Catalytic activity, mechanisms, and active sites were determined for methane steam reforming (MSR) over gadolinium-doped ceria (GDC) supported iridium (0.1 wt%) prepared by impregnation of GDC with iridium acetylacetonate. Isothermal steady-state rate measurements followed by micro-gas chromatography analysis were performed at 660 and
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Catalytic activity, mechanisms, and active sites were determined for methane steam reforming (MSR) over gadolinium-doped ceria (GDC) supported iridium (0.1 wt%) prepared by impregnation of GDC with iridium acetylacetonate. Isothermal steady-state rate measurements followed by micro-gas chromatography analysis were performed at 660 and 760 °C over Ir/GDC samples pretreated in N
2 or H
2 at 900 °C. Transient responses to CH
4 or H
2O step changes in isothermal conditions were carried out at 750 °C over Ir/GDC pretreated in He or H
2 using online quadrupole mass spectrometry. In the proposed mechanism, Ir/GDC proceeds through a dual-type active site associating, as follows: (i) Ir metallic particles surface as active sites for the cracking of CH
4 into reactive C species, and (ii) reducible (Ce
4+) sites at GDC surface responsible for a redox mechanism involving Ce
4+/Ce
3+ sites, being reduced by reaction with reactive C into CO (or CO
2) depending on the oxidation state of GDC and re-oxidized by H
2O. Full reduction of reducible oxygen species is possible with CH
4 after He treatment, whereas only 80% is reached in CH
4 after H
2 treatment.
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