Adsorption and reactivity of NO on copper-on-alumina catalysts. I. Formation of nitrate species and their influence on reactivity in NO and NH{sub 3} conversion
- Univ. of Bologna (Italy)
- Univ. of Turin (Italy)
The reactivity of copper-on-alumina catalysts in the reduction of NO by NH{sub 3} + O{sub 2} (SCR reaction) and oxidation of NH{sub 3} to N{sub 2} (NH{sub 3}ox reaction) as a function of the copper loading shows that (i) the specific rate of the SCR reaction per mole of copper decreases with increasing copper loading, whereas the NH{sub 3}ox reaction rate is nearly independent of the copper loading and (ii) the rate of the NH{sub 3}ox reaction is significantly higher in the absence of NO than that of the same reaction occurring during the SCR reaction. The catalysts were characterized by electron spin resonance (ESR), X-ray diffraction analysis, and UV-visible diffuse reflectance. The nature of the NO and NH{sub 3} adsorbed species was studied using ESR and infrared (IR) spectroscopies, and IR studies of the reactive coadsorption of NO and NH{sub 3} were carried out. The results obtained indicate that the above catalytic effects are due to the formation of nitrate species which block the reactivity of copper sites. The transformation of NO to N{sub 2} via the intermediate formation of ammonium nitrate was shown, but the data suggest that this is only a secondary pathway of reaction responsible for the formation of N{sub 2}O as a byproduct. The nature of active copper species on the surface and the presence of competitive pathways of transformation of NO to N{sub 2} are also discussed.
- OSTI ID:
- 525931
- Journal Information:
- Journal of Catalysis, Vol. 152, Issue 1; Other Information: PBD: Mar 1995
- Country of Publication:
- United States
- Language:
- English
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Related Subjects
20 FOSSIL-FUELED POWER PLANTS
40 CHEMISTRY
NITRIC OXIDE
ADSORPTION
SELECTIVE CATALYTIC REDUCTION
COPPER
SORPTIVE PROPERTIES
CATALYTIC EFFECTS
ALUMINIUM OXIDES
CHEMICAL REACTION KINETICS
ELECTRON SPIN RESONANCE
X-RAY DIFFRACTION
REACTION INTERMEDIATES
HETEROGENEOUS CATALYSIS
AMMONIA