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3D reconstruction and pore-scale modeling of coated catalytic filters for automotive exhaust gas aftertreatment

The result's identifiers

  • Result code in IS VaVaI

    <a href="https://www.isvavai.cz/riv?ss=detail&h=RIV%2F61388998%3A_____%2F19%3A00497313" target="_blank" >RIV/61388998:_____/19:00497313 - isvavai.cz</a>

  • Alternative codes found

    RIV/60461373:22340/19:43919370 RIV/49777513:23640/19:43955070

  • Result on the web

    <a href="https://www.sciencedirect.com/science/article/pii/S0920586117308416" target="_blank" >https://www.sciencedirect.com/science/article/pii/S0920586117308416</a>

  • DOI - Digital Object Identifier

    <a href="http://dx.doi.org/10.1016/j.cattod.2017.12.025" target="_blank" >10.1016/j.cattod.2017.12.025</a>

Alternative languages

  • Result language

    angličtina

  • Original language name

    3D reconstruction and pore-scale modeling of coated catalytic filters for automotive exhaust gas aftertreatment

  • Original language description

    This paper introduces a newly developed methodology for the pore-scale simulation of flow, diffusion and reaction in the coated catalytic filter. 3D morphology of the porous filter wall including the actual distribution of catalytic material is reconstructed from X-ray tomography (XRT) images and further validated with the mercury intrusion porosimetry (MIP). The reconstructed medium is then transformed into simulation mesh for OpenFOAM. Flow through free pores in the substrate as well as through the coated zones is simulated by porousSimpleFoam solver, while an in-house developed solver is used for component diffusion and reactions.nThree cordierite filter samples with different distribution of alumina-based coating ranging from in-wall to onwall are examined. Velocity, pressure and component concentration profiles are calculated enabling the prediction of permeability and component conversion depending on the actual microstructure of the wall. Thensimulation results suggest that the gas predominantly flows through remaining free pores in the filter wall and cracks in the coated layer. The mass transport into the coated domains inside the filter wall is enabled mainly by diffusion. Large domains of compact catalytic coating covering complete channel wall result in a significant increase of pressure drop as the local permeability of the coating is two orders of magnitude smaller than that of bare filter wall.

  • Czech name

  • Czech description

Classification

  • Type

    J<sub>imp</sub> - Article in a specialist periodical, which is included in the Web of Science database

  • CEP classification

  • OECD FORD branch

    20402 - Chemical process engineering

Result continuities

  • Project

    <a href="/en/project/LO1402" target="_blank" >LO1402: CENTEM+</a><br>

  • Continuities

    I - Institucionalni podpora na dlouhodoby koncepcni rozvoj vyzkumne organizace

Others

  • Publication year

    2019

  • Confidentiality

    S - Úplné a pravdivé údaje o projektu nepodléhají ochraně podle zvláštních právních předpisů

Data specific for result type

  • Name of the periodical

    Catalysis Today

  • ISSN

    0920-5861

  • e-ISSN

  • Volume of the periodical

    320

  • Issue of the periodical within the volume

    January

  • Country of publishing house

    NL - THE KINGDOM OF THE NETHERLANDS

  • Number of pages

    10

  • Pages from-to

    165-174

  • UT code for WoS article

    000448295200018

  • EID of the result in the Scopus database

    2-s2.0-85039838260