Selective oxidation of n-butane over MoV-containing oxidic bronze catalysts
MoV-containing oxidic bronze catalysts were synthesized, characterized, and tested in the selective oxidation of n-butane. For comparison, an activated V–P–O catalyst was also studied. The catalytic behavior of MoV-containing catalysts was found to be dependent on both the catalyst composition and t...
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creator | Solsona, B. Ivars, F. Concepción, P. López Nieto, J.M. |
description | MoV-containing oxidic bronze catalysts were synthesized, characterized, and tested in the selective oxidation of
n-butane. For comparison, an activated V–P–O catalyst was also studied. The catalytic behavior of MoV-containing catalysts was found to be dependent on both the catalyst composition and the nature of crystalline phases. In this way, the M1 phase (i.e., Te
2M
20O
57 and (SbO)
2M
20O
56 in Te- and Sb-containing catalysts, respectively) is proposed as an active and selective crystalline phase for
n-butane oxidation on these catalysts. The selectivity to maleic anhydride/acid obtained on MoV-catalysts follows the order: MoVTeNbO
>
MoVTeO
=
MoVSbNbO
>
MoVSbO
>
MoVNbO. Although less selective than a vanadium phosphorous catalyst, a higher productivity to MA is obtained over a MoVTeNbO mixed oxide catalyst as a consequence of its remarkably superior catalytic activity. Moreover, the amount of maleic anhydride obtained on oxidic bronze catalysts strongly depends on the composition of the feed. In addition, the nature of active sites, the reaction network for
n-butane oxidation, and a comparison of their catalytic performance in the oxidation of C
2–C
4 alkanes are discussed. |
doi_str_mv | 10.1016/j.jcat.2007.05.023 |
format | Article |
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n-butane. For comparison, an activated V–P–O catalyst was also studied. The catalytic behavior of MoV-containing catalysts was found to be dependent on both the catalyst composition and the nature of crystalline phases. In this way, the M1 phase (i.e., Te
2M
20O
57 and (SbO)
2M
20O
56 in Te- and Sb-containing catalysts, respectively) is proposed as an active and selective crystalline phase for
n-butane oxidation on these catalysts. The selectivity to maleic anhydride/acid obtained on MoV-catalysts follows the order: MoVTeNbO
>
MoVTeO
=
MoVSbNbO
>
MoVSbO
>
MoVNbO. Although less selective than a vanadium phosphorous catalyst, a higher productivity to MA is obtained over a MoVTeNbO mixed oxide catalyst as a consequence of its remarkably superior catalytic activity. Moreover, the amount of maleic anhydride obtained on oxidic bronze catalysts strongly depends on the composition of the feed. In addition, the nature of active sites, the reaction network for
n-butane oxidation, and a comparison of their catalytic performance in the oxidation of C
2–C
4 alkanes are discussed.</description><identifier>ISSN: 0021-9517</identifier><identifier>EISSN: 1090-2694</identifier><identifier>DOI: 10.1016/j.jcat.2007.05.023</identifier><identifier>CODEN: JCTLA5</identifier><language>eng</language><publisher>Amsterdam: Elsevier Inc</publisher><subject>Catalysis ; Chemistry ; Crystallography ; Exact sciences and technology ; FTIR of adsorbed 1-butene ; General and physical chemistry ; Materials science ; Mo–V–Te–Sb–Nb mixed metal oxides ; n-Butane oxidation to maleic anhydride ; Oxidation ; Propane to acrylic acid ; Theory of reactions, general kinetics. Catalysis. Nomenclature, chemical documentation, computer chemistry ; V–P–O catalyst</subject><ispartof>Journal of catalysis, 2007-08, Vol.250 (1), p.128-138</ispartof><rights>2007 Elsevier Inc.</rights><rights>2007 INIST-CNRS</rights><rights>Copyright © 2007 Elsevier B.V. All rights reserved.</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c423t-448565e82d390ef382eb8de26a47db96a23bed0d08008a765662b66b7a4a7c153</citedby></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://dx.doi.org/10.1016/j.jcat.2007.05.023$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>315,782,786,3552,27931,27932,46002</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=18964864$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Solsona, B.</creatorcontrib><creatorcontrib>Ivars, F.</creatorcontrib><creatorcontrib>Concepción, P.</creatorcontrib><creatorcontrib>López Nieto, J.M.</creatorcontrib><title>Selective oxidation of n-butane over MoV-containing oxidic bronze catalysts</title><title>Journal of catalysis</title><description>MoV-containing oxidic bronze catalysts were synthesized, characterized, and tested in the selective oxidation of
n-butane. For comparison, an activated V–P–O catalyst was also studied. The catalytic behavior of MoV-containing catalysts was found to be dependent on both the catalyst composition and the nature of crystalline phases. In this way, the M1 phase (i.e., Te
2M
20O
57 and (SbO)
2M
20O
56 in Te- and Sb-containing catalysts, respectively) is proposed as an active and selective crystalline phase for
n-butane oxidation on these catalysts. The selectivity to maleic anhydride/acid obtained on MoV-catalysts follows the order: MoVTeNbO
>
MoVTeO
=
MoVSbNbO
>
MoVSbO
>
MoVNbO. Although less selective than a vanadium phosphorous catalyst, a higher productivity to MA is obtained over a MoVTeNbO mixed oxide catalyst as a consequence of its remarkably superior catalytic activity. Moreover, the amount of maleic anhydride obtained on oxidic bronze catalysts strongly depends on the composition of the feed. In addition, the nature of active sites, the reaction network for
n-butane oxidation, and a comparison of their catalytic performance in the oxidation of C
2–C
4 alkanes are discussed.</description><subject>Catalysis</subject><subject>Chemistry</subject><subject>Crystallography</subject><subject>Exact sciences and technology</subject><subject>FTIR of adsorbed 1-butene</subject><subject>General and physical chemistry</subject><subject>Materials science</subject><subject>Mo–V–Te–Sb–Nb mixed metal oxides</subject><subject>n-Butane oxidation to maleic anhydride</subject><subject>Oxidation</subject><subject>Propane to acrylic acid</subject><subject>Theory of reactions, general kinetics. Catalysis. Nomenclature, chemical documentation, computer chemistry</subject><subject>V–P–O catalyst</subject><issn>0021-9517</issn><issn>1090-2694</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2007</creationdate><recordtype>article</recordtype><recordid>eNp9kE1LxDAQhoMouH78AU9F8Ng6SZM0BS8ifqHiwY9rSNOppKyJJt1F_fVmXcGbp4HheedlHkIOKFQUqDweq9GaqWIATQWiAlZvkBmFFkomW75JZgCMlq2gzTbZSWkEoFQINSM3DzhHO7klFuHD9WZywRdhKHzZLSbj83aJsbgLz6UNfjLOO__yQzpbdDH4LyxysZl_pintka3BzBPu_85d8nRx_nh2Vd7eX16fnd6WlrN6KjlXQgpUrK9bwKFWDDvVI5OGN33XSsPqDnvoQQEo00ghJeuk7BrDTWOpqHfJ4fruWwzvC0yTHsMi-lypaSs4b1UjM8TWkI0hpYiDfovu1cRPTUGvnOlRr5zplTMNQmdnOXT0e9kka-ZDNN669JdUreRK8sydrDnMby4dRp2sQ2-xdzHb1H1w_9V8A-Nwga8</recordid><startdate>20070815</startdate><enddate>20070815</enddate><creator>Solsona, B.</creator><creator>Ivars, F.</creator><creator>Concepción, P.</creator><creator>López Nieto, J.M.</creator><general>Elsevier Inc</general><general>Elsevier</general><general>Elsevier BV</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope></search><sort><creationdate>20070815</creationdate><title>Selective oxidation of n-butane over MoV-containing oxidic bronze catalysts</title><author>Solsona, B. ; Ivars, F. ; Concepción, P. ; López Nieto, J.M.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c423t-448565e82d390ef382eb8de26a47db96a23bed0d08008a765662b66b7a4a7c153</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2007</creationdate><topic>Catalysis</topic><topic>Chemistry</topic><topic>Crystallography</topic><topic>Exact sciences and technology</topic><topic>FTIR of adsorbed 1-butene</topic><topic>General and physical chemistry</topic><topic>Materials science</topic><topic>Mo–V–Te–Sb–Nb mixed metal oxides</topic><topic>n-Butane oxidation to maleic anhydride</topic><topic>Oxidation</topic><topic>Propane to acrylic acid</topic><topic>Theory of reactions, general kinetics. Catalysis. Nomenclature, chemical documentation, computer chemistry</topic><topic>V–P–O catalyst</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Solsona, B.</creatorcontrib><creatorcontrib>Ivars, F.</creatorcontrib><creatorcontrib>Concepción, P.</creatorcontrib><creatorcontrib>López Nieto, J.M.</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><jtitle>Journal of catalysis</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Solsona, B.</au><au>Ivars, F.</au><au>Concepción, P.</au><au>López Nieto, J.M.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Selective oxidation of n-butane over MoV-containing oxidic bronze catalysts</atitle><jtitle>Journal of catalysis</jtitle><date>2007-08-15</date><risdate>2007</risdate><volume>250</volume><issue>1</issue><spage>128</spage><epage>138</epage><pages>128-138</pages><issn>0021-9517</issn><eissn>1090-2694</eissn><coden>JCTLA5</coden><abstract>MoV-containing oxidic bronze catalysts were synthesized, characterized, and tested in the selective oxidation of
n-butane. For comparison, an activated V–P–O catalyst was also studied. The catalytic behavior of MoV-containing catalysts was found to be dependent on both the catalyst composition and the nature of crystalline phases. In this way, the M1 phase (i.e., Te
2M
20O
57 and (SbO)
2M
20O
56 in Te- and Sb-containing catalysts, respectively) is proposed as an active and selective crystalline phase for
n-butane oxidation on these catalysts. The selectivity to maleic anhydride/acid obtained on MoV-catalysts follows the order: MoVTeNbO
>
MoVTeO
=
MoVSbNbO
>
MoVSbO
>
MoVNbO. Although less selective than a vanadium phosphorous catalyst, a higher productivity to MA is obtained over a MoVTeNbO mixed oxide catalyst as a consequence of its remarkably superior catalytic activity. Moreover, the amount of maleic anhydride obtained on oxidic bronze catalysts strongly depends on the composition of the feed. In addition, the nature of active sites, the reaction network for
n-butane oxidation, and a comparison of their catalytic performance in the oxidation of C
2–C
4 alkanes are discussed.</abstract><cop>Amsterdam</cop><pub>Elsevier Inc</pub><doi>10.1016/j.jcat.2007.05.023</doi><tpages>11</tpages></addata></record> |
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subjects | Catalysis Chemistry Crystallography Exact sciences and technology FTIR of adsorbed 1-butene General and physical chemistry Materials science Mo–V–Te–Sb–Nb mixed metal oxides n-Butane oxidation to maleic anhydride Oxidation Propane to acrylic acid Theory of reactions, general kinetics. Catalysis. Nomenclature, chemical documentation, computer chemistry V–P–O catalyst |
title | Selective oxidation of n-butane over MoV-containing oxidic bronze catalysts |
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