2014
DOI: 10.1007/978-1-4899-8071-7_13
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SCR Reactor Models for Flow-Through and Wall-Flow Converters

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Cited by 4 publications
(3 citation statements)
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“…The effective diffusion coefficient in the catalyst washcoat phase, Deff, is calculated using the mean transport pore model [23], which accounts for contributions from both bulk and Knudsen diffusion. The mean transport pore model was chosen over more complex models, such as the random pore model, to limit model complexity [14,[23][24][25].…”
Section: / 35mentioning
confidence: 99%
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“…The effective diffusion coefficient in the catalyst washcoat phase, Deff, is calculated using the mean transport pore model [23], which accounts for contributions from both bulk and Knudsen diffusion. The mean transport pore model was chosen over more complex models, such as the random pore model, to limit model complexity [14,[23][24][25].…”
Section: / 35mentioning
confidence: 99%
“…As previously mentioned, the bulk diffusion coefficients, Dbulk,i, for NH3, NO, NO2, and N2O were calculated using the expressions in Table 2 [21]. The Knudsen diffusion coefficient, DK,i, was calculated using equation 11 [23]:…”
Section: / 35mentioning
confidence: 99%
“…The diesel particulate filter (DPF) model simulates the filtration and pressure drop behavior as well as the thermal and catalytic regeneration of the filter. The model has been presented and validated in numerous previous publications. It solves the transient mass, momentum, species, and energy balances in the channels of after-treatment devices, accounting for the catalytic surface reactions. axisuite uses differential and algebraic equations for the heat and mass transfer in the converter and is equipped with intralayer washcoat discretization to account for the coupling between reaction and diffusion phenomena.…”
Section: Discussionmentioning
confidence: 99%