Combined Effect of H2O and SO2 on V2O5/AC Catalysts for NO Reduction with Ammonia at Lower Temperatures

Abstract Combined effect of H 2 O and SO 2 on V 2 O 5 /AC the activity of catalyst for selective catalytic reduction (SCR) of NO with NH 3 at lower temperatures was studied. In the absence of SO 2 , H 2 O inhibits the catalytic activity, which may be attributed to competitive adsorption of H 2 O and reactants (NO and/or NH 3 ). Although SO 2 promotes the SCR activity of the V 2 O 5 /AC catalyst in the absence of H 2 O, it speeds the deactivation of the catalyst in the presence of H 2 O. The dual effect of SO 2 is attributed to the SO 4 2− formed on the catalyst surface, which stays as ammonium-sulfate salts on the catalyst surface. In the absence of H 2 O, a small amount of ammonium-sulfate salts deposits on the surface of the catalyst, which promote the SCR activity; in the presence of H 2 O, however, the deposition rate of ammonium-sulfate salts is much greater, which results in blocking of the catalyst pores and deactivates the catalyst. Decreasing V 2 O 5 loading decreases the deactivation rate of the catalyst. The catalyst can be used stably at a space velocity of 9000 h −1 and temperature of 250 °C.

[1]  R. T. Yang,et al.  Selective Catalytic Reduction of Nitrogen Oxides by Ammonia over Fe3+-Exchanged TiO2-Pillared Clay Catalysts , 1999 .

[2]  K. Nobe,et al.  Parametric and Durability Studies of NOx Reduction with NH3 on V2O5 Catalysts , 1978 .

[3]  L. Kiwi-Minsker,et al.  Fibrous structured catalytic beds for three-phase reaction engineering , 2000 .

[4]  P. Nelson,et al.  Isotopic labeling studies of the effects of temperature, water, and vanadia loading on the selective catalytic reduction of NO with NH3 over Vanadia-Titania catalysts , 1994 .

[5]  W. Grünert,et al.  Activity, selectivity and durability of VO–ZSM-5 catalysts for the selective catalytic reduction of NO by ammonia , 1999 .

[6]  W. S. Kijlstra,et al.  Deactivation by SO2 of MnOx/Al2O3 catalysts used for the selective catalytic reduction of NO with NH3 at low temperatures , 1998 .

[7]  P. Ciambelli,et al.  Effect of water on the kinetics of nitric oxide reduction over a high-surface-area V2O5/TiO2 catalyst , 1994 .

[8]  A. Bliek,et al.  Inhibiting and deactivating effects of water on the selective catalytic reduction of Nitric Oxide with ammonia over MnOx/Al2O3 , 1996 .

[9]  H. Ohara,et al.  SO2 oxidation over the V2O5/TiO2 SCR catalyst , 2001 .

[10]  E. Tronconi,et al.  Oxidation of sulfur dioxide to sulfur trioxide over honeycomb DeNoxing catalysts , 1993 .

[11]  N. Yamazoe,et al.  Effects of coexisting gases on the catalytic reduction of NO with NH3 over Cu(II) NaY , 1979 .

[12]  Zhenyu Liu,et al.  A novel carbon-supported vanadium oxide catalyst for NO reduction with NH3 at low temperatures , 1999 .

[13]  Zhenyu Liu,et al.  Promoting Effect of SO2 on Activated Carbon-Supported Vanadia Catalyst for NO Reduction by NH3 at Low Temperatures , 1999 .

[14]  G. Marbán,et al.  Low temperature selective catalytic reduction of NO over modified activated carbon fibres , 2000 .

[15]  P. Forzatti Environmental catalysis for stationary applications , 2000 .

[16]  Zhenyu Liu,et al.  Mechanism of SO2 promotion for NO reduction with NH3 over activated carbon-supported vanadium oxide catalyst , 2001 .

[17]  R. T. Yang,et al.  Superior Fe-ZSM-5 catalyst for selective catalytic reduction of nitric oxide by ammonia , 1999 .

[18]  G. Busca,et al.  Selective reduction of NO with NH3 on a new iron-vanadyl phosphate catalyst , 2000 .

[19]  G. Deo,et al.  Reactivity of V2O5Catalysts for the Selective Catalytic Reduction of NO by NH3: Influence of Vanadia Loading, H2O, and SO2 , 1996 .

[20]  TakahashiKazumasa,et al.  IMPROVEMENT OF V2O5–TiO2 CATALYST FOR NOx REDUCTION WITH NH3 IN FLUE GASES , 1981 .

[21]  Zhenyu Liu,et al.  Decomposition and Reactivity of NH4HSO4 on V2O5/AC Catalysts Used for NO Reduction with Ammonia , 2000 .

[22]  R. T. Yang,et al.  Selective catalytic reduction of NO with ammonia over V2O5 doped TiO2 pillared clay catalysts , 2000 .