Developing eco-friendly catalysts with high NOx removal efficiency and SO2 resistance in a wide temperature range is crucial. A series of efficient CeVO4/sulfated-SnO2 (CeV/Sn-S) and CeVO4/SnO2 (CeV/SnO2) catalysts were developed, and the optimal mass fraction of CeVO4 was 9 wt%. 9 %CeV/SnO2 and 9 %CeV/Sn-S achieved over 90.0 % NOx conversion at 220–385 and 240–430 °C, respectively, and they both showed notable SO2 resistance. CeV, 9 %CeV/SnO2 and 9 %CeV/Sn-S displayed different acid sites and SO2 adsorption capabilities. CeV exhibited low surface acidity, primarily Brønsted acidity. The introduction of SnO2 enhanced Lewis acidity, while sulfated SnO2 addition increased both Lewis and Brønsted acidity, and reduced SO2 adsorption, which benefited to the SO2 resistance. 9 %CeV/Sn-S had more lattice defects, a lager surface area, and higher Ce4+ and V5+ ratios than 9 %CeV/SnO2, indicating a stronger interaction between CeVO4 and sulfated SnO2. Then, 9 %CeV/Sn-S catalyst’s strong NH3 adsorption and moderate redox properties contributed to its higher NOx conversions and N2 selectivity above 330 °C, along with a broader operational window. Both Eley–Rideal (E-R) and Langmuir-Hinshelwood (L-H) mechanisms were observed in these catalysts. However, the presence of sulfates on 9 %CeV/Sn-S limited NOx adsorption, thereby reducing the contribution of L-H mechanism. The 9 %CeV/SnO2 catalyst’s strong Lewis acidity and abundant adsorbed NOx species favored the L-H mechanism, resulting in its higher NOx conversion below 250 °C compared to 9 %CeV/Sn-S. This work contributes to sharpening comprehension for the influence of acid sites and steering the design of novel SCR catalysts for efficient NOx abatement in practical applications.
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