The kinetic behavior of CuFe2O4/γ-Al2O3 bifunctional
catalyst is studied in the steam
reforming of dimethyl ether (SRD) under reaction-regeneration cycles
in a fluidized-bed reactor, in the 200–400 °C range for
the reaction step and with coke combustion with air at 500 °C
for the regeneration step. Results in the SRD process show that, in
order to attain a reproducible and active behavior of the catalyst
in successive reaction-regeneration cycles, a previous equilibrating
treatment is required, consisting of a steam reforming reaction under
high coke deposition conditions and subsequent coke combustion. Characterization
results of the catalyst subjected to different treatments reveal that
the equilibration and high activity of the catalyst are a consequence
of the following structural changes: (i) the presence of water in
the reaction medium gets the metallic copper redispersed within the
spinel matrix; and (ii) coke deposition, followed by its combustion,
is responsible for the structural change of the spinel from tetragonal
to cubic and the redispersion of the spinel on the γ-Al2O3 acid function.