3-D modeling of monolith reactors
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Cited by (46)
Dynamic modeling, simulation and optimization of the partially-autothermal reforming of biogas in coated monolith channels
2023, Chemical Engineering Journal AdvancesEffect of heat losses on monolithic reactors for VOC abatement
2019, Chemical Engineering JournalOptimization of a 3-D isothermal plug-flow model of a monolith reactor featuring first order reactions
2019, Chemical Engineering Research and DesignCitation Excerpt :Others focused on multiphase monolith reactor modeling, as did Kreutzer et al. (2005) who investigated two phase methane oxidation in microchannels, while Andersson et al. (1998) presented a three-phase flow model. In past years, Young and Finlayson (1974) quantified mass and heat transfer effects for fully developed flow in ducts, Heck et al. (1976), and Veser and Frauhammer (2000) presented 1-D monolith models, while Jahn et al. (1997) developed a 3-D model. Finally, Kolaczkowski (1999) discussed the challenges involved in monolith reactor design.
Numerical optimization of flow uniformity inside an under body- oval substrate to improve emissions of IC engines
2016, Journal of Computational Design and EngineeringTowards computationally-efficient modeling of transport phenomena in three-dimensional monolithic channels
2015, Applied Mathematics and ComputationA sensitivity study of the oxidation of compressed natural gas on platinum
2013, FuelCitation Excerpt :A range of catalysts are used in these processes ranging from the noble-metals such as platinum (Pt), palladium (Pd), and rhodium (Rh) to the less expensive transition metal oxides [1]. The catalytic monolith and packed-bed reactors enjoyed extensive research including both experiments and simulations [9–12] but models developed remain limited to relatively narrow range of operating conditions. An obvious but complex feature of catalytic surface oxidation is the presence of significant physical and chemical interactions at the solid–fluid interface.