An Investigation of the NO/H2/O2 (Lean-deNOx) Reaction on a Highly Active and Selective Pt/La0.5Ce0.5MnO3 Catalyst

The NO/H2/O2 reaction has been studied under lean-burn conditions in the 100–400°C range over 0.1 wt% Pt supported on La0.5Ce0.5MnO3 (mixed oxide containing LaMnO3, CeO2, and MnO2 phases). For a critical comparison, 0.1 wt% Pt was supported on γ-Al2O3 and tested under the same reaction conditions. The maximum in the NO conversion has been observed at 140°C (74% conversion) for the Pt/La0.5Ce0.5MnO3 and at 125°C (66% conversion) for the Pt/γ-Al2O3 catalyst using a GHSV of 80,000 h−1. Addition of 5% H2O in the feed stream influenced the performance of the catalyst in a positive way. In particular, it widened the operating temperature window of the catalyst above 200°C with appreciable NO conversion and had no negative effect on the stability of the catalyst for a 20-h run on reaction stream. Remarkable N2 selectivity values in the 80–90% range have been observed on the Pt/La0.5Ce0.5MnO3 catalyst in the 100–200°C range either in the absence or in the presence of water in the feed stream. This result is reported for the first time for the NO/H2/O2 lean-deNOx reaction at least on Pt-based catalysts. A maximum specific integral reaction rate of 397 μmol of N2/s.g of Pt metal was measured at 140°C during reaction with 0.25% NO/1% H2/5% O2/5% H2O/He gas mixture on the 0.1 wt% Pt/La0.5Ce0.5MnO3 catalyst. This value was found to be higher by 40% than that observed on the 0.1 wt% Pt/γ-Al2O3 catalyst at 125°C, and it is the highest value ever reported in the 100–200°C range. A TOF value of 0.49 s−1 was calculated at 140°C for the Pt/La0.5Ce0.5MnO3 catalyst. Temperature-programmed desorption (TPD) of NO and transient titration experiments of the catalyst surface following reaction have revealed important information concerning several mechanistic steps of the present catalytic system. A hydrogen-assisted NO dissociation step and a nitrogen-assisted mechanism for N2 and N2O formation are proposed to explain all the transient experiments performed in a satisfactory manner.

[1]  K. Eguchi,et al.  Sorption of nitrogen oxides on MnOy-ZrO2 and Pt-ZrO2-Al2O3 , 1998 .

[2]  S. Sciré,et al.  An investigation of the mechanism of the selective catalytic reduction of NO on various metal/ZSM-5 catalysts: reactions of H2/NO mixtures , 1994 .

[3]  G. Busca,et al.  Infrared study of the adsorption of nitrogen dioxide, nitric oxide and nitrous oxide on hematite , 1981 .

[4]  M. Vannice,et al.  NO Reduction with H2or CO over La2O3and Sr-Promoted La2O3 , 1998 .

[5]  K. Eguchi,et al.  Reversible Sorption of Nitrogen Oxides in Mn–Zr Oxide , 1996 .

[6]  T. P. Kobylinski,et al.  The catalytic chemistry of nitric oxide , 1974 .

[7]  D. Ferri,et al.  NO reduction by H2 over perovskite-like mixed oxides , 1998 .

[8]  C. Costa,et al.  The Selective Catalytic Reduction of Nitric Oxide with Methane over La2O3–CaO Systems: Synergistic Effects and Surface Reactivity Studies of NO, CH4, O2, and CO2 by Transient Techniques , 2000 .

[9]  M. A. Vannice,et al.  NO adsorption and decomposition on La2O3 studied by DRIFTS , 1999 .

[10]  G. Ertl,et al.  Handbook of Heterogeneous Catalysis , 1997 .

[11]  G. Emig,et al.  Kinetics and mechanism of the reduction of nitric oxides by H2 under lean-burn conditions on a Pt–Mo–Co/α-Al2O3 catalyst , 1998 .

[12]  A. Shestov,et al.  A Transient Kinetic Study of the Mechanism of the NO+H2 Reaction over Pt/SiO2 Catalysts: 1. Isotopic Transient Kinetics and Temperature Programmed Analysis , 1999 .

[13]  A. Ueda,et al.  Two conversion maxima at 373 and 573K in the reduction of nitrogen monoxide with hydrogen over Pd/TiO2 catalyst , 1998 .

[14]  F. Solymosi,et al.  Effect of NO on the CO-induced disruption of rhodium crystallites , 1988 .

[15]  K. Tomishige,et al.  Observation of Molecular Reaction Intermediate and Reaction Mechanism for NO Dissociation and No-H2 Reaction on Rh-Sn/SiO2 Catalysts , 1995 .

[16]  T. Shido,et al.  Highly Selective Catalytic Reduction of NO by H2over Au0and Au(I) Impregnated in NaY Zeolite Catalysts , 1996 .

[17]  H. Arai,et al.  An infrared study of nitric oxide adsorbed on rhodium-alumina catalyst , 1976 .

[18]  Bernard Delmon,et al.  Catalytic removal of NO , 1998 .

[19]  R. Burch,et al.  A Transient Kinetic Study of the Mechanism of the NO/C3H6/O2Reaction over Pt–SiO2Catalysts: Part I: Non-Steady-State Transient Switching Experiments , 1999 .

[20]  G. Somorjai,et al.  AES and TDS study of the adsorption of NH3 and NO on V2O5 and TiO2 surfaces: Mechanistic implications , 1989 .

[21]  A. Schmid,et al.  Investigation of the NO+H2 reaction on Pt{100} with low-energy electron microscopy , 1998 .

[22]  Guido Busca,et al.  Chemical and mechanistic aspects of the selective catalytic reduction of NOx by ammonia over oxide catalysts: A review , 1998 .

[23]  Alexis T. Bell,et al.  Decomposition and reduction of NO on transition metal surfaces: bond order conservation Morse potential analysis , 1993 .

[24]  R. Burch An investigation of the NO/H2/O2 reaction on noble-metal catalysts at low temperatures under lean-burn conditions , 1999 .

[25]  A. Kiennemann,et al.  Absorption/desorption of NOx process on perovskites: performances to remove NOx from a lean exhaust gas , 2000 .

[26]  H. Knözinger,et al.  Infrared study on the interaction of CO with alumina-supported rhodium , 1990 .

[27]  V. Pitchon,et al.  The current state of research on automotive lean NOx catalysis , 1997 .