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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Veröffentlicht in:Journal of catalysis 2007-08, Vol.250 (1), p.128-138
Hauptverfasser: Solsona, B., Ivars, F., Concepción, P., López Nieto, J.M.
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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.
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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 &gt; MoVTeO = MoVSbNbO &gt; MoVSbO &gt; 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. 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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 &gt; MoVTeO = MoVSbNbO &gt; MoVSbO &gt; 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. 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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 &gt; MoVTeO = MoVSbNbO &gt; MoVSbO &gt; 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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