In catalytic oxidation reactions, the presence of environmental
water poses challenges to the performance of Pt catalysts. This study
aims to overcome this challenge by introducing hydroxyl groups onto
the surface of Pt catalysts using the pyrolysis reduction method.
Two silica supports were employed to investigate the impact of hydroxyl
groups: SiO2–OH with hydroxyl groups and SiO2–C without hydroxyl groups. Structural characterization
confirmed the presence of Pt–O
x
, Pt–OH
x
, and Pt0 species
in the Pt/SiO2–OH catalysts, while only Pt–O
x
and Pt0 species were observed in
the Pt/SiO2–C catalysts. Catalytic performance tests
demonstrated the remarkable capacity of the 0.5 wt % Pt/SiO2–OH catalyst, achieving complete conversion of benzene at
160 °C under a high space velocity of 60,000 h–1. Notably, the catalytic oxidation capacity of the Pt/SiO2–OH catalyst remained largely unaffected even in the presence
of 10 vol % water vapor. Moreover, the catalyst exhibited exceptional
recyclability and stability, maintaining its performance over 16 repeated
cycles and a continuous operation time of 70 h. Theoretical calculations
revealed that the construction of Pt–OH
x
sites on the catalyst surface was beneficial for modulating
the d-band structure, which in turn enhanced the adsorption and activation
of reactants. This finding highlights the efficacy of decorating the
Pt surface with hydroxyl groups as an effective strategy for improving
the water resistance, catalytic activity, and long-term stability
of Pt catalysts.