Pt/TiO
2 and Pt-Eu
2O
3/TiO
2 catalysts were prepared via the impregnation method for catalytic oxidation of CO. The Pt-2Eu
2O
3/TiO
2 catalyst exhibited better CO oxidation activity as well as greater SO
2 resistance than the Pt/TiO
2 catalyst. For the inlet gas consisting of 0.8% CO, 5% O
2, and balanced N
2, the lowest complete conversion temperatures (
T100) of CO were 120 °C and 140 °C for the Pt-2Eu
2O
3/TiO
2 and Pt/TiO
2 catalysts, respectively. During the 72 h SO
2-resistance test at 200 °C under an inlet gas composition of 0.8% CO, 5% O
2, 15% H
2O, 50 ppm SO
2, and balanced N
2, the CO conversion on the Pt-2Eu
2O
3/TiO
2 catalyst remained >99%, while that on the Pt/TiO
2 catalyst gradually decreased to 77.8%. Pre-loading 2 wt% Eu
2O
3 on TiO
2 enhanced the dispersion of Pt, increased the proportion of Pt
0, and facilitated the adsorption and dissociation of H
2O, all of which promoted CO oxidation. SO
2 preferentially occupied the Eu
2O
3 sites by forming stable sulfates on the Pt-2Eu
2O
3/TiO
2 catalyst, which protected the Pt active sites from poisoning. The OH* species produced from the dissociation of H
2O played a significant role in promoting CO oxidation through the formation of COOH* as the key reaction intermediate. The developed Pt-2Eu
2O
3/TiO
2 catalyst has great application potential in terms of the removal of CO from industrial flue gases.
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