A hybrid catalyst-bonded membrane device using gaseous reactants
for a carbon monoxide reduction (COR) reaction in the cathode chamber,
an aqueous electrolyte for an oxygen evolution reaction (OER) in the
anode chamber, and an anion exchange membrane (AEM) for product separation
was modeled, constructed, and tested. The Cu electrocatalyst was electrodeposited
onto gas diffusion layers (GDLs) and was directly bonded to AEM by
mechanical pressing in the hybrid device. The impacts of relative
humidity at the cathode inlet on the selectivity and activity of COR
were investigated by computational modeling and experimental methods.
At a relative humidity of 30%, the Cu-based catalyst in the hybrid
device exhibited a total operating current density of 87 mA cm–2 with a −2.0 V vs Ag/AgCl reference electrode,
a Faradaic efficiency (FE) for C2H4 generation
of 32.6%, and an FE for a liquid-based carbon product of 42.6%. Significant
improvements in the partial current densities for COR were observed
in relation to planar electrodes or flooded gas diffusion electrodes
(GDEs). In addition, a custom test bed was constructed to characterize
the oxidation states of the Cu catalysts in real time along with product
analysis though the backside of the GDLs via operando X-ray absorption (XAS) measurements.