Alkaline Fuel Cell (AFC)
Alkali
fuel cells operate on compressed hydrogen
and oxygen and generally use a solution
of
potassium
hydroxide in water as their electrolyte.
Operating temperatures inside alkali cells
are around
150 to 200 °C. Because they produce
potable
water in addition to electricity, they
have
been a logical choice for spacecraft. NASA
selected alkali fuel cells for the Space
Shuttle fleet,
as well as the Apollo program of the 1960's,
mainly because of power generating efficiencies
that approach 70 percent. A major drawback,
however, is that alkali cells need very
pure hydrogen or an unwanted chemical reaction
forms
a solid carbonate that interferes with
chemical
reactions inside the cell. Since most methods
of generating hydrogen from other fuels
produce some carbon dioxide, this need
for
pure hydrogen
has slowed work on alkali fuel cells in
recent years. Another drawback is the need
for large
amounts of a costly platinum catalyst to
speed
up the reaction. However, several companies
are examining ways to reduce costs and
improve
the cells' versatility. Most of these alkali
fuel cells are being designed for transport
applications.1
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Phosphoric Acid Fuel Cell (PAFC)
The
Phosphoric Acid Fuel Cell is the most mature
fuel cell technology in terms of system development
and commercialization activities. It has been
under development for more than 20 years.
The phosphoric acid fuel cell uses liquid
phosphoric acid as the electrolyte. The phosphoric
acid is contained in a Teflon bonded silicone
carbide matrix. The small pore structure of
this matrix preferentially keeps the acid
in place through capillary action. Some acid
may be entrained in the fuel or oxidant streams
and addition of acid may be required after
many hours of operation. Platinum catalyzed,
porous carbon electrodes are used on both
the fuel (anode) and oxidant (cathode) sides
of the electrolyte. phosphoric acid fuel cell
power plant designs show electrical efficiencies
in the range from 36% to 42% (HHV2 ). The higher
efficiency designs operate with pressurized
reactants. The higher efficiency pressurized
design requires more components and likely
higher cost. A portion of the thermal energy
can be supplied at temperatures of ~ 250°F
to ~ 300°F. However, the majority of the
thermal energy is supplied at ~150°F.
The phosphoric acid fuel cell has a power
density of 160 to 175 watts/ft2 of active
cell area.3
One issue for phosphoric acid fuel cells is
that if the source of its hydrogen fuel is reformed
gasoline, sulfur must be removed from the fuel
entering the cell or it will damage the electrode
catalyst.
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Molten Carbonate Fuel Cell (MCFC)
The
Molten Carbonate Fuel Cell uses a molten carbonate
salt mixture, usually lithium carbonate and
potassium carbonate, as its electrolyte. The
electrolyte is suspended in ceramic matrix.
The anode is a nickel-chromium alloy, and
the cathode is a lithium-doped nickel oxide.4
Cell operating temperatures range from 600-800°C.
High-temperature molten carbonate fuel cells
can extract hydrogen from a variety of fuels
using either an internal or external reformer.
They are also less prone to carbon monoxide "poisoning" than
lower temperature fuel cells, which makes coal-based
fuels more attractive for this type of fuel
cell. Molten carbonate fuel cells work well
with catalysts made of nickel, which is much
less expensive than platinum. Molten carbonate
fuel cells exhibit up to 60 percent efficiency,
and this can rise to 80 percent if the waste
heat is utilized for cogeneration. Currently,
demonstration units have produced up to 2 megawatts
(MW), but designs exist for units of 50 to 100
MW capacity. Two major difficulties with molten
carbonate technology put it at a disadvantage
compared to solid oxide cells. One is the complexity
of working with a liquid electrolyte rather
than a solid. The other stems from the chemical
reaction inside a molten carbonate cell. Carbonate
ions from the electrolyte are used up in the
reactions at the anode, making it necessary
to compensate by injecting carbon dioxide at
the cathode.5
In addition, the electrolyte used in molten
carbonate fuel cells is highly corrosive, limiting
some of it potential applications.
Back to Top A. Solid Oxide Fuel Cell (SOFC)
The
Solid Oxide Fuel Cell uses a ceramic, solid-phase
electrolyte which reduces corrosion considerations
and eliminates the electrolyte management
problems associated with the liquid electrolyte
fuel cells. The solid oxide fuel cell is based
upon the use of a solid ceramic as the electrolyte.
The preferred electrolyte material is dense
yttria-stabilized zirconia. The solid oxide
fuel cell is a solid state device and shares
certain properties and fabrication techniques
with semi-conductor devices. The anode is
a porous nickel/zirconia cermet while the
cathode is magnesium-doped lanthanum manganate.
In development cells and small stacks, the
solid oxide fuel cell has demonstrated 0.6V/cell
at about 232 A/ft2. Lifetimes in excess of
30,000 hours for single cells have been demonstrated
as have a number of heat/cool cycles. Presently
available, unpressurized solid oxide fuel
cells deliver fuel to electric efficiencies
in the range of 45% (HHV). Argonne National
Laboratories suggests that pressurized systems
could yield fuel efficiencies of 60% (HHV).
The high operating temperature of the solid
oxide fuel cell offers the possibility of
internal reforming. As in the molten carbonate
fuel cell, CO does not act as a poison and
can be used directly as a fuel. The solid
oxide fuel cell is also the most tolerant
of any fuel cell type to sulfur. It can tolerant
several orders of magnitude more sulfur than
other fuel cells. With a 1830°F (1000°C)
operating temperature, the solid oxide fuel
cell requires a significant start-up time.
It is estimated that the fuel to electricity
efficiency of solid oxide fuel cells to range
from 50-70%, depending on the size of the power
plant. In addition, these efficiencies hold
from about 15%-100% power, making the cells
ideal for applications in which a wide range
of loads is found. Because most solid oxide
fuel cells utilize both hydrogen and carbon
monoxide fuel inside the cell, they can readily
operate on hydrocarbon fuels such as coal gas,
gasoline, diesel fuel, jet fuel, alcohol, and
natural gas.6
The efficiency of the solid oxide fuel cell
used in CHP applications will be higher than
the polymer electrolyte fuel cells for two major
reasons. The first reason is that the hydrocarbon
fuel is reformed into hydrogen and carbon monoxide
fuel largely inside the cell. This results in
some of the high temperature waste heat being
recycled back into the fuel. The second reason
is that air compression is not required. Especially
on smaller systems, this results in a higher
amount of net electricity being produced and
quieter operation. Because of the high temperatures
that the solid oxide fuel cell must run, they
may not be practical for sizes much below 1,000
watts or when portable applications are involved.7
B. Solid Oxide-Hybrid Fuel Cell Power Systems
A
recent development in high temperature stationary
fuel cell power plants is the coupling of
a microturbine generator with a high-pressure,
natural gas-fueled solid oxide fuel cell.
High pressure waste heat from solid oxide
fuel cell is routed into a microturbine, generating
10% or more additional power than if the exhaust
gas energy had not been recaptured. In a recent
test by Siemens-Westinghouse, the output of
a 200 kW solid oxide fuel cell was boosted
to 220 kW through use of a microturbine hybrid
configuration.8 A new configuration using higher
gas pressures and a 50 kW gas turbine is expected
to boost output to 250 kW.9 These systems are
to 55-60% efficient in converting the energy
in natural gas into power, better than the
current 50% efficiency of natural gas turbines.
According to Siemens-Westinghouse, hybrid
solid oxide fuel cells may have the potential
to reach 70% efficiency as hybrid technology
improves. A 1MW hybrid solid oxide fuel cell
demonstration plant is planned for installation
in 2002.
Back to Top A. Proton Exchange Membrane (PEM)
The
Proton Exchange Membrane Fuel Cell10 offers
an order of magnitude higher power density
than any other fuel cell system, with the
exception of the advanced aerospace alkaline
fuel cell, which has comparable performance.
The proton exchange membrane can operate on
reformed hydrocarbon fuels, with pretreatment,
and on air. The use of a solid polymer electrolyte
eliminates the corrosion and safety concerns
associated with liquid electrolyte fuel cells.
The anode and cathode are prepared by applying
a small amount of platinum black to one surface
of a thin sheet of porous, graphitized paper
which has previously been wet-proofed with
Teflon. Platinum requirements are currently
0.60 oz/kW. Improvements in proton exchange
membrane performance can reasonably be expected
to reduce platinum requirements to 0.035 oz/kW
or about $2/kW.
The proton exchange membrane typically operates
at 70-85°C. Its low operating temperature
provides instant start-up and requires no thermal
shielding to protect personnel. About 50% of
maximum power is available immediately at room
temperature. Full operating power is available
within about 3 minutes under normal conditions.
Recent advances in performance and design offer
the possibility of lower cost than any other
fuel cell system.
In 5 kW production fuel cell stacks, Ballard
is achieving a stack-only power density of over
5.4 kW/ft3. Power densities approaching 14.2
kW/ft3 are certainly feasible. A near-term system,
including fuel and oxidant controls, cooling,
and product water removal which operates on
hydrogen and air at 45 psia will provide 1.25
kW/ft3 and 40 W/lb. As is true with all fuel
cells, performance is improved by pressurizing
the air. In any application, there will be a
trade-off between the energy and financial cost
associated with compressing air to higher pressures
and the improved performance. Pressures above
45 psia are not likely to be advantageous for
most applications. Cell operating lifetimes
in excess of 50,000 hours were demonstrated
for the proton exchange membrane during the
NASA program.11
B. Regenerative Proton Exchange Membrane-based
fuel cells
Properly
designed, a proton exchange membrane fuel cell
can be run in reverse, acting as an electrolyzer.
This dual-function system is known as a reversible
or unitized regenerative fuel cell (URFC). A
regenerative fuel cell uses water and electrical
energy as inputs, electrolyzes the water, and
emits hydrogen and oxygen as outputs. These
units are currently in the prototype stage,
with novel applications such as creating hydrogen
during the day with solar electric power, then
using the hydrogen fuel at night to power a
hybrid solar/hydrogen fuel cell high-altitude
unmanned reconnaissance airplane.
The URFC is an excellent energy source in situations
where weight is a concern because it is lighter
than a separate electrolyzer and generator system.
In 1995, the regenerative fuel cell, coupled
with lightweight hydrogen storage, had by far
the highest energy density of any chemical battery--about
450 watt-hours per kilogram.12
Energy Conversion Devices, Inc. (ECDI) is currently
developing a regenerative fuel cell. According
to ECDI, their product is less costly than proton
exchange membrane cells because it does not
require platinum catalysts, and has a broader
operating temperature range. A proton exchange
membrane fuel cell's operating temperature is
60°C to 80°C, while the newly designed
regenerative fuel cell is able to operate within
a range of -20°C to 120°C.13
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Direct Methanol (DMFC)
Direct
methanol fuel cells are similar to the proton
exchange membrane cells in that they both
use a polymer membrane as the electrolyte.
However, in the direct methanol fuel cell,
the anode catalyst itself draws the hydrogen
from the liquid methanol, eliminating the
need for a fuel reformer. Efficiencies of
about 40% are expected with this type of fuel
cell, which would typically operate at a temperature
between 120-190 degrees F. Higher efficiencies
are achieved at higher temperatures.14
Direct methanol fuel cells are being considered
for a number of applications, including transport,
portable power including cellular phones and
laptop computers, auxiliary power for instrumentation
and vehicles, and as a battery replacement for
combat personnel and for battlefield applications.
The U.S. Office of Transportation Technologies
states that onboard reforming of liquid fuels,
such as gasoline, eliminates concerns about
hydrogen storage and a refueling infrastructure.
This could increase customer acceptance of the
technology and accelerate near-term introduction
of fuel cell vehicles. In addition, when compared
with conventional internal combustion engines,
the fuel cell system’s increased efficiency
will lower fuel consumption and reduce criteria
pollutants and carbon monoxide emissions which
contribute to global warming.15 Motorola, Mechanical
Technology, Inc., Los Alamos National Laboratory,
the Defense Advanced Research Projects Agency
(DARPA), and the U.S. Department of Energy are
among the major players in direct methanol fuel
cell research, development, and commercialization.
Back to Top Direct Carbon Fuel Cells
This
very new type of fuel cell is based on a process
called direct carbon conversion, in which
carbon particles are joined in an electrochemical
process with oxygen molecules to produce CO2
and electricity. The direct carbon fuel cell
technology was developed at Lawrence Livermore
National Laboratory (LLNL). The source of
carbon fuel can be any type of hydrocarbon,
including coal, lignite, natural gas, petroleum,
petroleum, coke, and biomass. Because it is
carbon, and not hydrogen, that fuels this
cell, hydrogen is released as a byproduct
of the cell reaction and could potentially
be captured for use in a separate hydrogen-powered
fuel cell.
According to a recent LLNL newsletter, the
technology uses aggregates of extremely fine
carbon particles, from 10 to 1,000 nanometers
in diameter, distributed in a mixture of molten
lithium, sodium, or potassium carbonate at 750-850°C.16
Total cell efficiencies are projected to be
70-80%, with power generation in the 1 kW/m2
range, sufficient for practical applications.
The carbon fuel particles can be produced through
pyrolysis of hydrocarbons, a thermal decomposition
method well-known as the source of carbon black
for tires, ink, and other applications in manufacturing
industries. While the concept has been successfully
demonstrated with a 3 W cell, this technology
is still in the experimental phase of development.
Because this is a high-temperature cell, it
would be best suited for stationary applications,
particularly in combination with CHP utilizing
the waste heat energy.
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Endnotes
1. Smithsonian Institute. "Collecting the History of Fuel Cells: A Smithsonian Research Project." Accessed February 1, 2002 at http://americanhistory.si.edu/csr/fuelcells/index.htm
2. Higher heating value (HHV) efficiency compares energy in fuel input (before reforming if reforming is required) to electrical output. Lower heating value (LHV) efficiency compares energy in hydrogen input to the cell to electrical output. HHV efficiencies are typically lower than LHV efficiencies, as HHV efficiency accounts for the fact that the input fuel is not pure hydrogen and that there is an energy cost for reforming. We report HHV efficiencies unless otherwise noted.
3. Department of Defense. U.S. Army Engineer Research and Development Center/Construction Engineering Research Laboratory (ERDC/CERL) Fuel Cell Program. Accessed January 30, 2002 at http://www.dodfuelcell.com/
4. Op. cit. Department of Defense ERDC/CERL Fuel Cell Program.
5. Op. cit. Smithsonian Institute.
6. Ben Wiens Energy Science Inc. March 2001. “The Future of Power Production” Accessed February 1, 2002 at http://www.benwiens.com/energy3.html
7. Op. cit. Ben Wiens Energy Science Inc.
8. U.S. Department of Energy. April 2000. “Department of Energy Announces World’s First ‘Hybrid’ Fuel-Cell Turbine.” DOE Fossil Energy Techline. April 17, 2000.
9. Siemens. January 2000. “Fuel Cells and gas Turbines: A Marriage of Efficiency.” Siemens Research and Innovation Webzine.
10. The Proton Exchange Membrane fuel cell (PEM or PEFC) is also known as Polymer Electrolyte Membrane (PEM) fuel cell.
11. Op. cit Department of Defense ERDC/CERL Fuel Cell Program.
12. LLNL. May 1997. “The Unitized Regenerative Fuel Cell “ Science and Technology Review. Lawrence Livermore National Laboratory. Accessed at http://www.llnl.gov/str/Mitlit.html
13. Energy Conversion Devices, Inc. “Regenerative Fuel Cells.” Accessed February 6, 2002 at http://www.ovonic.com/res/2_3_regen_fuel/regen_fuel_cells.htm
14. Fuel Cells 2000. “Types of Fuel Cells” Accessed February 1, 2002 at http://216.51.18.233/fctypes.htm
15. OTT. April 2001. “Direct Methanol Fuel Cell.” 2001 OTT Program Success Stories. Office of Advanced Automotive Technologies. http://www.ott.doe.gov/pdfs/dmfuelcell3_23_01.pdf
16. LLNL. June 2001. “Turning Carbon Directly into Electricity.” Science and Technology Review. Lawrence Livermore National Laboratory. Accessed at http://www.llnl.gov/str/June01/June01.html
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