nickel,
and
auxiliary during
is converted
hydrogen start-up
auxiliary
to nickel
supply
sulftde.
powers
of the fuel processor,
supply
of desulfurised
the fuel processor
is brought
An
the fuel cell while
an
fuel is used until
process
steps
: components
cost.
The
seal
mechanically,
between
on the fuel electrode
so it can
air electrode.
made from different
water
polymeric
including
those
the electrode.
techniques.
A further
materials, with welding
temperature.
advantage
Patent number: WO 00139873
disassembled
is that
the
components
may
Pressurised
water
The
invention
system
to trace and repair faults.
is a pressurised
system is under coolant of the exhaust pressurises Thus
water
Water vapour reforming hydrocarbon
the
stress, a valve directs part
stream
to a supercharger
it for a condensing
an increased
amount
out of the exhaust
stream,
continuously
recovery When
pressurise
that
heat-exchanger. of water
without
normal
the need to
any of the power
plant
components.
The
patent
plant
fueled
converted
fuel cell power
by a hydrocarbon
to hydrogen-rich
reformer. remove
a PEM
fuel,
which
fuel gas stream
A shift converter
is
CO gases created
by the reformer.
unit
a
direct
methanol
of low-cost,
electroconductive electrolyte but
layers
cathode
enables
the transfer
fuel
cell.
A
between proton
two
transmission
of methanol
to the
Purged anode, low-effluent
fuel cell
Applicant: IFC, USA
the anode exhaust
response
to
Control a
analyser,
periodically
in response
of the
converter
into the cathode
of this flow may be in
flammability
composition
sensor,
current
output
gas or
of electrochemical enables
be fabricated tolerances
with
easily
the minimum
relates to a composite
of flexible
graphite
embedded
fibres,
provide
and
permeability
in fuel cell
temperatures
Electrically
of the
temperature
close
the
of the unit cells.
also covers a method
of regulating
Here
a metal
highly
properties,
controlling
patent
process
electrolyte,
of
The
film
the degree
its
an easily
and a high-efficiency
Patent number: US 608703
through
cells
its thickness
plate
The electrical by heating
so that
silver
ceramic
etc. for a fuel
conductivity
material
to at least
migrates
and
into
is easily and
creates
pathways.
In this electrically field
plate,
separated
structure-
fuel cell.
the
218O:l
fuel cell fluid flow
straight
and
and 62OO:l.
cell to
ro the required of equipment,
diffusion) partially
a polymer
electrode
catalyst
with a fluorocarbon
such that the ion-exchange
outlets
electrolyte
the fuel and air (gas is covered entirely ion-exchange capacity
or
resin,
of the resin
between
higher
ratio
differential of the oxidant about
are
of the 0.75
have a length of
When
than
one
less than about
preferably
area
channels
at least
has an open width
mm. The channels cross-sectional
1
conductive, parallel
by lands,
channels
the polymer
Applicant: Asahi Glass, Japan describes
the metal electrically
Fluid flow field plate
pressure
fuel cell in which
may
in contact
Patent number: WO 00/40520
PEM fuel cell electrodes patent
by
the ceramic
a silver-containing
density
The
as
Applicant: Ballard Power Systems, Canada
of sulfonation.
for producing
rendered
its
and
polyethersulfone,
also provides
controllable
virtue
easily film-processable,
water-resistant.
strictly The
by
solvent
such
been
of silver, to form a layer on a
such as a bipolar
conductive
material
has
conductive
substrate
oxide
for a fuel cell is cheap,
organic
using a sulfonated
flow-field
ceramics
ceramic
chromia
the incorporation
750°C
and process for
mould-processable
formed
of gaskets,
for use in fuel cells.
oxide
or
be achieved
Applicant: Sumitomo Chemical, Japan
thermoplastic
to
of the sheet to gases, which
conductive
cell assembly.
in a fuel cell system.
in
ceramic
Applicant: Ceramic Fuel Cells Ltd, Australia
Polymer electrolyte their production
membrane
an electrochemical
relatively
The invention
Patent number: US 6087034
Patent number: US 6087028
solubiliry
mix so no
composite
plates and electrodes
range
electrolyte
sealing,
is required.
can be used in the making
the internal
driving
cell
Another
gases cannot
between
about
500
between flow
to
about
the fluid flow field
plate is used in a fuel cell operating
Applicant: National Power, UK This method
fed
to a timer.
Patent number: WO 00139877
Fabrication
of the externally
Flexible graphite
electrically
and fuel in the exhaust
anode flow field is reacted in a catalytic stream.
as fuel into
fuel
Applicant: Ucar Graph-Tech, USA
within
easily
oxidant
The
PEM
applications.
gasket material
to
This polymer
Patent number: WO 00139876
or by feeding
operation.
manufacturing
automotive
such
can be used, in
Patent number: US 6087033
with
side.
In this fuel cell residual
a hydrocarbon
corrosion-resistant
carbon
prevents
with
temperature
the temperature
relates to an electrode-eIectrolyte
layer
an and
methods
is that the operating
a
desired
the of
fuel cells constructed
the cells due to defective
unit cells in a fuel cell stack are equalised
The invention
for
with
in normal
within
alumina
optimum
unit
reaction.
activated
temperature
In this invention
Germany
barrier
reforming
or hydrocarbon,
instead
as
Patent number: US 6086839
Regulating system
for for
additional
as fast
or hydrocarbon.
Applicant: Forschungszentrum Jiilich, The invention
warmed-up
is introduced
units,
hydrogen
start,
process
Applicant: Toyota, Japan
Patent number: WO 00139875
Electrode-electrolyte
stacks
by a
and selective oxidiser
most of the undesired
than
reformate
the burner
describes
are
is started
lower
and
be reached
feed of hydrogen
resulting
Applicant: IFC, USA
a cold can
units
reformation
fueled PEM fuel cell
particular
a system
for an effective
burner
fraction
Hydrocarbon
during
possible external
Patent number: WO 00139874
provides
operation
Two
describes
that mass production
advantage
invention
by which,
condenses
of
(now Xcellsis) The
both
conductivity
Fuel cells for mass production
dbb fuel cell engines, Germany
&$icant:
and electrical
Patent number: US 6087032
The patent
plant.
secures
Applicant: Siemens, Germany
recovery
for a fuel cell power
repellency
than that for the
approach
be
Patent number: US 6086643
Applicant: IFC,
is greater
This
be used to join components
’ incompatible
up to its operational
and
is generated
at a current mA/cm2,
the field
138 and 400 mbar.
inlets
rhe and
channels
is
These fluid
flow field plates may be formed by embossing or moulding. Patent number: WO 00141260
A Fuel Cells Bulletin No. 30
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