Combustion of methane over a PdAl2O3SiO2 catalyst, catalyst activity and stability

Abstract Palladium supported on Si-stabilised alumina has been demonstrated to be an active and durable catalyst for the combustion of methane. Si is more effective in stabilising alumina than La or Ba when the elements are added through an impregnation technique. Multiple stabilisation with combinations of La, Ba and Si does not increase further the stability against sintering. The stability increases logarithmically with the amount of Si added (0.5–8 atomic%). The rate of sintering is not affected by an increase of the water vapour content of the atmosphere from 1 to 20 vol.%. Doping palladium with rhodium or platinum increases the activity of the catalyst for methane combustion. The high-temperature stability of pure Pd is however superior to the stabilities of the Rh- and Pt-doped catalysts. Addition of La or Ce to the Pd-catalyst increases its stability against thermal deactivation but leads to an overall decrease in activity. The activity of the as-prepared catalysts are affected by the Pd-content below a value corresponding to 5% of the monolayer capacity. Thermally deactivated catalysts show a stronger activity dependence of the Pd-content than asprepared catalysts. The combustion reaction is first order with respect to methane and zero-order with respect to oxygen (>2 vol.% of oxygen). Carbon dioxide has no inhibitory effects on the combustion. The activity of the Pd-catalyst is decreased by a factor of 5 through deactivation at 1473 K for 768 h. The decrease in activity is linearly correlated to the decrease in specific surface area.

[1]  R. Farrauto,et al.  REVERSIBLE POISONING OF PALLADIUM CATALYSTS FOR METHANE OXIDATION , 1991 .

[2]  E. Garbowski,et al.  Stabilization of alumina toward thermal sintering by silicon addition , 1991 .

[3]  J. Barbier,et al.  Propane and propene oxidation over platinum and palladium on alumina: Effects of chloride and water , 1994 .

[4]  F. Oudet,et al.  Thermal stabilization of transition alumina by structural coherence with LnAlO3 (Ln = La, Pr, Nd) , 1988 .

[5]  A. Kato,et al.  Lanthanide B-Alumina Supports for Catalytic Combustion Above 1000°C , 1989 .

[6]  S. Matsuda,et al.  Preparation of Larnthanum β-Alumina with High Surface Area by Coprecipitation , 1987 .

[7]  Patrick Briot,et al.  Effect of particle size on the reactivity of oxygen-adsorbed platinum supported on alumina , 1990 .

[8]  Francisco J. Urbano,et al.  Methane combustion over palladium catalysts: The effect of carbon dioxide and water on activity , 1995 .

[9]  J. Church,et al.  Stabilisation of aluminas by rare earth and alkaline earth ions , 1993 .

[10]  H. Schaper,et al.  The influence of lanthanum oxide on the thermal stability of gamma alumina catalyst supports , 1983 .

[11]  Luis Javier Hoyos,et al.  Catalytic combustion of methane over palladium supported on alumina and silica in presence of hydrogen sulfide , 1993 .

[12]  C. H. Bartholomew Sintering Kinetics of Supported Metals: Perspectives from a Generalized Power Law Approach , 1994 .

[13]  J. Mccarty Kinetics of PdO combustion catalysis , 1995 .

[14]  H. W. Zandbergen,et al.  Application of lanthanum to pseudo-boehmite and γ-Al2O3 , 1991 .

[15]  J. Butt,et al.  Activation, Deactivation, and Poisoning of Catalysts , 1988 .

[16]  H. Arai,et al.  Recent progress in high-temperature catalytic combustion , 1991 .

[17]  S. Järås,et al.  Catalytic Materials for High-Temperature Combustion , 1993 .