This work describes
the satisfactory performance of a Ni/Al
2
O
3
catalyst
derived from NiAl
2
O
4
spinel in ethanol steam
reforming and focuses on studying
the prevailing reaction routes for H
2
formation in this
system. NiAl
2
O
4
spinel was synthesized using
a coprecipitation method and reduced at 850 °C to obtain a Ni/Al
2
O
3
catalyst. The spinel structure and catalyst
were characterized using XRD, TPR, N
2
physisorption, NH
3
adsorption and TPD, TPO, SEM, and TEM. The experiments were
carried out in a fluidized-bed reactor at 500 or 600 °C and different
space-time values, using pure ethanol, ethanol–water, pure
ethylene, or ethylene–water feeds. The reaction takes place
through two paired routes activated by each catalyst function (metal
and acid sites) whose extent is limited by the selective catalyst
deactivation. The results evidence that at the beginning of the reaction
the main route for the formation of H
2
and carbon (nanotubes)
is the dehydration of ethanol on acid sites followed by decomposition
of ethylene on the Ni–Al
2
O
3
interface.
This route is favored at 500 °C. After the rapid deactivation
of the catalyst for ethylene decomposition, the route of H
2
formation by steam reforming of ethanol and water gas shift reactions
over Ni sites is favored. The morphology of the carbon deposits (nanotubes)
allows the catalyst to maintain a notable activity for the latter
pathways, with stable formation of H
2
(during 48 h in the
experiments carried out). At 600 °C, the extent of the gasification
reaction of carbon species lowers the carbon material formation. The
high formation of carbon material is interesting for the coproduction
of H
2
and carbon nanotubes with low CO
2
emissions.