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Advances in reforming and partial oxidation of hydrocarbons for hydrogen production and fuel cell applications

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Figure

Fig. 1. Evolution as a function of time of the anodic gas phase composition compared torate of 4 sccm; dashed line represents the levels measured at OCV in diluted H[46]the current of the cell; the cell was operated at V = 0.6 V in pure CH4 with a total flow2 at 900 °C.
Fig. 2. I-V33.3% H and I-P curves of the fuel cells with the 3 wt% Ru-Al2O3 catalyst layer operating on a mixed gas composed of pure hydrogen (a), 80% CH4 and 20% O2 (b), 66.7% CH4 and2O (c) and 66.7% CH4 and 33.3% CO2 (d) at different temperatures [48].
Table 1Chemical composition of Ni-metal/support catalyst and noble metal/support for steam reforming of methane.
Fig. 4. The rate of steam reforming is measured forsteam-to-carbon ratio was 1Ni/YSZ at 700 °C and (b) Sn/Ni/YSZ at 760 °C
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