Abstract

The active site in ZSM-5 zeolite-supported palladium, which shows the catalytic activity for NO reduction with methane as a reducing agent, has been investigated qualitatively and quantitatively by means of NO chemisorption and NaCl titration, comparing with PdO supported on silica. Palladium species in 0.4 wt.% Pd loaded H-ZSM-5 can adsorb NO equimolarly after calcination at 773 K, and almost all the NO was desorbed at around 673 K, while the palladium species on PdO/SiO 2 hardly adsorbed NO. The palladium species in Pd(0.4)/H-ZSM-5 are ion-exchangeable with Na + in NaCl solution, indicating that they exist in a cationic state of an isolated Pd 2+. This method for quantitative analysis of the isolated Pd 2+ cations is named as ‘NaCl titration’. The amount of the isolated Pd 2+ cationic species increased with increasing palladium content on Pd/H-ZSM-5, and PdO co-existed above 1 wt.%. The amount of the isolated Pd 2+ cation was unchanged after the reaction of NO 2–CH 4, NO 2–CH 4–O 2, or CH 4–O 2 at 673 K, while the adsorbed amount of NO per the Pd 2+ as determined by NO-TPD decreased after the NO 2–CH 4–O 2 reaction. It was found by NaCl titration that the catalytic activity of Pd/H-ZSM-5 for NO 2–CH 4–O 2 reaction increased with increasing amount of the isolated Pd 2+ cationic species up to 0.7 wt.%, while the increase in the amount of PdO led to decrease in selectivity towards NO 2 reduction. The palladium species that are active and selective for NO reduction with CH 4 will be proposed.

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