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  • Mathematical models of reaction and transport in porous catalyst on three different scales (nano, micro, and macro) are presented. Methodology is demonstrated on CO oxidation in porous Pt/gamma-Al2O3 catalyst, washcoated on monolith. Morphological characteristics are obtained from TEM and SEM images of the washcoat cross-section. Methods for passing the model results from the bottom to the top level are discussed. On the nano level (I), spatially 3D model of a single meso-porous gamma-Al2O3 particle (approximate to 0.1-1 mu m) is used. Digital reconstruction of porous medium is here based on virtual agglomeration of Al2O3 nanoparticles and consequent deposition of individual Pt crystallites. The model considers the effects of catalytic sites sizes and diffusion in small meso-pores (d approximate to 10 nm). On the micro level (II), spatially 3D model of porous catalytic washcoat (thickness approximate to 30 mu m) is used. Here the reconstruction is based on virtual packing of Pt/gamma-Al2O3 micro-parti
  • Mathematical models of reaction and transport in porous catalyst on three different scales (nano, micro, and macro) are presented. Methodology is demonstrated on CO oxidation in porous Pt/gamma-Al2O3 catalyst, washcoated on monolith. Morphological characteristics are obtained from TEM and SEM images of the washcoat cross-section. Methods for passing the model results from the bottom to the top level are discussed. On the nano level (I), spatially 3D model of a single meso-porous gamma-Al2O3 particle (approximate to 0.1-1 mu m) is used. Digital reconstruction of porous medium is here based on virtual agglomeration of Al2O3 nanoparticles and consequent deposition of individual Pt crystallites. The model considers the effects of catalytic sites sizes and diffusion in small meso-pores (d approximate to 10 nm). On the micro level (II), spatially 3D model of porous catalytic washcoat (thickness approximate to 30 mu m) is used. Here the reconstruction is based on virtual packing of Pt/gamma-Al2O3 micro-parti (en)
Title
  • Multi-scale modelling of reaction and transport in porous catalysts
  • Multi-scale modelling of reaction and transport in porous catalysts (en)
skos:prefLabel
  • Multi-scale modelling of reaction and transport in porous catalysts
  • Multi-scale modelling of reaction and transport in porous catalysts (en)
skos:notation
  • RIV/60461373:22340/10:00023272!RIV11-GA0-22340___
http://linked.open...avai/riv/aktivita
http://linked.open...avai/riv/aktivity
  • P(GP104/06/P301), S, Z(MSM6046137306)
http://linked.open...iv/cisloPeriodika
  • 1
http://linked.open...vai/riv/dodaniDat
http://linked.open...aciTvurceVysledku
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http://linked.open...iv/duvernostUdaju
http://linked.open...titaPredkladatele
http://linked.open...dnocenehoVysledku
  • 273198
http://linked.open...ai/riv/idVysledku
  • RIV/60461373:22340/10:00023272
http://linked.open...riv/jazykVysledku
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  • Mathematical modelling; Porous structure; Effective diffusion; Knudsen diffusion; Molecular dynamics; Pore size distribution (en)
http://linked.open.../riv/klicoveSlovo
http://linked.open...odStatuVydavatele
  • NL - Nizozemsko
http://linked.open...ontrolniKodProRIV
  • [95AA8042513F]
http://linked.open...i/riv/nazevZdroje
  • Chemical Engineering Science
http://linked.open...in/vavai/riv/obor
http://linked.open...ichTvurcuVysledku
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http://linked.open...vavai/riv/projekt
http://linked.open...UplatneniVysledku
http://linked.open...v/svazekPeriodika
  • 65
http://linked.open...iv/tvurceVysledku
  • Kočí, Petr
  • Štěpánek, František
  • Kubíček, Milan
  • Marek, Miloš
  • Novák, Vladimír
http://linked.open...ain/vavai/riv/wos
  • 000276206700062
http://linked.open...n/vavai/riv/zamer
issn
  • 0009-2509
number of pages
http://localhost/t...ganizacniJednotka
  • 22340
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