Modelling transport phenomena and chemical reactions in automotive three-way catalytic converters

This study concentrates on the external and internal mass transfer with multiple reactions in the catalytic layer of a three-way catalyst (TWC). A single channel model accounting for the species diffusion inside the washcoat using the effectiveness factor was developed. Validation and calibration of the model was achieved by comparing predictions against experimental data obtained previously by the same authors. The model was then applied to study the importance of both turbulent monolith structures and controlled washcoat structures on TWC conversions. The numerical results show that: (i) increasing the transport coefficients using turbulent monolith structures can produce either positive or negative effects on the TWC conversions; (ii) overall, the net effect of increasing the transport coefficients on the TWC conversions is positive; (iii) at high inlet gas temperatures and high space velocities the turbulent monolith structures present important improvements in the TWC conversions; (iv) the TWC conversions can be significantly improved enhancing the transport properties of the porous washcoat structure; (v) enhancements in the transport properties of the washcoat structure have deeper impacts on the TWC conversions than improvements in the monolith channel structure.

[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 .