Abstract
The effects of catalyst physicochemical property and operation condition on toluene destruction over Pd/Z-x (Z: ZSM-5; x: nSi/Al) were extensively studied. The support acidity has important impact on active phase dispersion and reaction product desorption. Pd/Z-25 shows the highest catalytic activity with toluene complete conversion at 220 °C, which is about 60 °C lower than that of Pd/Z-300. Both Pd loading and space velocity are key experimental factors determining toluene oxidation activity. The water vapor has a significant negative effect on the oxidation reaction, especially for the catalyst with higher Al content. The activity of the used Pd/Z-25 could not regain its initial level after removal of water vapor due to the formation of coke. Pd0 and Pd2+ species have a synergetic effect on toluene oxidation, and the catalytic activity is primarily correlated to the support acidity, the active phase dispersion, and the CO2 desorption capability.
| Original language | English |
|---|---|
| Pages (from-to) | 551-563 |
| Number of pages | 13 |
| Journal | Journal of Porous Materials |
| Volume | 21 |
| Issue number | 5 |
| DOIs | |
| State | Published - 1 Oct 2014 |
Keywords
- Acidity
- Catalytic oxidation
- Pd
- Reaction condition
- Support effect
- Toluene