Spatiotemporal behavior of Pt/Rh/CeO2/BaO catalyst during lean–rich cycling

Abstract Experiments were conducted to determine the impact of key operating variables (ceria loading, space velocity, cycle time, and rich pulse intensity) on the oxygen storage and release process of a Pt/Rh/CeO 2 /BaO monolithic catalyst during periodic lean (oxygen)–rich (propylene) operation. The concentrations were measured by spatially-resolved capillary inlet mass spectrometry (SpaciMS), and the temperature profile was measured by coherent optical frequency domain reflectometry (c-OFDR), providing detailed insight into the spatio-temporal features of the reaction system. The experiments revealed that the addition of ceria increased the breakthrough time of the propylene during a lean-to-rich transition due to an increased oxidation rate. Hydrogen was formed in the upstream and was consumed in the downstream section of the catalyst by reaction with ceria. Increasing the space velocity increased the upstream hydrogen formation rate and decreased its downstream oxidation rate. Increasing the lean and rich durations (while keeping their duration ratio constant) increased the oxygen uptake but resulted in propylene breakthrough and decreased the solid temperature. Increasing the rich period (at a fixed rich feed and total cycle time) allowed the catalyst to release more oxygen. A comparison of the ceria-containing catalyst to one without ceria revealed a more efficient complete oxidation for the former, while a comparison of the periodic to stationary operation revealed that less than half the propylene was converted to CO 2 by the former.

[1]  Jae-Soon Choi,et al.  Sulfur impact on NOx storage, oxygen storage, and ammonia breakthrough during cyclic lean/rich operation of a commercial lean NOx trap , 2007 .

[2]  B. Johansson,et al.  Two-dimensional gas-phase temperature measurements using phosphor thermometry , 2007 .

[3]  F. Meunier,et al.  Steam reforming of model compounds and fast pyrolysis bio-oil on supported noble metal catalysts , 2005 .

[4]  M. Harold,et al.  Fast lean-rich cycling for enhanced NOx conversion on storage and reduction catalysts , 2014 .

[5]  J. Kašpar,et al.  A Temperature-Programmed and Transient Kinetic Study of CO2Activation and Methanation over CeO2Supported Noble Metals , 1997 .

[6]  W. Epling,et al.  Overview of the Fundamental Reactions and Degradation Mechanisms of NOx Storage/Reduction Catalysts , 2004 .

[7]  M. Twigg Rôles of catalytic oxidation in control of vehicle exhaust emissions , 2006 .

[8]  A. Trovarelli,et al.  Catalytic Properties of Ceria and CeO2-Containing Materials , 1996 .

[9]  G. Groppi,et al.  Surface temperature profiles in CH4 CPO over honeycomb supported Rh catalyst probed with in situ optical pyrometer , 2011 .

[10]  Lino Guzzella,et al.  Is oxygen storage in three-way catalysts an equilibrium controlled process? , 2009 .

[11]  Jae-Soon Choi,et al.  Spatially resolved in situ measurements of transient species breakthrough during cyclic, low-temperature regeneration of a monolithic Pt/K/Al2O3 NOx storage-reduction catalyst , 2005 .

[12]  Jeffrey A. Sell,et al.  Dynamic behavior of automotive catalysts. III: Transient enhancement of water-gas shift over rhodium , 1985 .

[13]  Jae-Soon Choi,et al.  Intra-channel evolution of carbon monoxide and its implication on the regeneration of a monolithic Pt/K/Al2O3 NOx storage-reduction catalyst , 2006 .

[14]  M. Harold,et al.  Elucidating NH3 formation during NOx reduction by CO on Pt–BaO/Al2O3 in excess water , 2012 .

[15]  R. Dictor A kinetic study of the water-gas shift reaction over Rh/Al2O3 catalysts , 1987 .

[16]  Dan Luss,et al.  Optical frequency domain reflectometry measurements of spatio-temporal temperature inside catalytic reactors: Applied to study wrong-way behavior , 2013 .

[17]  Hydrogen Generation and Coke Formation over a Diesel Oxidation Catalyst under Fuel Rich Conditions , 2011 .

[18]  V. Balakotaiah,et al.  Determination of kinetics and controlling regimes for H2 oxidation on Pt/Al2O3 monolithic catalyst using high space velocity experiments , 2011 .

[19]  John Li,et al.  NOx release characteristics of lean NOx traps during rich purges , 2003 .

[20]  H. C. Yao,et al.  Ceria in automotive exhaust catalysts: I. Oxygen storage , 1984 .

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

[22]  Raymond J. Gorte,et al.  Evidence for Oxidation of Ceria by CO2 , 2000 .

[23]  M. Hatano,et al.  Hydrogen from water by reduced cerium oxide , 1983 .

[24]  William S. Epling,et al.  The effect of exothermic reactions during regeneration on the NOX trapping efficiency of a NOX storage/reduction catalyst , 2006 .

[25]  Hyun-chul Lee,et al.  Water-gas shift reaction over supported Pt-CeOx catalysts , 2009 .

[26]  M. Skoglundh,et al.  A transient in situ infrared spectroscopy study on methane oxidation over supported Pt catalysts , 2014 .

[27]  Kenneth A. Williams,et al.  Spatial and temporal profiles in millisecond partial oxidation processes , 2006 .

[28]  N. W. Cant,et al.  Catalytic oxidation. II. Silica supported noble metals for the oxidation of ethylene and propylene , 1970 .

[29]  Michael P. Harold,et al.  NOX storage and reduction on a Pt/BaO/alumina monolithic storage catalyst , 2004 .

[30]  V. Balakotaiah,et al.  Crystallite-Scale Model for NOx Storage and Reduction on Pt/BaO/Al2O3: Pt Dispersion Effects on NOx Conversion and Ammonia Selectivity , 2012 .

[31]  Yung-Fang Yu Yao,et al.  Oxidation of Alkanes over Noble Metal Catalysts , 1980 .

[32]  Todd J. Toops,et al.  Effect of Ceria on the Sulfation and Desulfation Characteristics of a Model Lean NOx Trap Catalyst , 2009 .

[33]  Karthik Ramanathan,et al.  Kinetic Parameters Estimation for Three Way Catalyst Modeling , 2011 .

[34]  Yi Liu,et al.  Spatio-temporal features of periodic oxidation of H2 and CO on Pt/CeO2/Al2O3 , 2011 .

[35]  D. Duprez,et al.  Hydrogen formation in propane oxidation on Pt-Rh/CeO2/Al2O3 catalysts , 1992 .

[36]  R. Gorte Ceria in catalysis: From automotive applications to the water–gas shift reaction , 2010 .

[37]  S. Pennycook,et al.  Interactions of Hydrogen with CeO2 , 2001 .

[38]  James C. Schlatter,et al.  Three-Way Catalyst Response to Transients , 1980 .

[39]  W. Epling,et al.  Effects of different regeneration timing protocols on the performance of a model NOX storage/reduction catalyst , 2010 .

[40]  Grigorios C. Koltsakis,et al.  Modeling dynamic phenomena in 3-way catalytic converters , 1999 .

[41]  The Effect of Ceria Content on the Performance of a NOx Trap , 2003 .

[42]  J. Herrmann,et al.  Influence of the reduction/evacuation conditions on the rate of hydrogen spillover on Rh/CeO2 catalysts , 1994 .

[43]  M. Harold,et al.  NOx Storage and Reduction with H2 on Pt/Rh/BaO/CeO2: Effects of Rh and CeO2 in the Absence and Presence of CO2 and H2O , 2011 .

[44]  M. Hatanaka,et al.  Ideal Pt loading for a Pt/CeO2-based catalyst stabilized by a Pt–O–Ce bond , 2010 .

[45]  B. Andersson,et al.  Oxygen Storage Dynamics in Pt/CeO2/Al2O3Catalysts☆ , 1998 .