Reaction of propane + NO + oxygen over PtRh was investigated
using
proton-conductive Sn0.9In0.1P2O7 (SIPO), Sn0.95Al0.05P2O7 (SAPO), Sn0.9Mg0.1P2O7 (SMPO), and Fe0.5Nb0.5P2O7 (FNPO) materials as catalyst supports. The proton conductor-supported
Pt–Rh catalysts (0.01 wt % Pt content and 0.005 wt % Rh content)
showed significantly different activities: temperatures at which propane
oxidation achieved 50% conversion (T
50%) were 313, 330, 405, and 550 °C for Pt–Rh/FNPO, Pt–Rh/SIPO,
Pt–Rh/SAPO, and Pt–Rh/SMPO, respectively; T
50% values for NO reduction were 330, 386, 465, and greater
than 600 °C for Pt–Rh/FNPO, Pt–Rh/SIPO, Pt–Rh/SAPO,
and Pt–Rh/SMPO, respectively. A similar tendency was also seen
for the dependence of catalytic activity on space velocity. Only small
differences in BET surface area and particle size were observed among
FNPO, SIPO, SAPO, and SMPO. In addition, the dispersion state of PtRh
was similar among the impregnated catalysts. Conversely, proton conductivity
of these catalyst supports decreased in the order FNPO > SIPO >
SAPO
> SMPO. In particular, protons were most strictly restricted to
the
lattice oxide ions in SMPO. On the basis of these results, the catalytic
activity of Pt–Rh/proton conductors was correlated with proton
conduction in the bulk of the catalyst supports.