Ethylene oxidation on IrO2, which is a metal-type conducting metal oxide, a
nd on Pt and Rh was used as a model reaction to compare the rate enhancemen
t and kinetic modification induced by (i) electrochemical promotion (non-Fa
radic electrochemical modification of catalytic activity effect) via electr
ochemical O2- supply from YSZ (Y2O3-stabilized ZrO2) and TiO2 and by (ii) m
etal-support interactions obtained by interfacing IrO2 with TiO2 (with and
without electrochemical promotion) or by depositing dispersed Rh on TiO2 an
d YSZ porous supports. It was found that the addition of TiO2, which is cat
alytically inactive, to IrO2 submicrometer particles enhances the activity
of IrO2 for C2H4 oxidation by a factor of 12 and that the same maximum rate
enhancement is obtained via electrochemical promotion of the IrO2 catalyst
(i.e., via electrochemical O2- supply to the IrO2 catalyst from a YSZ soli
d electrolyte). Furthermore it was found that the IrO2-TiO2 catalyst mixtur
es can only be marginally promoted electrochemically. These observations sh
ow conclusively that the mechanism of metal (IrO2)support (TiO2) interactio
n in the system IrO2-TiO2 is identical to that of the electrochemically pro
moted IrO2-YSZ system (i.e., continuous O2- supply to the IrO2 catalyst sur
face). This conclusion is also corroborated by independent kinetic and XPS
studies of electrochemical promotion of Pt utilizing TiO2 (instead of YSZ)
as the O2- donor. The kinetics of C2H4 oxidation were investigated on Rh fi
lms interfaced with YSZ at various imposed potentials and thus imposed work
function values, Phi (i.e., under conditions of electrochemical promotion
and also on finely dispersed Rh catalysts deposited on various doped and un
doped TiO2 and YSZ porous supports of measured work function Phi). Again it
was found that the reaction kinetics are affected in the same way upon var
ying the work function of the Rh film via electrical polarization of the Rh
/YSZ interface or upon varying the work function of the support of the disp
ersed Rh catalysts. This observation confirms the equivalence of the promot
ing mechanism of metal-support interactions and electrochemical promotion (
i.e., O2- migration onto the catalyst surface). The results show conclusive
ly that electrochemical promotion is an electrically controlled metal-suppo
rt interaction and that at least certain types of metal-support interaction
s are induced by reverse spillover of oxygen anions from the carrier onto t
he surface of the metal crystallites. (C) 2001 Academic Press.