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Figure
1
Figure
2
The
Abruña group has been focusing on the active pursuit of
anode
catalysts for
fuel oxidation, as well as the investigation of possible catalysts to
enhance
the cathodic reduction of oxygen. While
we have been looking at the individual components of a fuel cell in
great
detail, we have also tried our hand at developing an actual fuel cell. We
have now developed a micro fuel cell which
includes both of the components above, but is unique in a number of
ways when
compared to a macro scale room temperature fuel cell.
One
of the main differences is that typical
fuel cells employ polyelectrolyte membranes (PEMs) that prevent the
fuel from
mixing with the oxidant. While that
seems like an easy enough task, it is difficult to actually carry out
because
the PEM must be selectively permeable to protons. That
makes a PEM very costly to develop. It
also turns out that the PEMs used today
are not very robust and are not completely selective.
Our
idea was to completely eliminate the
costly PEM in our micro fuel cell.

Figure
3
Figure
4
It
has been shown that laminar flow can be employed, in place of a
polyelectrolyte
membrane (PEM), in order to develop a membraneless microchannel fuel
cell. In a microchannel, two
solutions can
be
flowed side by side and they will not mix. They
don’t even have to be pump very fast for this
to occur due to the
dimensions of the microchannel! We can
then pump fuel and oxidant together and fuel crossover will not occur
to an
appreciable extent at the temperatures, flow rates, and time scales
involved. Laminar flow also
allows proton
conduction at
the interface of the two solutions, thus eliminating the need of the
PEM
completely. By eliminating the PEM,
a
common component in macro-fuel cells, development costs can be reduced,
and the
complexity of the micro-fuel cell design can be decreased.
We
have developed a planar membraneless microchannel fuel cell design
which
includes a silicon microchannel with a “tapered flow
boundary” in order to
ensure the establishment of laminar flow of the fuel and oxidant
streams prior
to their coming into contact. This
design takes advantages of a large electrode area and allows for the
testing of
a variety of microchannels and fuel systems. The power produced from
the H2/O2
single microchannel fuel cell, using Pt as the catalyst, was on the
order of
0.60 mW/cm2. Using
this
design, we will be able to integrate the catalyst materials above in
order to
increase the power generated from this device. Figure
1 shows a side-view of the planar microchannel fuel
cell. Figure
2 is a power curve for a
5-microchannel
array, using hydrogen as a fuel, fabricated in order to increase the
power
output of this device. This system can
be a considered a versatile platform for testing a number of
electrodes, fuels,
and microchannel dimensions. We will
continue design optimization and power output enhancement.
We
will also continue to investigate the use
of new fuel systems that could not be considered with PEM fuel cells. Figure
3 shows the actual individual
components of the versatile device platform, as well as the fully
assembled
micro fuel cell integrated with a fuel pumping system and data
collection
instrumentation.
This research has been spear-headed by the formation of the Cornell
Fuel
Cell Institute taking a radical
departure from
conventional thinking and approaches to develop new materials that
could improve the efficiency of the main components of a low
temperature (< 150°C) fuel cell and on reformer
catalysts for
low temperature operation.
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