DYNAMIC INVESTIGATION OF THE ROLE OF THE SURFACE SULFATES IN NOX REDUCTION AND SO2 OXIDATION OVER V2O5-WO3 TIO2 CATALYSTS/

Citation
C. Orsenigo et al., DYNAMIC INVESTIGATION OF THE ROLE OF THE SURFACE SULFATES IN NOX REDUCTION AND SO2 OXIDATION OVER V2O5-WO3 TIO2 CATALYSTS/, Industrial & engineering chemistry research, 37(6), 1998, pp. 2350-2359
Citations number
30
Categorie Soggetti
Engineering, Chemical
ISSN journal
08885885
Volume
37
Issue
6
Year of publication
1998
Pages
2350 - 2359
Database
ISI
SICI code
0888-5885(1998)37:6<2350:DIOTRO>2.0.ZU;2-P
Abstract
Transient experiments performed over synthesized and commercial V2O5-W O3/TiO2 catalysts during catalyst conditioning and during step changes of the operating variables (SO2 inlet concentration and temperature) show that conditioning of the catalyst is required to attain significa nt and reproducible steady-state data in both the reduction of NOx and the oxidation of SO2. The response time of conditioning for NOx reduc tion is of a few hours and that for SO2 oxidation is of several hours. Fourier transform infrared spectroscopy temperature programmed decomp osition, and thermogravimetric measurements showed that catalyst condi tioning is associated with a slow process of buildup of sulfates: the different characteristic conditioning times observed in the reduction of NOx and in the oxidation of SO2 suggest that the buildup of sulfate s occurs first at the vanadyl sites and later on at the exposed titani a surface. Formation of sulfates at or near the vanadyl sites increase s the reactivity in the de-NOx reaction, possibly due to the increase in the Bronsted and Lewis acidity of the catalyst, whereas the titania surface acts as SO3 acceptor and affects the outlet SO3 concentration during catalyst conditioning for the SO2 oxidation reaction. The resp onse time to step changes in SO2 concentration and temperature is of a few hours in the case of SO2 oxidation and much shorter in the case o f NOx reduction. The different time responses associated with conditio ning and with step changes in the settings of the operating variables have been rationalized in terms of the different extent of perturbatio n of the sulfate coverage experienced by the catalyst.