Pt and Pd supported
on beta zeolites, with different silica to
alumina ratios (SARs), are examined in the form of diesel oxidation
catalysts (DOCs) for the oxidation of CO, NO, C3H8, and C3H6. The effect of SARs on the physicochemical
properties of the catalysts, their subsequent oxidation activity,
and sulfur tolerance was investigated. A beta zeolite with a high
SAR has low acidity and high hydrophobicity, which induces the agglomeration
of either Pt or Pd in the catalysts during preparation and thermal
treatment. The effect of sintering is more severe on Pt than on Pd
catalysts. High-SAR zeolites retained Pt in a more metallic fraction
in the obtained catalysts, whereas this effect was not significant
for the Pd-based catalyst, wherein Pd exists mostly in the oxide form.
High-SAR Pt/BEA and Pd/BEA catalysts exhibit better conversion of
CO, NO, C3H8, and C3H6 than low-SAR catalysts. A linear relationship for turnover frequency
(TOF) with SAR (and with average particle size) was found for all
four oxidation reactions, namely, the higher is the SAR, the higher
is the TOF. This suggests that the catalysts are tailorable by adjusting
the SAR of the zeolite supports. A five-cycle test indicated that
zeolite-based catalysts have greater stability than alumina-based
catalysts. The activity for NO oxidation was very stable for the high-silicious
Pt/BEA catalyst with time-on-stream, which was not the case for the
Pt/Al2O3 catalyst. The Pd/BEA catalysts were
more susceptible to sulfur poisoning than their Pt counterparts; however,
they were easily regenerated. Also, the Pt/BEA catalysts were effectively
regenerated, especially for the highest SAR.