This study reports on the activity and stability of PdO/γ-AlOOH/γ-Al
2O
3 monolith catalysts, promoted with varying amounts of CeO
2, for CH
4 oxidation. Although the beneficial effects of CeO
2 have been reported for powdered catalysts, this study used
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This study reports on the activity and stability of PdO/γ-AlOOH/γ-Al
2O
3 monolith catalysts, promoted with varying amounts of CeO
2, for CH
4 oxidation. Although the beneficial effects of CeO
2 have been reported for powdered catalysts, this study used a cordierite (2MgO.2Al
2O
3.5SiO
2) mini-monolith (400 cells per square inch, 1 cm diameter × 2.5 cm length; ~52 cells), washcoated with a suspension of γ-Al
2O
3 combined with boehmite (γ-AlOOH), followed by sequential deposition of Ce and Pd (0.5 wt.%) by wetness impregnation. The monolith catalysts’ CH
4 oxidation activity and stability were assessed in the presence of CO, CO
2, H
2O and SO
2 at low temperature (≤550 °C), relevant to emission control from lean-burn natural gas vehicles (NGVs). The CeO
2 loading (0 to 4 wt.%) did not significantly impact the adhesion and thermal stability of the washcoat, but CeO
2 reduced the inhibition of CH
4 oxidation by H
2O and SO
2. The catalyst activity, measured by temperature-programmed methane oxidation (TPO) in a dry feed gas with 0.07 vol.% CH
4, showed that adding CeO
2 to the γ-AlOOH/γ-Al
2O
3 washcoat suppressed the activity of the catalysts; whereas, CeO
2 improved the catalyst activity when H
2O (2 and 5 vol.%) was present in the feed gas. Moreover, adding CeO
2 decreased catalyst deactivation that occurred in the presence of 10 vol.% H
2O and 5 ppmv SO
2 at 500 °C, measured over a 25 h time-on-stream (TOS) period. The highest catalyst activity and stability for CH
4 oxidation in the presence of H
2O was obtained by adding 2 wt.% CeO
2 to the washcoat.
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