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

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OP-V-13DESIGN OF PILOT REACTOR AND MONOLITHIC CATALYST FORAUTOTERMAL REFORMING OF OXYGENATESV. Sadykov a,b , N. Mezentseva a *, Z. Vostrikov a , G. Alikina a , S. Pavlova a , S. Beloshapkin c ,J.R.H. Ross c , V. Ulyanitsky da <strong>Boreskov</strong> <strong>Institute</strong> <strong>of</strong> <strong>Catalysis</strong>, Pr. Akademika Lavrentieva, 5, Novosibirsk, 630090, Russia*Corresponding author: +7-383-3308056, mnv@catalysis.rub Novosibirsk State University, Novosibirsk, 630090, Russiac University <strong>of</strong> Limerick, Limerick, Irelandd Lavrentiev <strong>Institute</strong> <strong>of</strong> Hydrodynamics, Novosibirsk, RussiaTransformation <strong>of</strong> bi<strong>of</strong>uels into syngas via selective oxidation/auto<strong>the</strong>rmal reforming isnow considered as one <strong>of</strong> <strong>the</strong> most important task <strong>of</strong> catalysis in <strong>the</strong> energy-related fields.However, due to a high reactivity <strong>of</strong> oxygenates a heavy coking is observed leading to <strong>the</strong>catalyst deactivation. To deal with this phenomenon, active components comprised <strong>of</strong>complex oxides with a high lattice oxygen mobility (favors efficient gasification <strong>of</strong> cokeprecursors) promoted by precious metals (responsible for oxygenates activation) aresuggested. For achieving a high performance, monolithic substrates with a good <strong>the</strong>rmalconductivity could be promising for providing an efficient heat transfer from <strong>the</strong> inletexo<strong>the</strong>rmal zone <strong>of</strong> <strong>the</strong> reactor (where oxygen is consumed) into its rear part, whereendo<strong>the</strong>rmal steam and dry reforming occur. To prevent <strong>the</strong>rmal cracking <strong>of</strong> oxygenates andprovide an efficient evaporation <strong>of</strong> fuel at a small overheating degree, ensure its good mixingwith steam/air, new types <strong>of</strong> evaporators/mixers are to be designed. This paper presentsresults <strong>of</strong> research aimed at addressing <strong>the</strong>se problems at <strong>the</strong> pilot-scale level.As heat-conducting substrates, fechraloy foil (thickness up to 0.2 mm) and gauze (wirediameter 0.2-0.3 mm, square mesh ~ 0.5x0.5 mm) protected by corundum layer via blastdusting were used. Stacked flat and corrugated bands <strong>of</strong> foil were winded into <strong>the</strong> Arkhimedspiral (external cylinder diameter ~50 mm, length 20 mm) forming triangular channels withsizes up to 3 mm. After spark-welding <strong>of</strong> tungsten rods as electrical current inlets, this heatedmonolithic substrate was used for <strong>the</strong> evaporation <strong>of</strong> liquid fuels sprayed via a nozzle directlyinto its inlet part. Similar fechraloy substrates or discs cut from fechraloy gauzes were usedfor preparation <strong>of</strong> monolithic catalysts by washcoating with a slurry <strong>of</strong> Ln-Ce-Zr-O mixedoxides (Ce:Zr = 1:1, Ln = La, Pr, or Sm) prepared via Pechini route and ultrasonicallydispersed in water with addition <strong>of</strong> peptizers and surfactants (loading up to 10 wt.%). Preciousmetals up to 1% wt.% <strong>of</strong> Pt, Pd, Ru, ) and/or Ni (up to 10 wt. %) with respect to doped ceriazirconiaoxide were supported by incipient wetness impregnation. For preparation <strong>of</strong> pilot-192

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