Glycerol solutions
were vaporized and reacted over ceria catalysts
with different morphologies to investigate the relationship of product
distribution to the surface facets exposed, particularly, the yield
of bio-renewable methanol. Ceria was prepared with cubic, rodlike,
and polyhedral morphologies via hydrothermal synthesis by altering
the concentration of the precipitating agent or synthesis temperature.
Glycerol conversion was found to be low over the ceria with a cubic
morphology, and this was ascribed to both a low surface area and relatively
high acidity. Density functional theory calculations also showed that
the (100) surface is likely to be hydroxylated under reaction conditions
which could limit the availability of basic sites. Methanol space-time-yields
over the polyhedral ceria samples were more than four times that for
the cubic material at 400 °C, where 201 g of methanol was produced
per hour per kilogram of the catalyst. Under comparable glycerol conversions,
we show that the rodlike and polyhedral catalysts produce a major
intermediate to methanol, hydroxyacetone (HA), with a selectivity
of
ca.
45%, but that over the cubic sample, this
was found to be 15%. This equates to a 13-fold increase in the space-time-yield
of HA over the polyhedral samples compared to the cubes at 320 °C.
The implications of this difference are discussed with respect to
the reaction mechanism, suggesting that a different mechanism dominates
over the cubic catalysts to that for rodlike and polyhedral catalysts.
The strong association between exposed surface facets of ceria to
high methanol yields is an important consideration for future catalyst
design in this area.