Modelling transport phenomena and chemical reactions in automotive three-way catalytic converters
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[1] A. Holmgren. Enhanced Mass Transfer in Monolith Catalysts with Bumps on the Channel Walls , 1999 .
[2] R. Hayes,et al. A fast approximation method for computing effectiveness factors with non-linear kinetics , 2007 .
[3] Pio Forzatti,et al. A comparison of lumped and distributed models of monolith catalytic combustors , 1995 .
[4] B. Su,et al. Insights into hierarchically meso–macroporous structured materials , 2006 .
[5] R. Hayes,et al. Calculating effectiveness factors in non-uniform washcoat shapes , 2005 .
[6] Grigorios C. Koltsakis,et al. Oxygen Storage Modeling in Three-Way Catalytic Converters , 2002 .
[7] Petr Kočí,et al. Meso-scale modelling of CO oxidation in digitally reconstructed porous Pt/γ-Al2O3 catalyst , 2006 .
[8] R. Hayes,et al. A New Technique to Measure the Effective Diffusivity in a Catalytic Monolith Washcoat , 2004 .
[9] J. Blanco,et al. New TiO2 monolithic supports based on the improvement of the porosity , 2005 .
[10] Katherine W. Hughes,et al. Three-Way-Catalyst Modeling - A Comparison of 1D and 2D simulations , 2007 .
[11] Rutherford Aris,et al. On the effects of radiative heat transfer in monoliths , 1977 .
[12] G. Rosen. The mathematical theory of diffusion and reaction in permeable catalysts , 1976 .
[13] Kyriacos Zygourakis,et al. Transient operation of monolith catalytic converters: a two-dimensional reactor model and the effects of radially nonuniform flow distributions , 1989 .
[14] S. Järås,et al. Numerical analysis of the transient performance of high-temperature monolith catalytic combustors: Effect of catalyst porosity , 1995 .
[15] R. Hayes,et al. Evaluating the effective diffusivity of methane in the washcoat of a honeycomb monolith , 2000 .
[16] M. Marek,et al. Effective diffusivities and pore-transport characteristics of washcoated ceramic monolith for automotive catalytic converter , 2006 .
[17] P. Gilot,et al. Modelling of the behaviour of a three way catalytic converter at steady state Influence of the propene diffusion inside the catalytic layer , 2000 .
[18] R. Aris,et al. Multiple oxidation reactions and diffusion in the catalytic layer of monolith reactors , 1983 .
[19] Dennis N. Assanis,et al. One-dimensional automotive catalyst modeling , 2005 .
[20] Mário Costa,et al. Evaluation of the conversion efficiency of ceramic and metallic three way catalytic converters , 2008 .
[21] Laxminarayan L. Raja,et al. A critical evaluation of Navier–Stokes, boundary-layer, and plug-flow models of the flow and chemistry in a catalytic-combustion monolith , 2000 .
[22] Louise Olsson,et al. Kinetic Modelling in Automotive Catalysis , 2004 .
[23] J. K. Hochmuth,et al. A discussion on transport phenomena and three-way kinetics of monolithic converters , 2006 .
[24] Karthik Ramanathan,et al. Light-off criterion and transient analysis of catalytic monoliths , 2003 .
[25] Martin Votsmeier,et al. Wall-flow filters with wall-integrated oxidation catalyst: A simulation study , 2007 .
[26] D. Papadias,et al. Simplified method of effectiveness factor calculations for irregular geometries of washcoats , 2000 .
[27] Robert E. Hayes,et al. Diffusion limitation effects in the washcoat of a catalytic monolith reactor , 1996 .
[28] S. Kolaczkowski. Measurement of effective diffusivity in catalyst-coated monoliths , 2003 .
[29] W. Tao,et al. Experimental Study on Effect of Interwall Tube Cylinder on Heat/Mass Transfer Characteristics of Corrugated Plate Fin-and-Tube Exchanger Configuration , 1992 .
[30] Gbmm Guy Marin,et al. Competing reactions in three-way catalytic converters : modelling of the NOx conversion maximum in the light-off curves under net oxidising conditions , 2000 .
[31] Clemens Brinkmeier,et al. Automotive three way exhaust aftertreatment under transient conditions : measurements, modeling and simulation , 2006 .
[32] Mario Montes,et al. Monolithic reactors for environmental applications: A review on preparation technologies , 2005 .
[33] Geoffrey Cunningham,et al. The development of a two-dimensional transient catalyst model for direct injection two-stroke applications , 2001 .
[34] Roland Wanker,et al. A fully distributed model for the simulation of a catalytic combustor , 2000 .
[35] Klaus Müller-Haas,et al. Innovative Metallic Substrates for Exhaust Emission Challenges for Gasoline and Diesel Engines , 2005 .
[36] S. E. Voltz,et al. Kinetic Study of Carbon Monoxide and Propylene Oxidation on Platinum Catalysts , 1973 .
[37] Daniel Schweich,et al. Three-way monolithic converter: Simulations versus experiments , 1996 .
[38] Petr Kočí,et al. Catalytic Converters for Automobile Diesel Engines with Adsorption of Hydrocarbons on Zeolites , 2005 .
[39] Mário Costa,et al. The relative importance of external and internal transport phenomena in three way catalysts , 2008 .
[40] V. Balakotaiah,et al. Shape normalization and analysis of the mass transfer controlled regime in catalytic monoliths , 2002 .
[41] Petr Kočí,et al. Modeling of Three-Way-Catalyst Monolith Converters with Microkinetics and Diffusion in the Washcoat , 2004 .
[42] Γεώργιος Σ. Κωνσταντάς. Development and application of a computer aided engineering methodology supporting the design optimization of automotive exhaust treatment systems , 2006 .