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A titanium-doped Ce 0.8 Sm 0.2 O 1.9 composite is developed as an anode component of low temperature solid oxide fuel cells running on methane fuel. Crystallographic parameters of (Ce 0.8-x Ti x )Sm 0.2 O 2-δ (0.00 0.8-x Ti x )Sm 0.2 O 2-δ composites are applied to an anode-supported single cell consisting of Ni-(Ce 0.8-x Ti x )Sm 0.2 O 2-δ anode/Ce 0.8 Sm 0.2 O 1.9 electrolyte/La 0.6 Sr 0.4 Co 0.2 Fe 0.8 O 3-δ cathode. Catalytic properties of Ni-(Ce 0.8-x Ti x )Sm 0.2 O 2-δ are inspected with the electrochemical performance and performance stability of the cells in dry methane fuel. The cell with Ni-(Ce 0.73 Ti 0.07 )Sm 0.2 O 2-δ (x = 0.07) anode displays a low polarization resistance and an optimum maximum power density (679 mW cm −2 at 600 °C). A performance stability investigation indicates that the cell exhibits a fairly low degradation rate of 3 mV h −1 during a 31 h operation in dry methane. These findings suggest the application potential of the titanium doped Ce 0.8 Sm 0.2 O 1.9 for the anode of solid oxide fuel cells.

This short communication describes the performance of a solid oxide fuel cell (SOFC) fueled by directly feeding premium gasoline to the anode without using external reforming. The novel component of the fuel cell that enables such operation is the mixed conductivity of MoO 2 -based anode. Using this anode, a fuel cell demonstrating a maximum power density of 31 mW/cm 2 at 0.45 V was successfully fabricated. Over a 24 h period of operation, the open cell voltage remained stable at ∼0.92 V. Scanning electron microscopy (SEM) examination of the anode surface pre- and post-testing showed no evidence of coking.

A NiMo–Ce0.5Zr0.5O2-δ (NiMo-CZ) catalyst has been developed for gasoline-fed solid oxide fuel cells (SOFCs). To apply the catalyst on a button-type single cell, the NiMo-CZ is deposited on top of conventional Ni-yttria-stabilized zirconia (YSZ) anode as a catalytic internal micro-reforming layer. The NiMo-CZ layer is effective in increasing the gasoline conversion and enhancing the yields of both H2 and CO at 750 °C. On the other hand, due to the high mechanical stress induced from the constrained sintering with a thicker catalyst layer, only a limited amount of catalyst (~20 mg) could be applied over the conventional button-type cell, which is not beneficial for enhancing overall cell performances. To overcome this issue, a tubular single cell configuration is adopted that allowed for higher catalyst loadings. By introducing higher catalyst loadings (~80 mg) in the vacant tubular channel of the single cell, the gasoline conversion, H2 yield, and CO yield all improve while cell lifetime increases by 42% compared to the performance of the button-type cell. The results suggest the potential of the NiMo-CZ catalyst for gasoline-fed SOFCs, and it demonstrates the advantage of the tubular single cell configuration for incorporating higher catalyst loadings for internal catalytic fuel reforming.