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

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OP-V-18dynamic saturation with additional oxygen pulses and immediately following pump-probeexperiments allowed defined investigations with oxidation pr<strong>of</strong>iles close to those present atatmospheric pressure in a short contact time reactor.Results and discussionImpacts <strong>of</strong> <strong>the</strong> oxidation state and co-presence <strong>of</strong> methane and oxygen clearly differ as afunction <strong>of</strong> dopants promoting <strong>the</strong> fluorite structured ceria/zirconia solid solution supportingPt as active metal. Employing Pr as dopant yields a catalyst capable to preserve a minimumselectivity in all studied cases using <strong>the</strong> «working state» <strong>of</strong> <strong>the</strong> catalyst as origin. A significantand fast hydrogen release was observed, which varied only slightly altering <strong>the</strong> oxidation state<strong>of</strong> <strong>the</strong> sample by pre-injected oxygen. Fur<strong>the</strong>rmore, <strong>the</strong> co-presence <strong>of</strong> O 2 and CH 4 injectingboth reactants at short time <strong>of</strong>fset did not lead to an entire loss <strong>of</strong> selectivity. The weakness <strong>of</strong><strong>the</strong> Pr doped sample relates to <strong>the</strong> relative slow formation <strong>of</strong> CO. It is currently not entirelyclear if <strong>the</strong> low CO formation rate, i.e. <strong>the</strong> freeing <strong>of</strong> <strong>the</strong> catalyst surface from CH x species,leads to a build-up <strong>of</strong> carbonaceous species impacting under ambient pressure conditions on<strong>the</strong> activity. However, <strong>the</strong> presence <strong>of</strong> CH x at «working state» is clearly confirmed for <strong>the</strong> Gddoped sample. The activity <strong>of</strong> <strong>the</strong> Pr doped catalyst is clearly lower than that <strong>of</strong> <strong>the</strong> Gd dopedcatalyst, which may be slightly observed in terms <strong>of</strong> hydrogen release, but it become muchmore obvious when focusing on <strong>the</strong> formation <strong>of</strong> carbon monoxide as primary carbon oxidesproduct. The Gd doped sample shows a complex behavior <strong>of</strong> performance as a function <strong>of</strong> <strong>the</strong>catalyst’s oxidation state.The Gd-doped catalyst seems more selective towards syn<strong>the</strong>sis gas at <strong>the</strong> «working state»established by reaction <strong>of</strong> oxygen with methane injected at 0.5 seconds <strong>of</strong>fset at a ratio <strong>of</strong> 1:2.The Pr-doped catalyst reveals a more stable behavior showing no major loss in selectivitywhen <strong>the</strong> «working state» determined quantity <strong>of</strong> oxygen becomes altered or when oxygenand methane become injected with shorter time <strong>of</strong>fset.Acknowledgement: Support by <strong>the</strong> joined European laboratory on catalysis betweenFrance and Russia (LFRC,LEA-313) and support by <strong>the</strong> RFBR-CNRS 05-03-34761 project isacknowledged.References:1. R.E. Kirk, D.F. Othmer (Eds.), third ed., Encyclopedia <strong>of</strong> Chemical Technology, vol. 12, Wiley Interscience,New York, 1980, p.952.2. R. Horn, K.A. Williams, N.J. Degenstein, A. Bitsch-Larsen, et al., J. Catal. 249 (2007), p.380.3. R. Horn, K.A. Williams, N.J. Degenstein, L.D. Schmidt, Chem. Eng. Sci. 62 (2007), p.1298.4. V.A. Sadykov, et al., <strong>Catalysis</strong> Today 117(2006), p.475.203

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