Detailed reaction kinetics for double-layered Pd/Rh bimetallic TWC monolith catalyst

Abstract Detailed intrinsic reaction kinetics for the double-layered Pd/Rh-based TWC has been developed by combining the reaction kinetics derived for the individual Pd- and Rh-based catalysts without any further adjustment of the kinetic parameters obtained from the reaction kinetics of each catalyst. A 2D non-isothermal monolith reactor model based upon the combined reaction kinetics developed well describes the general trend of the TWC performance of and the temperature distribution in the double-layered Pd/Rh and Rh/Pd monolith reactors under steady-state conditions, irrespective of the location of Pd and Rh layers in the double-layered TWC monolith, mainly due to the thin catalyst layers washcoated onto the channels of the monolith. The detailed reaction kinetics has been further validated by its capability of predicting the TWC performance of the commercial Rh/Pd double-layered monolith reactor.

[1]  Robert Walter McCabe,et al.  Automotive exhaust catalysis , 2003 .

[2]  Robert E. Hayes,et al.  Finite-element model for a catalytic monolith reactor , 1992 .

[3]  D. W. Goodman,et al.  Comparative kinetic studies of CO$z.sbnd;O2 and CO$z.sbnd;NO reactions over single crystal and supported rhodium catalysts , 1986 .

[4]  Sung Bong Kang,et al.  Activity Function for Describing Alteration of Three-Way Catalyst Performance over Palladium-Only Three-Way Catalysts by Catalyst Mileage , 2011 .

[5]  Gbmm Guy Marin,et al.  The effects of oscillatory feeding of CO and O2 on the performance of a monolithic catalytic converter of automobile exhaust gas: a modelling study , 1993 .

[6]  B. J. Yoon,et al.  Simulation of a Nonisothermal Modern Three-Way Catalyst Converter , 2010 .

[7]  D. Duprez,et al.  Effects of Pretreatments on the Surface Composition of Alumina-Supported Pd–Rh Catalysts , 2001 .

[8]  A. Martínez-Hernández,et al.  Effect of low-sulfur fuels upon NH3 and N2O emission during operation of commercial three-way catalytic converters , 2007 .

[9]  H. Yang,et al.  Mathematical modeling of monolith catalysts and reactors for gas phase reactions , 2008 .

[10]  K. Bischoff An extension of the general criterion for importance of pore diffusion with chemical reactions , 1967 .

[11]  Dennys E. Angove,et al.  Nitrous oxide formation during the reaction of simulated exhaust streams over rhodium, platinum and palladium catalysts , 1998 .

[12]  B. Cho Mechanistic importance of intermediate N2O + CO reaction in overall NO + CO reaction system. II: Further analysis and experimental observations , 1994 .

[13]  Kathleen C. Taylor,et al.  Selective reduction of nitric oxide over noble metals , 1980 .

[14]  R. Hayes,et al.  Evaluating the effective diffusivity of methane in the washcoat of a honeycomb monolith , 2000 .

[15]  D. Duprez,et al.  Selective steam reforming of aromatic hydrocarbons: IV. Steam conversion and hydroconversion of selected monoalkyl- and dialkyl-benzenes on Rh catalysts , 1984 .

[16]  D. Trimm,et al.  The effect of steam and hydrogen in promoting the oxidation of carbon monoxide over a platinum on alumina catalyst , 2007 .

[17]  Mário Costa,et al.  Modelling transport phenomena and chemical reactions in automotive three-way catalytic converters , 2009 .

[18]  Young Sun Mok,et al.  Modeling of monolith reactor washcoated with CuZSM5 catalyst for removing NO from diesel engine by urea , 2006 .

[19]  S. E. Voltz,et al.  Kinetic Study of Carbon Monoxide and Propylene Oxidation on Platinum Catalysts , 1973 .

[20]  Daniel Schweich,et al.  Three-way monolithic converter: Simulations versus experiments , 1996 .

[21]  Robert E. Hayes,et al.  MASS AND HEAT TRANSFER EFFECTS IN CATALYTIC MONOLITH REACTORS , 1994 .

[22]  H. Bart,et al.  Kinetic study of three-way catalyst of automotive exhaust gas: Modeling and application , 2009 .

[23]  T. Yamada,et al.  Effect of basic metal additives on NOx reduction property of Pd-based three-way catalyst , 2001 .

[24]  Iljeong Heo,et al.  The alteration of the performance of field-aged Pd-based TWCs towards CO and C3H6 oxidation , 2009 .

[25]  Sung Bong Kang,et al.  Activity function describing the effect of Pd loading on the catalytic performance of modern commercial TWC , 2012 .

[26]  A. M. Efstathiou,et al.  The effect of calcination temperature on the oxygen storage and release properties of CeO2 and Ce–Zr–O metal oxides modified by phosphorus incorporation , 2005 .

[27]  N. W. Cant,et al.  Steady-state oxidation of carbon monoxide over supported noble metals with particular reference to platinum , 1978 .

[28]  W. R. Williams,et al.  Steps in hydrogen oxidation on rhodium: hydroxyl desorption at high temperatures , 1993 .

[29]  B. Cho Mechanistic importance of intermediate N2O + CO reaction in overall NO + CO reaction system. I: Kinetic analysis , 1992 .

[30]  G. Djéga-Mariadassou,et al.  A new approach in the kinetic modelling of three-way catalytic reactions , 2004 .

[31]  R. Reid,et al.  The Properties of Gases and Liquids , 1977 .

[32]  Jc Jaap Schouten,et al.  Acetylene and carbon monoxide oxidation over a Pt/Rh/CeO2/γ-Al2O3 automotive exhaust gas catalyst: kinetic modelling of transient experiments , 2001 .

[33]  D. Duprez,et al.  Steam effects in three-way catalysis , 1994 .

[34]  D. Duprez,et al.  Oxygen storage capacity measurements of three-way catalysts under transient conditions , 2002 .

[35]  R. Hayes,et al.  Three-way catalytic converter modelling with detailed kinetics and washcoat diffusion , 2004 .

[36]  S. Oh,et al.  Enhancement effect of water on oxidation reactions over commercial three-way catalyst , 2008 .

[37]  A. Sarkar,et al.  CO oxidation and NO reduction over supported Pt-Rh and Pd-Rh nanocatalysts: a comparative study , 2005 .

[38]  James C. Cavendish,et al.  Transients of monolithic catalytic converters. Response to step changes in feedstream temperature as related to controlling automobile emissions , 1982 .

[39]  Koji Yokota,et al.  Nitric oxide reduction performance of automotive palladium catalysts , 1989 .

[40]  Hyuk Jae Kwon,et al.  Detailed reaction kinetics over commercial three-way catalysts , 2007 .

[41]  Gbmm Guy Marin,et al.  Development of a transient kinetic model for the CO oxidation by O2 over a Pt/Rh/CeO2/γ-Al2O3 three-way catalyst , 1998 .

[42]  Freek Kapteijn,et al.  New non-traditional multiphase catalytic reactors based on monolithic structures , 2001 .

[43]  P. Ciambelli,et al.  The effect of sulphation on the catalytic activity of CoOx/ZrO2 for NO reduction with NH3 in the presence of O2 , 2009 .

[44]  M. Skoglundh,et al.  Screening of TiO2-Supported Catalysts for Selective NOx Reduction with Ammonia , 2004 .

[45]  Petr Kočí,et al.  Modeling of Three-Way-Catalyst Monolith Converters with Microkinetics and Diffusion in the Washcoat , 2004 .

[46]  J. Botas,et al.  Influence of water and hydrocarbon processed in feedstream on the three-way behaviour of platinum−alumina catalysts , 1997 .