Developing sulfur tolerance catalyst for combustion of volatile organic compounds (VOCs) is of great significance in the removal of industrial waste gas. In this work, the roles of support over Pd-based catalyst for the sulfur tolerance during toluene oxidation were investigated by loading 0.5 wt% Pd onto CeO2, Al2O3, TiO2, and SiO2 with or without SO2 pretreatment. Results showed that the Pd/CeO2 displays an attractive toluene conversion of 90% at 220 °C, outperforming other supported Pd catalysts, especially the Pd/TiO2 catalyst (with a T90 of 253 °C). However, after SO2 pretreatment, the toluene oxidation performance of Pd/TiO2 ranked first, and its T90 was 38 °C lower than that of Pd/CeO2. Characterization results indicated that the Pd0 active species on the CeO2 surface is highly prone to reacts with SO2 to form stable Ce2(SO4)3 deposition. Additionally, the decrease in activated oxygen capacity inhibits its redox performance. These factors collectively result in poor sulfur resistance of Pd/CeO2. While the outstanding sulfur resistance of Pd/TiO2 was closely linked to the ready decomposition of sulfates on its surface. This work elucidates the critical role of the support in dictating catalytic performance and anti-poisoning capability, thereby offering new perspectives for the design of high-performance Pd-based catalysts for VOC remediation.




