The
medium temperature shift (MTS) microreactor has been proposed
in order to decrease the CO content of reformate for fuel cell applications.
The Ni–K/CeO2 catalyst is synthesized and coated
on stainless-steel plates by electrophoretic deposition (EPD) and
then evaluated at 300–390 °C. The morphology of the catalyst
layers are analyzed by X-ray diffractometry (XRD), scanning electron
microscopy (SEM), and three-dimensional (3D) optical microscopy. The
FT-IR analysis and conductivity measurements are used for slurry characteristics
of different polyethylenimine (PEI) contents. The activity of the
catalytic plates inside the microreactor is tested at different gas
hourly space velocity (GHSV) values and H2O/CO molar ratio
of 3. The CO conversion is raised by increasing the coating time from
1 min to 3 min, and it has an optimum at 140 V for applied voltage
(between 30 V and 180 V). Also, it is found that the CO conversion
is optimal at a PEI content of 0.3 wt %. Generally, the optimum
conditions are achieved at 3 min, 140 V, and 0.3 wt % PEI,
which results to 93% and 5.8% (GHSV = 12 000 mL h–1 gcat
–1) for CO conversion and CH4 selectivity, respectively.
Consequently, the results confirm the fact that the microreactor performance
will be enhanced, compared to using a packed-bed reactor.