Solid oxide fuel cells (SOFCs) show high energy-conversion efficiency and thus emit less CO 2 than conventional combustion engines. Although SOFCs can directly convert hydrocarbons such as liquefied petroleum gas, these fuels readily induce coking on the electrodes of fuel cell stacks. To avoid coking, hydrocarbons can be subjected to a preliminary endothermic steam-reforming step at a relatively low temperature using waste heat from the stack. Herein, we report that a Rh/ Ce 0.25 Zr 0.75 O 2 catalyst exhibited higher propane-steam-reforming activity than other Rh/Ce 1À x Zr x O 2 catalysts and Rh/γ-Al 2 O 3 . Catalyst characterization revealed that Rh/Ce 0.25 Zr 0.75 O 2 had excellent redox property and high H 2 O-adsorption activity, which contributed to the activation of steam and thus enhanced the propane-steam-reforming activity of this catalyst.
Results and DiscussionThe temperature dependences of the catalytic activities of Rh/ Ce 1À x Zr x O 2 and Rh/γ-Al 2 O 3 are shown in Figure 1a. At 200°C, no propane consumption was observed over Rh/γ-Al 2 O 3 , and conversion was low over all the Rh/Ce 1À x Zr x O 2 catalysts. At 250°C, some of the propane was consumed, and the propaneconversion activities of the catalysts decreased in the order Rh/ Ce 0.25 Zr 0.75 O 2 > Rh/Ce 0.5 Zr 0.5 O 2 > Rh/Ce 0.75 Zr 0.25 O 2 > Rh/CeO 2 > Rh/ ZrO 2 > Rh/γ-Al 2 O 3 . At the target temperature for this study (300°C), Rh/Ce 0.25 Zr 0.75 O 2 showed the best activity: the propane conversion reached 55 %, which was 6 times that over Rh/γ-Al 2 O 3 . At 300°C, the catalyst activities for propane conversion decreased in the order Rh/Ce 0.25 Zr 0.75 O 2 > Rh/Ce 0.5 Zr 0.5 O 2 > Rh/ ZrO 2 > Rh/Ce 0.75 Zr 0.25 O 2 > Rh/CeO 2 (Figure 1b). At 350°C, propane conversion over Rh/Ce 0.25 Zr 0.75 O 2 and Rh/ZrO 2 reached 100 %, and the activities of the other catalysts decreased in the [a] L.