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Boreskov Institute of Catalysis of the Siberian Branch of Russian ...

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PP-III-5WASHCOATS FOR STRUCTURED REACTORS IN PROPANEOXIDATION. V 2 O 5 SUPPORTED ON TiO 2 WASHCOAT DEPOSITEDON METALLIC PLATES AND FOAMSA. Essakhi 1 , A. Löfberg 1 , S. Paul 1 , P. Supiot 2 , B. Mutel 2 , V. Le Courtois 1 ,E. Bordes-Richard 11Unité de Catalyse et de Chimie du Solide, UMR 8181, Université des Sciences etTechnologies de Lille, Bât. C3, Cité Scientifique, 59655 Villeneuve d'Ascq, France.Fax:+33-320436561; e-mail: axel.l<strong>of</strong>berg@univ-lille1.fr2Laboratoire de Génie des Procédés d’Interactions Fluides Réactifs-Matériau, Université desSciences et Techologies de Lille, Bât. C5, Cité Scientifique, 59655 Villeneuve d'Ascq, France.IntroductionMicroreactors or structured reactors (including heat exchanger-type reactors) <strong>of</strong>fer apotential to conduct mass or heat transfer-demanding reactions under safe conditions whilemaintaining and/or increasing selectivity and productivity. In <strong>the</strong> case <strong>of</strong> reactions <strong>of</strong> selectiveoxidation <strong>of</strong> hydrocarbons <strong>the</strong> whole mass <strong>of</strong> <strong>the</strong> transition metal oxide is reacting in usualreactors (fixed or fluidized beds) and it is not so straightforward to get high catalyticactivity/selectivity in a thin layer. The goal is <strong>the</strong>refore to obtain high surface area whencovering a low, geometric area <strong>of</strong> <strong>the</strong> metallic substrate, while maintaining a high mechanicaland chemical stability [1,2]. The coating <strong>of</strong> aluminum and <strong>of</strong> stainless steel plates byVO x /TiO 2 catalysts for oxidative dehydrogenation <strong>of</strong> propane [2-4] was studied using dipcoatingand sol-gel methods, which provided high mechanical stability but poor chemicalstability as revealed by <strong>the</strong> iron poisoning <strong>of</strong> <strong>the</strong> catalyst. Ano<strong>the</strong>r way <strong>of</strong> coating using aplasma-assisted chemical vapor deposition (PACVD) had already been explored in <strong>the</strong> case <strong>of</strong>silica supported cobalt for Fischer-Tropsch syn<strong>the</strong>sis <strong>of</strong> clean fuels [4-6]. In <strong>the</strong> present paper<strong>the</strong> parameters to control PACVD during <strong>the</strong> coating <strong>of</strong> metallic plates by VO x /TiO 2 catalystsfor ODH <strong>of</strong> propane are studied. The same PACVD technique was applied to metallic foamsfor <strong>the</strong> first time.Results and DiscussionPACVD <strong>of</strong> tetramethyldisiloxane used for silicon [6,7] was adapted to coat metallicsubstrates (here called S). A typical rate <strong>of</strong> increasing thickness <strong>of</strong> films <strong>of</strong> polymers is300 nm·mn –1 . A new sample holder was designed to allow <strong>the</strong> coating <strong>of</strong> metallic foam (Cr-Ni from Metafoam). After mineralisation in O 2 -N 2 plasma, a calcination step was applied tostabilize <strong>the</strong> layer <strong>of</strong> silica primer onto S. Titania was fur<strong>the</strong>r deposited on <strong>the</strong> SiO 2 /S plate orfoam by using an alcoholic/aqueous suspension <strong>of</strong> titania (anatase) powder (Aldrich).311

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