Abstract

The relation between hydrocarbon selectivity and cobalt particle size was studied using different alumina supports. Alumina phases, i.e. δ-, θ- and α-Al2O3 were produced from a small and a medium pore γ-Al2O3 by heat treatment. All catalysts were prepared by incipient wetness impregnation resulting in a cobalt loading of 12, 20 and 30wt.% cobalt. The catalysts were tested in a fixed bed reactor at 20bar, 483K and H2/CO=2.1. The relation between methane, olefin and C5+ selectivities was studied for 2–14nm cobalt particles supported on δ- and θ-Al2O3 supports prepared from the two different γ-Al2O3. The C5+ selectivity increases with increasing Co particle size for particles less than 8–9nm where the selectivity goes through a maximum. The C5+ selectivity decreases for larger Co particles and then seems to approach a constant value independent of the alumina phase and pore size. The lowest CH4 selectivity and the highest olefin to paraffin ratio were obtained at maximum C5+ selectivity.

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