reaction, and hence the continuous Pt island network on the flat Si
substrate possess higher activity towards CO oxidation compared
to the blanket Pt on silicon and the Ru decorated Pt film.
Fig. 2(B) shows the cyclic voltammograms of the three
electrodes recorded in 1 M CH OH/1 M H SO aqueous
3
2
4
À1
solution at a potential scan rate of 20 mV s . The CV curve
of the continuous Pt island network/Si shows that the methanol
oxidation peak had the maximum around 0.63 V vs. SCE and a
very low onset potential of B0.38 V. Also shown in Fig. 2(B) is
the CV curves of the blanket Pt film and the Ru decorated Pt
film, which show a much smaller current density with a higher
onset potential. The negative onset potential shift indicated that
the continuous Pt island network/Si can effectively reduce
6
overpotentials in the methanol electrooxidation reaction.
Noted that the methanol oxidation peak in the forward scan
for the continuous Pt island network/Si electrode was much
larger than the peak in the region of 0.3–0.5 V in the reverse
scan. In the cyclic voltammetric scan, the anodic peaks in the
forward scan and in the reverse scan are associated with
electrooxidation of methanol and removal of incompletely
oxidized carbonaceous species (CO-like poisoning species)
on the electrode, respectively. The catalyst tolerance against
CO adsorption may be evaluated by the ratio of the current
Fig. 1 SEM images: (A) blanket Pt on flat Si substrate; (B) Ru on
blanket Pt; and (C) continuous Pt island network on the flat silicon
substrate; (D) X-ray photoelectron spectrum (XPS) of (a) blanket
Pt/Si; (b) Ru decorated blanket Pt; and (c) continuous Pt island network.
2
performed by flowing a 10% CO/N gas mixture in the 1 M
H SO aqueous solution at +100 mV for 35 min, using a Pt wire
2 4
as the counter electrode and a saturated calomel reference
electrode (SCE). Before scanning, the solution was purged with
density of the forward anodic peak (I
7
f
) to that of the reverse
anodic peak (I ), (I /I ). For the continuous Pt island/Si
b
f b
N gas for 30 min to removed CO remained in the solution.
2
electrode, the (I /I ) ratio was calculated to be B19. This ratio
f b
Representative CO-stripping voltammograms for the conti-
nuous Pt island network/Si, the Ru decorated Pt film and the
blanket Pt/Si electrodes are illustrated in Fig. 2(A).
was more than 9 times and 20 times larger than that of the Ru
decorated Pt film and the blanked Pt film, respectively.
Chroamperometry technique was employed to further test the
activity of theses three electrodes. Fig. 2(C) shows the chrono-
amperogram of electroactivity of the three electrodes at the
2
À1
A high ESA of 67 m g was obtained for the continuous Pt
island network/Si electrode by integrating the CO-electrooxidation
peak of first CO stripping cycle, assuming an oxidation charge
3 2 4
oxidation potential of B0.4 V in the 1 M CH OH/1 M H SO
À2
value of 420 mC cm for a monolayer of CO adsorbed on a
smooth platinum surface. The ESA of the continuous Pt island
aqueous solutions at 25 1C. Steady-state currents for methanol
electrooxidation were measured for more than 800 s. At the
oxidation potential of 0.4 V, the steady-state currents at 800 s for
the continuous Pt island network/Si, Ru decorated Pt film
5
network/Si electrode is much higher than that of the Ru decorated
À1
2
Pt film electrode (21 m g ) and that of the blanket Pt electrode
2
16 m g ). This shows that the continuous Pt island network/Si
À1
À2
À2
(
and blanket Pt/Si are B10 mA cm , B4 mA cm , and
À2
electrode has a relatively high ESA, most likely due to the
interconnect structure of the Pt islands. Such well-defined contin-
uous Pt island network structure provides abundant active sites
for the electrooxidation reaction of methanol.
B0.05 mA cm , respectively. The observation implied that
most CO-like poisoning species could be oxidized and removed
from the Pt catalyst so that the catalytic oxidation of methanol
could be kept proceeding efficiently on the continuous Pt island
network/Si electrode. Because oxygen containing species on the
From the CO-stripping curve, we noticed a lower onset poten-
tial and smaller peak potential for CO oxidation on the contin-
uous Pt island network electrode in comparison to the Ru
decorated Pt film and the blanket Pt film/Si. Examination of the
CO oxidation curves reveals that the onset potential of the
continuous Pt island network/Si electrode (B0.43 V) is lower
than that of the Ru decorated/Pt (B0.48) and the blanket Pt/Si
2
SiO surface layer can promote the CO removal as described
above, the improvement of the electrooxidation activity can be
ascribed to the synergistic effect of the Pt island catalyst and the
2
SiO surface layer. These results are very consistent with the CV
studies shown in Fig. 2(A) and (B).
Tafel plot for electrochemical oxidation of 1 M CH OH/1 M
3
À1
(B0.60 V). The CO oxidation peak potential for the continuous Pt
H SO aqueous solution at a scan rate of 1 mV s is shown in
2
4
island network/Si (B0.57 V) is also lower than that for the Ru
decorated Pt (B0.60 V) and the blanket Pt/Si (B0.64 V), probably
due to an enhanced CO oxidation rate on the Pt islands
Fig. 1S in the ESI.w The blanket Pt/Si and Ru decorated Pt film
have a Tafel slope of B115 mV/dec and B137 mV/dec, respec-
tively. On the other hand, the continuous Pt island network/Si
exhibits a much larger Tafel slope (B245 mV/dec), suggesting a
great difference in the electrooxidation mechanism for the
continuous Pt island network/Si electrode from the other
two electrodes. This might be ascribed to the Pt island network
2
surrounded by the chemical SiO layer, which was formed on
the Si substrate in the electrolyte. The presence of the oxide layer
on the silicon substrate can promote the oxidation of CO
4
adsorbed on the active Pt sites via the bifunctional mechanism.
The oxygen-containing species on SiO
2
(such as hydroxyl surface
structure and the presence of active oxygenated on the SiO
2
8
group) can transform CO-like poisoning species adsorbed on Pt to
CO , releasing the active sites on Pt for further electrochemical
surface layer. The mechanistic difference could result in the
better catalytic activity and CO tolerance of the 2-D
2
This journal is ꢀc The Royal Society of Chemistry 2008
Chem. Commun., 2008, 6516–6518 | 6517