eformer
Patents
is
:liminates
operational. the
rssociated
with
Applicant:
Ballard
Power
Systems,
4ppLicant:
manifolding
configuration
in
this fuel cell stack simplifies sealing mechanisms associated
the with
the
stack
manifolds,
reactant
streams
between
the separator
resilient passages
MEA seals. may also be adjoining
between surfaces
Patent number:
and
pi thick
region zone
zone
ieposited
plate pairs.
US 6066409
vapour
WO
Applicant:
Applicant:
Degussa,
that
includes
particles
Germany
catalyst finely
is described dispersed
on a powdery,
4n
alloy
electrically
poisoning
when
the
For
particles
have mean
between
0.5 and >2 nm.
Patent number:
alloy
crystallite
Energy
Applicant:
and
sizes
US 6066410
moulding plate
for
or
a PEM
combined
conductive
them
from
with on
walls
The
and
surfaces
prevents
Applicant:
in sub-freezing
of the
start-up,
premature
Canada A method operation which
includes
described. stream which direct
63
During
a fuel
Patent
system
reformer
start-up
in
i>
the fuel
number:
includes ro
the
coolant
of the fuel until
WO
long
th<
for fuel the
that
On
Patent
the
fuel
UK
cooling,
manner,
jressure
drop
iucing
hydrogen
patent number:
the
with
to give a a very
low
for
pro-
suitable
for a fuel cell. WO
001325
13
Here
flow
separator
OOl31814
fuel
the 0,
tc inlel
t
the
Hz !
when
z1
:
two
plate
coextensive shaped
cell
sheet
to promote
of reactant electrodes
together
and form number:
of at metal the
gases to the in the
elements
metal
space between
for a PEM
is constructed
These
Patent
of Gas
USA
a separator
elements
operatior
fuel cell installation, and
gas
may the
Institute
distribution
In this process for reliable
adjacent
or oxidising
WO
a
surface parallel
and
ro
number:
Applicant:
Germany
closed
Matthey,
Sheet metal PEM bipolar plate
US 6068941
is
Johnson
adjacent
whose
cooling
perpendicular
Applicant:
valve
of the stack.
US 6071634
reformer
channels
channels
least
inlet
increases,
thus
00131813
side,
Technology,
closed,
overheating
in
electric
reactant
to raise
off the module
output
Yvithout
available The
Japan
so
of air alcohol
is first
c:urrent
:ompact
fuel cell stack includes coolant
its
plane.
catalyst,
valve
passages.
:ounter-current
or
to improve
separator
Operation of a PEM fuel cell installation
switch
of hydrogen
t he anode
contains fhis reactor vessel .elective oxidation stages and has
from
the size of the
Toshiba,
PEM
rectangular
to the cathode
of a PEM
dosed
in the plate,
This
Fuel
amount
Siemens,
t he amount
Cooling in a solid polymer fuel cell stack
oxidise
number:
a
Patent
00130202,
the cathode to
the
by varying
anode
and added exhaust gas is recirculated t’o the fresh fuel gas, which increases
Removing CO from H,
is introduced
via
system
and/or
Systems,
cell
fuel
The
fuel cell stack
is fed to part of the fuel cells provide output power by oxidation
field
diffusing
commencing
a fuel
plate.
fuel cell’s performance.
environments.
producing heat cell’s temperature.
Power of
of
into
a controlled
is fed through flow
a
by a perforated
area,
fuel cell has methanol fed
carbon
start-up Ballard
channel
holes
filler. WO
0013 18 16
generation
4pplicant:
resin
during shutdown, to passages prevent trapped water from freezing
earth
clogging of the passages. Patent number: WO 00129092
Improved capability
It
WO
1Datent number:
is separated
an adjacent
especially
cell.
carbon
International
or ethanol
coating
an alkaline
the
an
protects
layer that limits
oxide
build-up
have.
which
corrosion.
is overlaid metal
assembly
coating
by in
Forschungszentrum
channel,
collector
Start-up of cold fuel cell Cells, USA Here a PEM
simply,
Germany
Applicant:
Applicant:
be
US 6068943
discharged
00/30203
Fuel
can
impurities
Here the electrode
injection-
uses a metal thin film.
/ lpplicant: BG, UK I n this system hydrogen-richer
from
fuel
and
F‘ower
power
Fuel introduced via perforated plate
a low surface
powder
the
the
Applicant:
polymer
with
a method
which
resulting
in
Patent number:
USA
fuel
a
by
reactor.
compo-
of a current
graphite
carbon in reformers
reformer
>xidising
are described
compression-
highly
International
alumina
avoided
a
plate
process
comprises
Cells, USA The walls of the fuel gas passages in this
a
moulding
Patent numbers:
Inhibiting deposition
safely
includes
Partners,
improved
jition
conductive carrier material. The catalyst is particularly resistant to CO
losses
liilich,
Current collector
alloy
cell
Nrcput mpurities
comprising
00130201
PEM anode catalyst A PtRu
provides
a fuel
1
electron-beam
fuel
Germany
This invention
deposition.
Patent number:
%tent number:
md
Korea
for use in a fuel cell powered
chicle, which
Forschungszeutrum
is preferably
by
Jhysical
SK Corporation,
‘his patent describes a miniature
4pplicant:
: F
resulting power
fuel reformer
IIncreased power density I lulich,
Enterprise
The
NItput.
Applicant:
US 6068942
eformer
1
:atalytically active metal, n significantly improved
Coolant provided
number:
patent
00130200
the electrode-membrane
nterfacial 3-475
non-active
of separator
1
USA membrane-electrode
assembly
directed
plates
Gore
Holdings, this .n
because
are not
start-up.
VIEAs with improved 3ower output
Canada The
WO
rlliniature
0, partial pressure I ,redetermined f i s reached in the cathode region.
typically
reformer
‘Jatent number:
Improved reactant manifolding and sealing
This
delay
a coolant
stack. nestle flow
them. WO
00131815
Fuel Cells
Bulletin
No. 28