11.07.2015 Views

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

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

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

SHOW MORE
SHOW LESS

You also want an ePaper? Increase the reach of your titles

YUMPU automatically turns print PDFs into web optimized ePapers that Google loves.

OP-I-22al., 2008; Monolith, 2008). The NO x storage/reduction experiments are performed in <strong>the</strong>temperature range 100-500 °C in <strong>the</strong> presence <strong>of</strong> CO 2 and H 2 O.ModellingSpatially distributed NSRC model is developed (Kočí et al., 2008), considering <strong>the</strong>following ammonia reaction pathway: NH 3 is formed by <strong>the</strong> reaction <strong>of</strong> H 2 with NO x and itcan fur<strong>the</strong>r react with oxygen and NO x deposited on <strong>the</strong> catalyst surface, producing N 2 .Considering this scheme with ammonia as an active intermediate <strong>of</strong> <strong>the</strong> NO x reduction, agood agreement with experiments is obtained in terms <strong>of</strong> <strong>the</strong> NO x reduction dynamics andselectivity. Reduction front travelling in <strong>the</strong> flow direction along <strong>the</strong> reactor is predicted, with<strong>the</strong> NH 3 maximum on <strong>the</strong> moving boundary. When <strong>the</strong> front reaches <strong>the</strong> reactor outlet, <strong>the</strong>main NH 3 peak is observed in <strong>the</strong> exhaust gas (Kočí et al., 2008).Under certain operating conditions, a smaller NH 3 peak is observed experimentally at <strong>the</strong>reactor outlet just after <strong>the</strong> beginning <strong>of</strong> <strong>the</strong> regeneration phase (before <strong>the</strong> main NH 3 peak).We show that this more complex, double NH 3 peak dynamics can be described by <strong>the</strong> samespatially distributed model with proper values <strong>of</strong> kinetic parameters governing <strong>the</strong> rate <strong>of</strong> NH 3formation and decomposition.References1. Cumaranatunge L., Mulla S.S., Yezerets A., Currier N.W., Delgass W.N., Ribeiro F.H., Ammonia is ahydrogen carrier in <strong>the</strong> regeneration <strong>of</strong> Pt/BaO/Al 2 O 3 NO x traps with H 2 , Journal <strong>of</strong> <strong>Catalysis</strong> 246 (2007) 29.2. DieselNet, http://www.dieselnet.com (2008).3. Epling W.S., Campbell L.E., Yezerets A., Currier N.W., Parks J.E., Overview <strong>of</strong> <strong>the</strong> Fundamental Reactionsand Degradation Mechanisms <strong>of</strong> NO x Storage/Reduction Catalysts, <strong>Catalysis</strong> Reviews 46 (2004) 163.4. Epling W.S., Yezerets A., Currier N.W., The effects <strong>of</strong> regeneration conditions on NO x and NH 3 releasefrom NO x storage/reduction catalysts, Applied <strong>Catalysis</strong> B: Environmental 74 (2007) 117.5. Kobayashi T., Yamada T., Kayano K. Study <strong>of</strong> NO x Trap Reaction By Thermodynamic Calculation, SAETechnical Paper 970745 (1997).6. Kočí P., Plát F., Štěpánek J., Kubíček M., Marek M. Dynamics and selectivity <strong>of</strong> NO x reduction in NO xstorage catalytic monolith, <strong>Catalysis</strong> Today (2008) in press, doi:10.1016/j.cattod.2007.11.023.7. Monolith, http://www.vscht.cz/monolith (2008).68

Hooray! Your file is uploaded and ready to be published.

Saved successfully!

Ooh no, something went wrong!