Current use of the supported V
2O
5-WO
3/TiO
2 catalyst for the selective catalytic reduction (SCR) of NO
x with NH
3 is extensive. Improved low temperature NO conversion is critical to mitigate N
2O generation at currently used high temperatures (T>300°C) and to improve performance under âcold startâ conditions. These problems can seemingly be overcome by the integration of redox promoters such as Ce and Cu. Furthermore, the effect of SO
2 typically found in industrial flue gas on the structure-performance relations of the catalysts is still poorly understood. In the present work,
in situ Raman and IR spectroscopies are used to investigate the anchoring, interactions, surface structures and acidity of the metal oxide surface sites. The effects of CeO
x, CuO
x and SO
x surface sites on the SCR performance of the catalysts is measured using temperature programmed surface reaction (TPSR) spectroscopy. The results indicate that the redox promoters are fully dispersed on the TiO
2 support and create unique surface hydroxyls that serve as the primary anchoring sites for the surface VO
x sites. Both the redox promoters and the surface sulfates affect the surface acidity, with the basic redox and acidic sulfate surface sites strengthening the Lewis and Brønsted acid characters of the catalysts, respectively. Both redox promoters enhanced the low temperature NO conversion activity of the catalyst, but only the CeO
x promoted catalyst exhibited lower N
2O generation. While the unpromoted catalyst remained unaffected by sulfation, the NO conversion activity of the redox promoted catalysts was inhibited. Finally, it was found that the SCR reaction can efficiently proceed via both Lewis and Brønsted acid sites, resolving the long-lived debate regarding the superior role of one acid site over another. These results serve to establish currently missing fundamental structure-performance relations for the interactions between CeO
x, CuO
x and SO
x surface sites and the
V
2O
5-WO
3/TiO
2 catalytic system.
