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

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PP-IV-7MESOPOROUS ANODES BASED ON YSZ DOPED WITHTiO 2 OR CeO 2 FOR DIRECT OXIDATION OF HYDROCARBONSIN ELECTROCATALYTIC MEMBRANE REACTORV. Pârvulescu 1 , S. Somacescu 1 , P. Osiceanu 1 , A. Cojocaru 2 , D-I. Vaireanu 2 and B.L. Su 31 <strong>Institute</strong> <strong>of</strong> Physical Chemistry, Spl. Independentei 202, Bucharest, RomâniaE-mail: vpirvulescu@chimfiz.icf.ro2 University Politehnica <strong>of</strong> Bucharest, Faculty <strong>of</strong> applied Chemistry and Materials Science,1-7 Polizu St., Bucharest3 University <strong>of</strong> Namur (FUNDP), Laboratoire de Chimie des Matériaux Inorganiques,61 rue de Bruxelles, B-5000 Namur, BelgiumIntroductionFuel cells with solid oxide (SOFCs) show <strong>the</strong> most promise for being able to directlyutilize hydrocarbon fuels [1]. Developments <strong>of</strong> intermediate-temperature solid oxide fuel cellsrequire optimization <strong>of</strong> anode compositions and microstructure. Incorporation <strong>of</strong> titania orceria was proved to enhance <strong>the</strong> performance <strong>of</strong> conventional anode cermets, consisting <strong>of</strong>metallic Ni and yttria stabilized zirconia (YSZ). The present study is centered on <strong>the</strong> syn<strong>the</strong>sis<strong>of</strong> mesoporous Ni and 8 mol% yttria-stabilized zirconia doped with titania or ceria andutilization <strong>of</strong> <strong>the</strong>se materials in direct oxidation <strong>of</strong> hydrocarbons in electrocatalytic membranereactor. The application <strong>of</strong> membrane reactors to <strong>the</strong> hydrocarbon oxidation has attractedconsiderable attention in <strong>the</strong> recent years [2,3].ExperimentalMesoporous x%TiO 2 (CeO 2 ) - ZrO 2 – 8%Y 2 O 3 powders with x = 5, 10, 15, 20 and 30molar content were syn<strong>the</strong>sized by hydro<strong>the</strong>rmal treatment using cetyltrimetyl-ammoniumbromide as surfactant, zirconium oxychloride - ZrOCl 2 , Y(NO 3 ) 3 , titanium propoxide asinorganic precursors and urea as <strong>the</strong> hydrolyzing agent. The molar ratio used was <strong>the</strong>following: oxide/surfactant/urea = 1: 0, 36: 7. The mixture was loaded into Teflon link steelautoclave and heated 3 days at 100 °C. All <strong>the</strong> products obtained were filtered, washed anddried at 100 °C and calcinated in a flow <strong>of</strong> N 2 followed by a flow <strong>of</strong> air at 550 °C. Ni wassupported by impregnation from aqueous Ni (NO 3 ) 2 solution. The obtained materials werecharacterized by X-ray diffraction, SEM and TEM microscopy, IR, UV-Vis, X-rayPhotoelectron and electrochemical impedance (EI) spectroscopy, N 2 adsorption-desorption.Two electrode and three electrode cell configurations were used in conjunction with EIS, in<strong>the</strong> range <strong>of</strong> 100 KHz to 10m Hz, to determine <strong>the</strong> ionic resistivity and its dependence on <strong>the</strong>TiO 2 and CeO 2 concentration. The electrochemical reactor was constructed from YSZ disc <strong>of</strong>408

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