Structure of flame-made vanadia/titania and catalytic behavior in the partial oxidation of o-xylene

Vanadia/titania particles with a specific surface area (SSA) up to 195 m 2 g −1 and a V 2O 5 content up to 40% (w/w) or V coverage up to 59 V nm −2 were prepared by flame spray pyrolysis (FSP) under various conditions. The catalysts were characterized by nitrogen adsorption, X-ray diffraction, tempe...

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Veröffentlicht in:Journal of catalysis 2008-05, Vol.256 (1), p.74-83
Hauptverfasser: Schimmoeller, Bjoern, Schulz, Heiko, Ritter, Anika, Reitzmann, Andreas, Kraushaar-Czarnetzki, Bettina, Baiker, Alfons, Pratsinis, Sotiris E.
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container_end_page 83
container_issue 1
container_start_page 74
container_title Journal of catalysis
container_volume 256
creator Schimmoeller, Bjoern
Schulz, Heiko
Ritter, Anika
Reitzmann, Andreas
Kraushaar-Czarnetzki, Bettina
Baiker, Alfons
Pratsinis, Sotiris E.
description Vanadia/titania particles with a specific surface area (SSA) up to 195 m 2 g −1 and a V 2O 5 content up to 40% (w/w) or V coverage up to 59 V nm −2 were prepared by flame spray pyrolysis (FSP) under various conditions. The catalysts were characterized by nitrogen adsorption, X-ray diffraction, temperature-programmed reduction, and in situ Raman spectroscopy and tested for partial oxidation of o-xylene. Depending on vanadia content, monomeric, polymeric, and crystalline vanadia species were formed on TiO 2 support particles by FSP. Increasing the high-temperature particle residence time and concentration (production rate) during FSP reduced the SSA and increased the vanadia coverage of TiO 2 beyond a theoretical “monolayer” (>8–10 V nm −2) while retaining amorphous (monomeric and polymeric) VO x surface species. Controlling liquid precursor and dispersion gas feed rates, precursor concentration, and V 2O 5 content allowed the tailoring of SSA and the population of the different VO x species in these vanadia/titania mixed oxides. For comparison, vanadia/titania catalysts containing 10% (w/w) V 2O 5 with comparable SSA and V coverage were prepared by impregnation, resulting in typical amorphous (10 V nm −2) VO x species. Catalysts containing 7, 10, and 20% (w/w) V 2O 5 were deposited directly from the flame on ceramic foams that were tested for the partial oxidation of o-xylene to phthalic anhydride. The global activity of flame-made and conventionally impregnated catalysts depended mainly on SSA and vanadia loading (number of V surface sites), whereas the amorphous or crystalline nature of the VO x species seemed to be less critical. In contrast, selectivity to phthalic anhydride was significantly affected by the nature of the VO x species; amorphous species exhibited higher selectivity for conversion
doi_str_mv 10.1016/j.jcat.2008.03.005
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For comparison, vanadia/titania catalysts containing 10% (w/w) V 2O 5 with comparable SSA and V coverage were prepared by impregnation, resulting in typical amorphous (&lt;10 V nm −2) and crystalline (&gt;10 V nm −2) VO x species. Catalysts containing 7, 10, and 20% (w/w) V 2O 5 were deposited directly from the flame on ceramic foams that were tested for the partial oxidation of o-xylene to phthalic anhydride. The global activity of flame-made and conventionally impregnated catalysts depended mainly on SSA and vanadia loading (number of V surface sites), whereas the amorphous or crystalline nature of the VO x species seemed to be less critical. 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The catalysts were characterized by nitrogen adsorption, X-ray diffraction, temperature-programmed reduction, and in situ Raman spectroscopy and tested for partial oxidation of o-xylene. Depending on vanadia content, monomeric, polymeric, and crystalline vanadia species were formed on TiO 2 support particles by FSP. Increasing the high-temperature particle residence time and concentration (production rate) during FSP reduced the SSA and increased the vanadia coverage of TiO 2 beyond a theoretical “monolayer” (&gt;8–10 V nm −2) while retaining amorphous (monomeric and polymeric) VO x surface species. Controlling liquid precursor and dispersion gas feed rates, precursor concentration, and V 2O 5 content allowed the tailoring of SSA and the population of the different VO x species in these vanadia/titania mixed oxides. For comparison, vanadia/titania catalysts containing 10% (w/w) V 2O 5 with comparable SSA and V coverage were prepared by impregnation, resulting in typical amorphous (&lt;10 V nm −2) and crystalline (&gt;10 V nm −2) VO x species. Catalysts containing 7, 10, and 20% (w/w) V 2O 5 were deposited directly from the flame on ceramic foams that were tested for the partial oxidation of o-xylene to phthalic anhydride. The global activity of flame-made and conventionally impregnated catalysts depended mainly on SSA and vanadia loading (number of V surface sites), whereas the amorphous or crystalline nature of the VO x species seemed to be less critical. In contrast, selectivity to phthalic anhydride was significantly affected by the nature of the VO x species; amorphous species exhibited higher selectivity for conversion &lt;90% compared with catalysts containing crystalline V 2O 5.</description><subject>Catalysis</subject><subject>Ceramic foam</subject><subject>Ceramic sponge</subject><subject>Chemical engineering</subject><subject>Chemistry</subject><subject>Exact sciences and technology</subject><subject>Flame-coated</subject><subject>Flame-spray pyrolysis</subject><subject>General and physical chemistry</subject><subject>in situ Raman spectroscopy</subject><subject>Nanostructured V 2O 5/TiO 2</subject><subject>Nitrogen</subject><subject>Oxidation</subject><subject>Partial oxidation</subject><subject>Phthalic anhydride</subject><subject>Spectrum analysis</subject><subject>Theory of reactions, general kinetics. Catalysis. 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Nomenclature, chemical documentation, computer chemistry</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Schimmoeller, Bjoern</creatorcontrib><creatorcontrib>Schulz, Heiko</creatorcontrib><creatorcontrib>Ritter, Anika</creatorcontrib><creatorcontrib>Reitzmann, Andreas</creatorcontrib><creatorcontrib>Kraushaar-Czarnetzki, Bettina</creatorcontrib><creatorcontrib>Baiker, Alfons</creatorcontrib><creatorcontrib>Pratsinis, Sotiris E.</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>Schimmoeller, Bjoern</au><au>Schulz, Heiko</au><au>Ritter, Anika</au><au>Reitzmann, Andreas</au><au>Kraushaar-Czarnetzki, Bettina</au><au>Baiker, Alfons</au><au>Pratsinis, Sotiris E.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Structure of flame-made vanadia/titania and catalytic behavior in the partial oxidation of o-xylene</atitle><jtitle>Journal of catalysis</jtitle><date>2008-05-15</date><risdate>2008</risdate><volume>256</volume><issue>1</issue><spage>74</spage><epage>83</epage><pages>74-83</pages><issn>0021-9517</issn><eissn>1090-2694</eissn><coden>JCTLA5</coden><abstract>Vanadia/titania particles with a specific surface area (SSA) up to 195 m 2 g −1 and a V 2O 5 content up to 40% (w/w) or V coverage up to 59 V nm −2 were prepared by flame spray pyrolysis (FSP) under various conditions. The catalysts were characterized by nitrogen adsorption, X-ray diffraction, temperature-programmed reduction, and in situ Raman spectroscopy and tested for partial oxidation of o-xylene. Depending on vanadia content, monomeric, polymeric, and crystalline vanadia species were formed on TiO 2 support particles by FSP. Increasing the high-temperature particle residence time and concentration (production rate) during FSP reduced the SSA and increased the vanadia coverage of TiO 2 beyond a theoretical “monolayer” (&gt;8–10 V nm −2) while retaining amorphous (monomeric and polymeric) VO x surface species. Controlling liquid precursor and dispersion gas feed rates, precursor concentration, and V 2O 5 content allowed the tailoring of SSA and the population of the different VO x species in these vanadia/titania mixed oxides. For comparison, vanadia/titania catalysts containing 10% (w/w) V 2O 5 with comparable SSA and V coverage were prepared by impregnation, resulting in typical amorphous (&lt;10 V nm −2) and crystalline (&gt;10 V nm −2) VO x species. Catalysts containing 7, 10, and 20% (w/w) V 2O 5 were deposited directly from the flame on ceramic foams that were tested for the partial oxidation of o-xylene to phthalic anhydride. The global activity of flame-made and conventionally impregnated catalysts depended mainly on SSA and vanadia loading (number of V surface sites), whereas the amorphous or crystalline nature of the VO x species seemed to be less critical. In contrast, selectivity to phthalic anhydride was significantly affected by the nature of the VO x species; amorphous species exhibited higher selectivity for conversion &lt;90% compared with catalysts containing crystalline V 2O 5.</abstract><cop>Amsterdam</cop><pub>Elsevier Inc</pub><doi>10.1016/j.jcat.2008.03.005</doi><tpages>10</tpages></addata></record>
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subjects Catalysis
Ceramic foam
Ceramic sponge
Chemical engineering
Chemistry
Exact sciences and technology
Flame-coated
Flame-spray pyrolysis
General and physical chemistry
in situ Raman spectroscopy
Nanostructured V 2O 5/TiO 2
Nitrogen
Oxidation
Partial oxidation
Phthalic anhydride
Spectrum analysis
Theory of reactions, general kinetics. Catalysis. Nomenclature, chemical documentation, computer chemistry
title Structure of flame-made vanadia/titania and catalytic behavior in the partial oxidation of o-xylene
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