Electrochemical Performance for Ordered Intermetallics
Figure 1: Schematic
of direct formic
acid PEMFCs
Figure 2: Crystal structures
Polymer
electrolyte membrane fuel cells (PEMFCs) that can run
directly on liquid fuels of small organic molecules such as methanol,
ethanol,
formic acid (FA) and others, featuring higher volametric and
gravimetric
energy densities and better energy efficiency have recently attracted
considerable interest as wide variety of power applications because of
the
simple handling of liquid fuels in storage and transfer (Fig. 1). In
order to
develop commercially available PEMFCs using liquid fuels which satisfy
demands
from both economical and environmental points of view, we must
overcome difficulties in the development of electrocatalysts in the fuel cells.
Serious
losses of energy due to the slow kinetics in the oxidation of SOMs and
gradual drops
of catalytic activity by carbon monoxide (CO) poisoning occur in the
anode
process. The improvement of electrocatalytic activity and tolerance to
CO in
the electro-oxidation of SOMs with Pt-based bimetallic and trimetallic
electrodes,
and Pt-group metals has been attempted. For example, the Pt-Ru alloys
are among
some of the most efficient catalysts for oxidation of methanol and have
shown
relative tolerance to CO poisoning, increased current densities, and a
decreased overpotential for fuel oxidation when compared to pure Pt. However, Pt-Ru alloy has inherently
poorly defined
surface structures, for example, with its surface sites occupied by Pt
or Ru in
a random fashion (Fig. 2-(a) and (c)). In
addition, the use of Ru-based alloys in place of pure Pt introduces a
stability
problem: during extended periods of operation, particularly under
non-optimal
usage (especially at high temperatures and current densities), the
alloy
surface becomes depleted of Ru. We have considered that these
properties of
ordered intermetallic compounds demand necessities for improving the
performance of anode materials with bimetallic alloys. In the surface
of PtPb and
PtBi ordered intermetallic phases whose employments have been proposed
by us
for first time as anode electrocatalyst materials, atomically ordering
of two
element atoms (Fig. 2-(b) and (d)) for showing higher activity are
meted.

Figure 3: Cyclic
Voltammograms of Pt, PtBi, PtPb Figure 4: Cyclic
Voltammograms for CO Oxidation Studied
PtBi
ordered intermetallic bulk phases have been shown to exhibit
remarkable electrocatalytic activity for the oxidation of FA in terms
of onset
potential and current density (Fig. 3 (b)). The
PtBi phases showed an onset of oxidation potential
(-0.12 V) of
approximately 300 mV less positive than pure Pt (Fig. 3 (a)). The steady-state current density of the PtBi
phases is 40 times larger than that of pure Pt in the FA oxidation. Moreover, oxidation curve observed at PtPb
ordered intermetallic phases (Fig. 3 (c)) also showed negative
potential shift
and increased steady-state current density, compared to PtBi ordered
intermetallic phases. The onset
potential and the oxidation current of the PtPb phases are -0.2 V and
3.6 mAcm-2,
respectively. CO is known to be among most problematic poison in PEM
direct fuel
cells with SOMs. The CO intermediate
species strongly adsorb onto the Pt atoms and seriously degrade the
oxidation
of FA and methanol. Eliminating the CO
intermediate and inhibiting the adsorption of the CO intermediate are
the major
factors in high anode performance. As
shown in Fig. 4 (B), the Pt surface show no current up to about +0.65 V
and a
sharp peak about +0.65 V ascribed to the oxidation of adsorbed CO to CO2
after exposing CO to the surfaces, compared to (A) before adsorption of
CO on
Pt. On the other hand, the effect of CO exposure to PtBi ordered
intermetallic
phases is different to compared pure Pt surfaces (C).
The voltammograms remained essentially
unchanged between before and after CO exposure, indicating that CO
molecules do
not irreversibly adsorb on the surface of PtBi ordered intermetallic
phases. The
dramatic drop in the affinity of CO for PtBi ordered imtermetallic
surface is a
direct consequence of its structure, specially, the difference in the
Pt-Pt
distance between Pt and PtBi. The expansion of the Pt-Pt distance in
PtBi might
make it very difficult for CO to bind in bridge site or three-fold
hollow site
configurations.
Figure 5: pXRD
pattern and STEM
image of PtPb nanoparticles Figure 6: Rotating
Disk Electrode Voltammograms
Ordered intermetallic phases need to be prepared in
nanoparticle form, so as to have increased surface area, which, in
turn, should
lead to enhanced electrochemical activity per platinum atom for
incorporating
ordered intermetallic phases into actual PEMFCs. We have prepared
nanoparticles
of ordered intermetallic phases by reducing metal precursors salts with
reducing agents at room-temperature. For example, we prepared PtPb
ordered
intermetallic nanoparticles with H2PtCl6∙6H2O,
Pb(C2H3O2)2∙3H2O,
and
sodium borohydride (NaBH4) whose BET surface areas were 15 m2g-1.
In addition, the
pXRD pattern (Fig. 5 (a)) of the PtPb nanoparticles showed the
formation of
single phase of ordered intermetallic PtPb. STEM image of synthesized
PtPb nanoparticles
(Fig. 5 (b)) showed the individual particles about 15-30 nm in size,
and these
aggregate to form networks. Lattice
fringes are clearly evident (Fig. 5(c)). When
the
activity of the PtPb nanoparticles was compared to that of commercially
available Pt and Pt-Ru alloy nanoparticles for the oxidation of FA, the
PtPb nanoparticles
showed remarkable superiority of electrochemical catalytic activity in
terms of
oxidation onset potential (-0.18 V vs.
Ag/AgCl) and current density (3 mAcm-2).