investigated. The activity measurements revealed that the propane conversion had a direct relation with reaction temperature and nickel loading and increased with increasing of both these factors. However, there was an optimum value for nickel content and reaction temperature in which the H2 and CO yields were maximum. The 7.5 wt% Ni/Al2O3 exhibited high stability for 12 h without any decrease in activity. However, the selectivity declined gradually with reaction time due to carbon formation. The TPO analysis revealed that an increase in O2/C molar ratio from 0.25 to 0.75 caused a decrease in the amount of deposited carbon. Also, the amount of accumulated carbon slightly decreased with rising the reaction temperature. These results were confirmed by the SEM analysis and the filamentous carbon was observed on the catalyst surface. In addition, the increase in reduction temperature caused an increase in C3H8 conversion and H2/CO ratio.</description><subject>Alumina</subject><subject>Aluminum oxide</subject><subject>Carbon</subject><subject>Catalysts</subject><subject>Catalytic converters</subject><subject>Conversion</subject><subject>Nickel</subject><subject>Oxidation</subject><subject>Propane</subject><subject>Reaction time</subject><subject>Reduction</subject><subject>Synthesis gas</subject><subject>Transitional aluminas</subject><issn>0926-860X</issn><issn>1873-3875</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2017</creationdate><recordtype>article</recordtype><recordid>eNqNjM2KwjAUhYMoWEff4cKsizH1p12KzM9mVBgXrirXGjEScju5CUxXvvp0xAdwdTh83zkdkUzyRZZm-WLWFYks1DzN53LfFwPmq5RSTYtZIm7fjQsXzYbhAxm2nk6xCoYcHBtYYUDbBFPBFn0waGHza054x3T-l2t0Gtr2pZlq8hQZ1uio8g23U2taujbjpS05HkGVm3tm5eOZAw9F74yW9eiRL-L1_W23-kxrTz9RczhcKXrXooOSSskiVxOVPWf9AT-CUZY</recordid><startdate>20170105</startdate><enddate>20170105</enddate><creator>Peymani, Mohammad</creator><creator>Alavi, Seyed Mehdi</creator><creator>Rezaei, Mehran</creator><general>Elsevier Science SA</general><scope>7SR</scope><scope>7U5</scope><scope>8BQ</scope><scope>8FD</scope><scope>JG9</scope><scope>L7M</scope></search><sort><creationdate>20170105</creationdate><title>Synthesis Gas Production by Catalytic Partial Oxidation of Propane on Mesoporous Nanocrystalline Ni/Al^sub 2^O^sub 3^ Catalysts</title><author>Peymani, Mohammad ; Alavi, Seyed Mehdi ; Rezaei, Mehran</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-proquest_journals_20220982123</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2017</creationdate><topic>Alumina</topic><topic>Aluminum oxide</topic><topic>Carbon</topic><topic>Catalysts</topic><topic>Catalytic converters</topic><topic>Conversion</topic><topic>Nickel</topic><topic>Oxidation</topic><topic>Propane</topic><topic>Reaction time</topic><topic>Reduction</topic><topic>Synthesis gas</topic><topic>Transitional aluminas</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Peymani, Mohammad</creatorcontrib><creatorcontrib>Alavi, Seyed Mehdi</creatorcontrib><creatorcontrib>Rezaei, Mehran</creatorcontrib><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>Peymani, Mohammad</au><au>Alavi, Seyed Mehdi</au><au>Rezaei, Mehran</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Synthesis Gas Production by Catalytic Partial Oxidation of Propane on Mesoporous Nanocrystalline Ni/Al^sub 2^O^sub 3^ Catalysts</atitle><jtitle>Applied catalysis. A, General</jtitle><date>2017-01-05</date><risdate>2017</risdate><volume>529</volume><spage>1</spage><pages>1-</pages><issn>0926-860X</issn><eissn>1873-3875</eissn><abstract>Propane partial oxidation to synthesis gas at various feed conditions was investigated over nickel catalysts supported on high surface area γ-alumina. The physicochemical characteristics of the calcined, reduced and spent samples were determined by TPR, BET, XRD, TPO and SEM analyses. The influences of Ni content, reduction and reaction temperatures, gas hourly space velocity (GHSV) and feed ratio on the catalytic properties were investigated. The activity measurements revealed that the propane conversion had a direct relation with reaction temperature and nickel loading and increased with increasing of both these factors. However, there was an optimum value for nickel content and reaction temperature in which the H2 and CO yields were maximum. The 7.5 wt% Ni/Al2O3 exhibited high stability for 12 h without any decrease in activity. However, the selectivity declined gradually with reaction time due to carbon formation. The TPO analysis revealed that an increase in O2/C molar ratio from 0.25 to 0.75 caused a decrease in the amount of deposited carbon. Also, the amount of accumulated carbon slightly decreased with rising the reaction temperature. These results were confirmed by the SEM analysis and the filamentous carbon was observed on the catalyst surface. In addition, the increase in reduction temperature caused an increase in C3H8 conversion and H2/CO ratio.</abstract><cop>Amsterdam</cop><pub>Elsevier Science SA</pub></addata></record> |
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subjects | Alumina Aluminum oxide Carbon Catalysts Catalytic converters Conversion Nickel Oxidation Propane Reaction time Reduction Synthesis gas Transitional aluminas |
title | Synthesis Gas Production by Catalytic Partial Oxidation of Propane on Mesoporous Nanocrystalline Ni/Al^sub 2^O^sub 3^ Catalysts |
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