e-journal
Metallic phases of cobalt-based catalysts in ethanol steam reforming: The effect of cerium oxide
Abstract.
The catalytic activity of cobalt in the production of hydrogen via ethanol steam reforming has been
investigated in its relation to the crystalline structure of metallic cobalt. At a reaction temperature of
350 8C, the specific hydrogen production rates show that hexagonal close-packed (hcp) cobalt possesses
higher activity than face-centered cubic (fcc) cobalt. However, at typical reaction temperatures (400–
500 8C) for ethanol steam reforming, hcp cobalt is transformed to less active fcc cobalt, as confirmed by in
situ X-ray diffractometry (XRD). The addition of CeO2 promoter (10 wt.%) stabilizes the hcp cobalt
structure at reforming temperatures up to 600 8C. Moreover, during the pre-reduction process, CeO2
promoter prevents sintering during the transformation of Co3O4 to hcp cobalt. Both reforming
experiments and in situ diffuse-reflectance infrared Fourier transform spectroscopy (DRIFTS) showed
that the surface reactions were modified by CeO2 promoter on 10% Ce–Co (hcp) to give a lower CO
selectivity and a higher H2 yield as compared with the unpromoted hcp Co.
Keywords: Ethanol steam reforming, Hydrogen production, Metallic cobalt, CeO2 promoter, In situ X-ray, diffractometry (XRD), In situ diffuse-reflectance infrared Fourier, transform spectroscopy (DRIFTS).
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