Supported iron oxides are active oxidation catalysts whose efficiency and selectivity can be controlled by the level of dispersion of the Fe phase. Here we describe a simple route to highly dispersed, supported Fe(III) catalysts. Well-defined active sites are prepared by incipient wetness impregnation of aqueous Fe(EDTA) complexes on neat and alkali-modified SiO2, Al2O3, ZrO2, and CeO2. Impregnation is followed by heat treatment under O2 to remove the EDTA ligand, leaving only the highly dispersed iron oxide centers on the support surface. The catalysts are characterized by H2-TPR, XPS and diffuse reflectance UV-visible spectroscopy (DRS) and compared to iron catalysts prepared using more common, although often more expensive, precursors. DRS results of these catalysts are characteristic of isolated Fe3+ cations up to 0.5 Fe/nm2 and of highly dispersed Fe3+ amorphous layers up to 0.9 Fe/nm2, greatly exceeding that of typical precursors. Additionally, H2-TPR and XPS show the Fe(III) to Fe(II) transition expected of highly dispersed Fe3+ species and no evidence of bulk iron oxides. Finally, the activity, selectivity, and kinetic behavior of the catalysts are studied for adamantane oxidation with aqueous H2O2 as a model reaction for selective C-H bond activation. For this reaction, the initial TOF of this highly dispersed Fe3+ surface species is in the order of 10 s-1, as compared with TOF <1 s-1 for a more traditional catalyst starting with Fe(NO3)3.
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