A comparison of the activity and deactivation of Ag/Al2O3 and Cu/ZSM-5 for HC-SCR under simulated diesel exhaust emission conditions

The performances of two model HC-SCR catalysts, 5% Cu/ZSM-5 (Si/Al ratio of 30) and 2% Ag/Al2O3, are compared and contrasted under a variety of different operating conditions. We have examined the activity of these catalysts by using a wide range of hydrocarbons. The activity of the Cu/ZSM-5 catalyst is not significantly affected by the nature of the hydrocarbon species, whereas the Ag catalyst shows a strong dependence. The Ag catalyst displays poorer low-temperature activity with propene than with longer chain hydrocarbons, such as decane. The use of diesel fuel with the Ag catalyst induces deactivation at lower temperatures, because of coke deposition. The Ag catalyst is strongly deactivated by sulphur. The Cu/ZSM-5 catalyst is much more resistant to chemical deactivation. The Ag/Al2O3 catalyst is capable of withstanding high-temperature ageing conditions, whereas the Cu/ZSM-5 catalyst is significantly deactivated after such ageing because of a combination of Cu sintering and zeolite dealumination.

[1]  H. Kung,et al.  Effect of Cu loading and addition of modifiers on the stability of Cu/ZSM-5 in lean NOx reduction catalysis , 1997 .

[2]  P. Gilot,et al.  A review of NOx reduction on zeolitic catalysts under diesel exhaust conditions , 1997 .

[3]  Junji Shibata,et al.  Promotion effect of H2 on the low temperature activity of the selective reduction of NO by light hydrocarbons over Ag/Al2O3 , 2003 .

[4]  M. Flytzani-Stephanopoulos,et al.  Hydrothermal stability of cerium modified Cu-ZSM-5 catalyst for nitric oxide decomposition , 1996 .

[5]  N. W. Cant,et al.  The mechanism of the selective reduction of nitrogen oxides by hydrocarbons on zeolite catalysts , 2000 .

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

[7]  F. Meunier,et al.  A review of the selective reduction of NOx, with hydrocarbons under lean-burn conditions with non-zeolitic oxide and platinum group metal catalysts , 2002 .

[8]  D. Murzin,et al.  Silver/Alumina Catalyst for Selective Catalytic Reduction of NOx to N2 by Hydrocarbons in Diesel Powered Vehicles , 2004 .

[9]  N. Kruse,et al.  Promotional effect of SO2 on the selective catalytic reduction of NOx with propane/propene over Ag/γ-Al2O3 , 2001 .

[10]  J. Ross,et al.  Effect of ex situ treatments with SO2 on the activity of a low loading silver–alumina catalyst for the selective reduction of NO and NO2 by propene , 2000 .

[11]  E. Basaldella,et al.  Effect of hydrothermal treatment on Cu-ZSM-5 catalyst in the selective reduction of NO , 1999 .

[12]  S. Satokawa,et al.  Influence of low concentration of SO2 for selective reduction of NO by C3H8 in lean-exhaust conditions on the activity of Ag/Al2O3 catalyst , 2001 .

[13]  A. Campero,et al.  Changes in Cu2+ environment upon wet deactivation of Cu-ZSM-5 deNOx catalysts , 2000 .

[14]  H. Kung,et al.  Deactivation of Cu/ZSM-5 Catalysts for Lean NOxReduction: Characterization of Changes of Cu State and Zeolite Support , 1996 .

[15]  J. Kašpar,et al.  Improvement of SOx-Resistance of Silver Lean-DeNOx Catalysts by Supporting on CeO2-Containing Zirconia , 2002 .

[16]  A. P. Walker Mechanistic studies of the selective reduction of NOx over Cu/ZSM-5 and related systems , 1995 .

[17]  Kazuyuki Ueda,et al.  Catalytic reduction system of NOx in exhaust gases from diesel engines with secondary fuel injection , 1998 .

[18]  N. Kruse,et al.  On the promotion by SO2 of the SCR process over Ag/Al2O3: influence of SO2 concentration with C3H6 versus C3H8 as reductant , 2002 .

[19]  M. Richter The effect of hydrogen on the selective catalytic reduction of NO in excess oxygen over Ag/Al2O3 , 2004 .

[20]  M. Shelef,et al.  Spectroscopic studies of the stability of zeolitic deNOx catalysts , 1997 .