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

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OP-II-8MODELING OF DIESEL FILTERS FOR PARTICULATE REMOVALMatyáš Schejbal a , Petr Kočí a , Milan Kubíček b , Miloš Marek aa Department <strong>of</strong> Chemical Engineering, <strong>Institute</strong> <strong>of</strong> Chemical Technology PragueFax: +420 220 444 320, e-mail: matyas.schejbal@vscht.cz, http://www.vscht.cz/monolithb Department <strong>of</strong> Ma<strong>the</strong>matics, <strong>Institute</strong> <strong>of</strong> Chemical Technology PragueTechnická 5, 166 28 Prague 6 – Dejvice, Czech RepublicA diesel particulate filter(DPF) is regarded as <strong>the</strong> most hopeful technology to reduceparticulate matter or soot from exhaust gas <strong>of</strong> a diesel engine with filtration efficienciesfrequently excessing 90%. It is constructed from a square cell monolith structure and <strong>the</strong>channels are plugged at alternate ends. Exhaust gas entering <strong>the</strong> channel is forced to exitthrough <strong>the</strong> ceramic porous wall into <strong>the</strong> adjoining cells and thus leaving behind <strong>the</strong>particulates. The collected particulate matter inside <strong>the</strong> trap has to be periodically oxidized toreduce <strong>the</strong> pressure drop. The burning <strong>of</strong> <strong>the</strong> collected particle matter inside <strong>the</strong> traprepresents DPF regeneration. The deposition <strong>of</strong> particles and <strong>the</strong> regeneration <strong>of</strong> filters aresubject <strong>of</strong> modeling. We have developed an advanced ma<strong>the</strong>matical nonstationary spatially2D model <strong>of</strong> <strong>the</strong> filter and its regeneration. The momentum, mass and enthalpy balances <strong>of</strong><strong>the</strong> gas and <strong>the</strong> solid phase were employed in <strong>the</strong> model including <strong>the</strong> description <strong>of</strong> heatconduction, diffusion in <strong>the</strong> solid phase and complex soot combustion kinetics. Thedescription <strong>of</strong> kinetics <strong>of</strong> two types <strong>of</strong> combustion by O 2 – both <strong>the</strong> <strong>the</strong>rmal initiated one and<strong>the</strong> catalyzed one (e.g. Ce oxides based catalyst is added to <strong>the</strong> fuel) and <strong>the</strong> oxidation by NO 2is used in <strong>the</strong> reaction-diffusion equations for each gaseous component. The results <strong>of</strong>simulations include <strong>the</strong> prediction <strong>of</strong> development <strong>of</strong> concentrations, temperature, pressureand flow pattern, soot layer thickness along <strong>the</strong> filter. Contribution presents parametricstudies, simulations review and detailed discussion <strong>of</strong> <strong>the</strong> kinetics <strong>of</strong> NO 2 -assisted sootoxidation coupled with NO/NO 2 equilibrium reaction and also a filtration model. Thefiltration model includes cake and deep-bed filtrations and thus predicts porosity,permeability, filtration efficiency <strong>of</strong> <strong>the</strong> soot layer and <strong>the</strong> wall. Main advantage <strong>of</strong> <strong>the</strong>developed numerical model for simulations is fast computing <strong>of</strong> both <strong>the</strong> regeneration processand <strong>the</strong> DPF loading. S<strong>of</strong>tware for <strong>the</strong> solution <strong>of</strong> <strong>the</strong> above mentioned models will bedescribed and results for various operation conditions will be presented.89

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