U.S. patent application number 11/866954 was filed with the patent office on 2008-04-03 for polymer electrolyte fuel cell having improved current collector plates and method of forming the same.
This patent application is currently assigned to MATSUSHITA ELECTRIC INDUSTRIAL CO., LTD.. Invention is credited to Nobuhiro HASE, Kazuhito Hatoh, Susumu Kobayashi, Hiroki Kusakabe, Hideo Ohara, Soichi Shibata, Shinsuke Takeguchi.
Application Number | 20080079186 11/866954 |
Document ID | / |
Family ID | 29243388 |
Filed Date | 2008-04-03 |
United States Patent
Application |
20080079186 |
Kind Code |
A1 |
HASE; Nobuhiro ; et
al. |
April 3, 2008 |
POLYMER ELECTROLYTE FUEL CELL HAVING IMPROVED CURRENT COLLECTOR
PLATES AND METHOD OF FORMING THE SAME
Abstract
A polymer electrolyte fuel cell may have a cell stack of a
plurality of unit cells. Each of the unit cells includes a
hydrogen-ion conductive polymer electrolyte membrane, an anode and
a cathode sandwiching the polymer electrolyte membrane, an
anode-side separator having a gas flow channel for supplying a fuel
gas to the anode, and a cathode-side separator having a gas flow
channel for supplying an oxidant gas to the cathode. A pair of
current collector plates sandwiches the cell stack, and a pair of
end plates clamps the cell stack and the current collector plates
under pressure. The current collector plates have a conductive
carbon material as a main component, and have a terminal section
for connecting a power output cable in the vicinity of an
inlet-side manifold for the fuel gas or the oxidant gas.
Inventors: |
HASE; Nobuhiro; (Osaka,
JP) ; Hatoh; Kazuhito; (Osaka-shi, JP) ;
Kusakabe; Hiroki; (Osaka, JP) ; Ohara; Hideo;
(Osaka, JP) ; Kobayashi; Susumu; (Nara, JP)
; Shibata; Soichi; (Osaka, JP) ; Takeguchi;
Shinsuke; (Osaka, JP) |
Correspondence
Address: |
STEVENS, DAVIS, MILLER & MOSHER, LLP
1615 L. STREET N.W.
SUITE 850
WASHINGTON
DC
20036
US
|
Assignee: |
MATSUSHITA ELECTRIC INDUSTRIAL CO.,
LTD.
OSAKA
JP
571-8501
|
Family ID: |
29243388 |
Appl. No.: |
11/866954 |
Filed: |
October 3, 2007 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
|
|
10778602 |
Feb 17, 2004 |
7294423 |
|
|
11866954 |
Oct 3, 2007 |
|
|
|
PCT/JP03/04723 |
Apr 14, 2003 |
|
|
|
10778602 |
Feb 17, 2004 |
|
|
|
Current U.S.
Class: |
264/105 |
Current CPC
Class: |
Y02E 60/50 20130101;
H01M 8/0263 20130101; H01M 8/2483 20160201; H01M 8/0245 20130101;
H01M 8/0232 20130101; H01M 8/241 20130101; H01M 8/0258 20130101;
H01M 8/2457 20160201; H01M 8/0234 20130101 |
Class at
Publication: |
264/105 |
International
Class: |
B29C 43/18 20060101
B29C043/18 |
Foreign Application Data
Date |
Code |
Application Number |
Apr 17, 2002 |
JP |
2002-114552 |
Claims
1. A method of molding a current collector plate for a fuel cell
stack, said method comprising: evenly charging a molding compound
into a mold, said molding compound comprising a conductive carbon
material; compressing said molding compound in said mold at a first
temperature and a first pressure; providing a metal plate with a
conductive layer on a surface thereof; opening the mold and
inserting said metal plate into the mold; charging a further amount
of the molding compound into the mold to surround said metal plate
with said molding compound; and applying a second pressure and a
second temperature to the mold to from a current collector plate
having said metal plate embedded in said molding material, said
second pressure being higher than said first pressure and said
second temperature being higher than said first temperature.
2. The method of claim 1, wherein said metal plate is made of brass
and said conductive layer is platinum.
3. The method of claim 1, wherein said metal plate is made of Ti
and said conductive layer is TiN.
4. The method of claim 1, wherein said metal plate is made of Al
and said conductive layer is Ti--Al--N.
5. The method of claim 1, wherein said metal plate is made of
stainless steel SUS 316 and said conductive layer is Pb.
6. The method of claim 1, wherein said metal plate is made of
stainless steel SUS 316 and said conductive layer is In-doped tin
oxide.
7. The method of claim 1, wherein said step of providing said metal
plate with a conductive layer on a surface thereof comprises:
decomposing a gas on a metal substrate, said gas being a mixture of
silane, methane (CH.sub.4) and diborane (PH.sub.3) in a ratio
wherein P/(Si+C)=10 atomic % with the mixture having a pressure of
10 Torr conductive layer is an n-type doped SiC layer and with the
substrate at a predetermined temperature; and depositing a gold
electrode on the SiC layer.
8. The method of claim 7, wherein said predetermined temperature is
about 300.degree. C.
9. The method of claim 8, wherein said a time of said decomposing
step is controlled to provide a thickness of said n-type doped SiC
layer of 1000 .ANG..
Description
[0001] This is a divisional application of application Ser. No.
10/778,602 filed Feb. 17, 2004, the content of which is
incorporated by reference herein in its entirety; application Ser.
No. 10/778,602 is a continuation in part of PCT/JP2003/04723 filed
Apr. 14, 2003.
TECHNICAL FIELD
[0002] The present invention relates to a fuel cell for use in
portable power sources, electric vehicle power sources,
cogeneration systems or the like and more particularly to a current
collector plate of a polymer electrolyte fuel cell.
RELATED ART
[0003] A solid polymer electrolyte fuel cell generates electric
power by electrochemically reacting a fuel gas containing hydrogen
and an oxidant gas containing oxygen, such as air, through a
polymer electrolyte membrane that selectively transports hydrogen
ions.
[0004] The fuel cell generally comprises a cell stack of a
plurality of unit cells. Each of the unit cells comprises an anode
and a cathode sandwiching the polymer electrolyte membrane, an
anode-side separator for supplying the fuel gas to the anode, and a
cathode-side separator for supplying the oxidant gas to the
cathode. The cell stack further includes, on each end of the cell
stack, a current collector plate for collecting current and an
insulator plate for electrically insulating the cell stack from the
outside. The stack is sandwiched by end plates which are clamped by
clamping devices so that a clamping pressure of an appropriate load
is applied to the cell stack. The end plates are provided with
structure for supplying and discharging the fuel gas, oxidant gas,
and a coolant. A unit having such a structure is called a fuel cell
stack.
[0005] In order to supply the cell stack with the fuel gas, oxidant
gas and coolant, at least one of the current collector plates,
positioned at respective ends, has through-holes through which the
gases or coolant flows. The current collector plate is commonly
made of a metallic material, such as stainless steel or copper,
that is plated with gold in order to prevent the corrosion of these
through-holes, reduce the contact resistance to the separator of
the neighboring cell, and improve the electrical conductivity of
the current collector plate itself in the planar direction, for
suppressing the loss due to the electrical resistance. The
gold-plated current collector plate will corrode from minute pits
if the thickness of the gold plating is insufficient. Thus, an
anti-corrosion structure that eliminates the direct contact of the
gases has been proposed, for the through-holes, for supplying and
discharging the gases and coolant.
[0006] However, the use of the gold-plated metallic current
collector plate presents the following problems. In order that the
polymer electrolyte fuel cell functions normally, the water content
of the polymer electrolyte membrane must be high, so the supplied
gases and the discharged gases contain large amounts of steam.
Therefore, the metallic current collector plate is subject to
corrosion at its parts contacting the supplied gases and the gases
to be discharged. If the metal corrodes at the gas supply route,
metal ions generated thereby are included in the reaction gases,
impairing the performance of the electrolyte membrane. Also, if the
metal corrodes at the coolant supply route, the insulating property
of the coolant deteriorates and may cause a leak current, resulting
in a decrease in the amount of power generation.
[0007] In order to prevent the inclusion of ions, due to the
corrosion of metal, it is necessary to either increase the
thickness of the gold-plating or employ an anti-corrosion
structure. However, increasing the thickness of the gold-plating is
very costly. Also, employing an anti-corrosion structure involves
an increase in the number of components and production steps,
thereby increasing the complexity of the cell structure and
assembling operation. Attempts have been made to use a carbon
material as the current collector, since it does not suffer from
corrosive ion leaching. The carbon material, however, is brittle
and has higher electrical resistivity than metal, thereby
necessitating that the current collector plates have a sufficient
thickness to overcome this.
SUMMARY OF THE INVENTION
[0008] The present invention provides a polymer electrolyte fuel
cell having improved current collector plates. This fuel cell is
formed of a cell stack of a plurality of unit cells. Each of the
unit cells includes a hydrogen-ion conductive polymer electrolyte
membrane, an anode and cathode sandwiching the polymer electrolyte
membrane, an anode-side separator having a gas flow channel for
supplying a fuel gas to the anode, and a cathode-side separator
having a gas flow channel for supplying an oxidant gas to the
cathode. A pair of current collector plates sandwiches the cell
stack, and a pair of end plates clamps the cell stack and the
current collector plates under pressure. The current collector
plates have a conductive carbon material, and have a terminal
section for connecting a power output coupling, for example, a
power cable, closer to an inlet-side manifold for the fuel gas or
the oxidant gas than to an outlet-side manifold for the fuel gas or
the oxidant gas.
[0009] The terminal section may have a coating layer of a good
electrical conductor. The coating layer of a good electrical
conductor may be provided in a region that extends from the
terminal section to a part corresponding to an inlet-side part of
the gas flow channel of the cell communicating with the inlet-side
manifold.
BRIEF DESCRIPTION OF THE DRAWINGS
[0010] FIG. 1A is a partial sectional side view of an example of
the structure of a fuel cell stack in accordance with the present
invention;
[0011] FIG. 1B three-dimensionally shows the flow of the oxidant
gas through the cell stack of the fuel cell as illustrated in FIG.
1A;
[0012] FIG. 1C shows a different flow of gas from that of FIG. 1B,
wherein the fuel and oxidant gases and cooling water are introduced
from one of the end plates and discharged from the other end
plate;
[0013] FIG. 2 is a front view of a current collector plate in
Embodiment 1 of the present invention;
[0014] FIG. 3 is a back view of the current collector plate
illustrated in FIG. 2;
[0015] FIG. 4 is a sectional view taken on line IV-IV of FIG.
2;
[0016] FIG. 5 is a perspective view of connecting a power output
coupling such as a cable to the current collector plate;
[0017] FIG. 6 is a front view of a current collector plate in
Embodiment 2 of the present invention;
[0018] FIG. 7 is a back view of another example of the current
collector plate;
[0019] FIG. 8 is a front view of an example of an insulator plate
to be used with the current collector plate;
[0020] FIG. 9 is a front view of an anode-side separator in
Embodiment 3 of the present invention;
[0021] FIG. 10 is a front view of a current collector plate to be
combined with the separator plate of FIG. 9;
[0022] FIG. 11 is a sectional view taken on line XI-XI of FIG.
10;
[0023] FIG. 12 is a front view of a cathode-side separator in
Embodiment 3 of the present invention;
[0024] FIG. 13 is a front view of a current collector plate to be
combined with the separator plate of FIG. 12;
[0025] FIG. 14 is a sectional view taken on line XIV-XIV of FIG.
13;
[0026] FIG. 15 is a front view of another anode-side separator;
[0027] FIG. 16 is a front view of a current collector plate to be
combined with the separator of FIG. 15;
[0028] FIG. 17 is a front view of another cathode-side
separator;
[0029] FIG. 18 is a front view of a current collector plate to be
combined with the separator of FIG. 17;
[0030] FIG. 19 is a longitudinal sectional view of another example
of the current collector plate;
[0031] FIG. 20 is a front view of an anode-side current collector
plate in Embodiment 4 of the present invention;
[0032] FIG. 21 is a front view of a cathode-side current collector
plate in Embodiment 4 of the present invention;
[0033] FIG. 22 is a front view of an anode-side current collector
plate in Embodiment 5 of the present invention;
[0034] FIG. 23 is a back view of the anode-side current collector
plate of FIG. 22;
[0035] FIG. 24 is a front view of an anode-side current collector
plate in Embodiment 6 of the present invention;
[0036] FIG. 25 is a sectional view taken on line XXV-XXV of FIG.
24; and
[0037] FIG. 26 is an enlarged sectional view of the main part of an
example of a good electrical conductor layer formed on the surface
of a core metal plate.
DETAILED DESCRIPTION OF EMBODIMENTS
[0038] The present inventors have examined the use of a plate,
which may be a molded plate, that is mainly composed of a carbon
material, which is free from corrosion, as a current collector
plate. As a result, they have found that when the current collector
plates have a current-output terminal section in the vicinity of,
i.e., adjacent to or close to, an inlet-side manifold for the
reaction gas, particularly the fuel gas, effects unique to a
polymer electrolyte fuel cell can be obtained. That is, the
electrodes are humidified by water generated by the reaction on the
inlet side of the reaction gas supplied to the electrodes.
Furthermore, the polymer electrolyte membranes exhibit hydrogen-ion
conductivity when moistened with water and are thereby effectively
humidified.
[0039] Highly humidifying the electrodes improves their operational
durability. To achieve this, highly humidified reaction gases may
be supplied to the cell. However, an increase in the degree of
humidification of the fuel gas leads to a decrease in energy
efficiency.
[0040] According to the present invention, the terminal section is
provided adjacent to, close to or in the vicinity of an inlet-side
reaction gas manifold of the current collector plates. In other
words, the terminal section is closer to the inlet-side reaction
gas manifold than to an outlet-side reaction gas manifold, as
discussed in the examples below and illustrated in the drawings. As
a result, the current density at the electrode-reaction parts
adjacent to the inlet-side manifold is heightened, and the amount
of water generated by the reaction is therefore increased, so that
the electrodes can be kept in a highly humidified condition.
[0041] A current collector plate including a conductive graphite
plate, or a molded plate of a composite material of a conductive
carbon material and a binder, has higher electrical resistivity
than a metallic current collector plate. This higher resistivity
occurs even if the plate is made electrically anisotropic such that
the electrical resistivity in the plane direction is smaller, as
described in detail below. Thus, in the planar direction of the
current collector plate, a part close to the terminal section has
less electrical resistance to the terminal section than a distant
part. Accordingly, there is a difference in current density between
the part close to the terminal section and the distant part, and
the electrode reaction increases at the former part having higher
current density. In order to further enhance the current density on
the inlet side of the reaction gas at the electrode, it is
preferable to provide a coating layer on the current collector
plate, including a good electrical conductor, in a region extending
from the terminal section of the current collector plate to the
part of the current collector plate corresponding to the inlet-side
part of the reaction gas of the electrode.
[0042] When the current density on the inlet side of the fuel gas
at the anode is heightened, as described above, the amount of water
generated by the reaction at the corresponding cathode is
increased, and the generated water moves to the anode side by
reverse diffusion. In this way, by highly humidifying the inlet
part of the reaction gas (which part is not expected to be
humidified by the water generated at the electrode section)
particularly the vicinity of the inlet part of the fuel gas,
electrode durability can be improved. Also, the degree of
humidification of the fuel gas supplied to the cell can be
decreased, and energy efficiency can be improved.
[0043] In another mode of the present invention, the current-output
terminal section of the current collector plate has a coating layer
including a metal film or plate, which is a good electrical
conductor. This makes it possible to reduce the energy loss due to
the electrical resistance at the terminal section resulting from
the use of a conductive carbon material, which has lower
conductivity than metal, and to improve the strength of the
terminal section. In another mode, the metal plate constituting the
coating layer is extended so as to overlap the separator in the
fuel cell stack, i.e., the metal plate has applied thereto the
clamping pressure of the cell stack. Thus, a reinforcing effect can
be improved.
[0044] Also, the present inventors have determined that with a
current collector plate of the invention as described above, the
electrical resistivity in the planar direction is smaller than the
electrical resistivity in the thickness direction, i.e., the
stacking direction of the stack. As a result, by compression
molding a composite material of a highly graphitized carbon
material and a binder, the inventors have succeeded in obtaining an
electrically anisotropic current collector plate in which the
electrical resistivity in the planar direction is smaller. This
current collector plate is thin and avoids the performance
deterioration in the prior art device caused by metal ions
discussed above.
[0045] In still another embodiment, the present invention may
include a current collector plate that is integrated with (i.e. of
a one-piece structure with) the adjoining separator. This can
reduce the number of components as well as the loss due to the
electrical resistance caused by contact resistance.
[0046] In another embodiment, the present invention may include a
metal plate that is for connecting a power output coupling such as
a cable and that is clamped to the terminal section of the current
collector plate at two or more points. This can prevent the
cracking of the terminal section of the current collector
plate.
[0047] One example of a current collector plate including a
conductive carbon, which is used in the present invention, is a
conductive carbon plate, such as a commercially available glassy
carbon plate or an expanded graphite plate, which is worked into a
desired predetermined shape by cutting, abrasive blasting or the
like. The conductive carbon plate may have an electrical
resistivity of approximately 1 m.OMEGA.cm or less in the planar
direction. Also, the current collector plate may be made of a
molding material prepared by adding a graphite powder to a binder
which is a thermoplastic resin, such as polyphenylene sulfide or
polypropylene, or a thermoplastic resin, such as epoxy resin or
phenol resin, or a mixture thereof, and is obtained by forming the
molding material into a predetermined shape by compression molding,
injection molding, or the like. It should be noted that in each of
the embodiments described herein, the term "binder" may include
such resins. It is also possible to use a plate obtained by forming
such a molding material in a plate and working the plate into a
predetermined shape by cutting or abrasive blasting. These molded
plates preferably have an electrical resistivity of approximately 5
m.OMEGA.cm or less in the planar direction.
[0048] When molding the separators of a fuel cell, it is desirable,
in terms of material cost reduction, to mold the current collector
plates out of the same molding material as that of the separators.
With regard to the thickness of the current collector plate, the
terminal section and the other part may have a different thickness.
In changing the thickness, it is desirable to employ such a
structure that the difference in thickness is eased by a curved
surface in order to prevent the occurrence of breaking of the
material caused by the concentration of stress on the base portion
of the terminal section. Also, the thickness of the current
collector plate should be at least about 3 to 6 mm to prevent
breakage.
[0049] The present invention is more specifically described below
by way of embodiments.
Embodiment 1
[0050] FIG. 1 shows an example of a polymer electrolyte fuel cell
stack in a first embodiment.
[0051] An electrolyte membrane electrode assembly (MEA) 1 includes
a polymer electrolyte membrane and an anode and cathode sandwiching
the polymer electrolyte membrane. The polymer electrolyte membrane
has a size slightly larger than that of the electrodes. The
periphery of the polymer electrolyte membrane is sandwiched by
gaskets. The MEAs 1 and bi-polar separators are alternately
stacked. Two kinds of separators are used: a single separator 2 has
an oxidant gas flow channel on one side and a fuel gas flow channel
on the other side and serves both as a cathode-side separator and
an anode-side separator, and a composite separator 2A has a coolant
flow channel that is formed between a cathode-side separator 2A-1
and an anode-side separator 2A-2.
[0052] An end plate 5a is joined to the upper end of the cell stack
with a cathode-side current collector plate 3a and an insulator
plate 4a. An end plate 5b is joined to the lower end of the stack
with an anode-side current collector plate 3b and an insulator
plate 4b. End plates 5a and 5b are clamped by bolts 6 and nuts 8,
so that a predetermined load is applied to the cell stack.
Reference character 7 represents a spring. The end plate 5a has
inlets/outlets for the reaction gases and coolant. In FIG. 1, an
oxidant gas outlet 11, a fuel gas inlet 12 and a coolant outlet 13
are illustrated. In this way, a polymer electrolyte fuel cell stack
10 is assembled.
[0053] Current collector plates 3a and 3b have terminal sections
15a and 15b, respectively, which protrude from the side of the cell
stack, and power output couplings or cables 16a and 16b are
connected to these terminal sections by metal fittings 17a and 17b,
respectively. In FIG. 1, current collector plates 3a and 3b are
illustrated as serving also as a cathode-side separator and an
anode-side separator, respectively, but this is not to be construed
as limiting the current collector plates, as specifically described
below.
[0054] FIGS. 2 to 4 illustrate a current collector plate serving
also as a cathode-side separator. FIG. 2 is a front view of the
cathode side of the current collector plate, and FIG. 3 is a back
view thereof. FIG. 4 is a sectional view taken on line IV-IV of
FIG. 2. In FIG. 3, the power output coupling or cable, the metal
plates for connecting the coupling or cable, etc., are omitted.
[0055] A current collector plate 30 has a pair of oxidant gas
manifold apertures 31, a pair of fuel gas manifold apertures 32,
and a pair of coolant manifold apertures 33. The current collector
plate 30 has an oxidant gas flow channel 34 that communicates with
the pair of manifold apertures 31 on the cathode facing side. On
the insulator-plate-facing side, the current collector plate 30 has
grooves 37, 38 and 39 surrounding the manifold apertures 31, 32 and
33, respectively, and O-rings are fitted into these grooves. The
O-rings fitted into these grooves are compressed between the
current collector plate and the insulator plate to prevent leakage
of the gases and coolant from the respective manifold
apertures.
[0056] The current collector plate 30 also has a terminal section
35 with two holes 36, and two metal plates 45 are fastened to the
terminal section so as sandwich it with threaded fasteners 46 and
nuts 47. Reference character 48 represents a spring washer, and
reference character 49 represents a flat washer. A core wire 41 of
a power output coupling or cable 40 is connected to the metal
plates 45 with solder 42. In FIG. 2, with respect to the pair of
oxidant gas manifold apertures 31 and the pair of fuel gas manifold
apertures 32, the one closer to the terminal section 35 is the
inlet-side manifold aperture.
[0057] With regard to the connecting points between the terminal
section 35 of the current collector plate 30 and the metal plates
45 for connecting the power output coupling or cable, there is no
particular limitation, but the connecting points are preferably two
or more, as illustrated in FIGS. 2 and 3. The reason is that this
equalizes the pressure of the contact surface, thereby lessening
the loss caused by the resistance and leveling out the stress
produced by clamping. Also, in addition to connecting the metal
plates to both sides of the terminal section as described above,
the metal plate may be connected to only one side of the terminal
section. However, connecting the metal plates to both sides
produces the effect of increasing the contact surface and reducing
the contact resistance. Furthermore, this equalizes the stress
applied to the terminal section and therefore produces the effect
of preventing the breaking caused by excessive clamping.
[0058] FIG. 5 shows another example of connecting the power output
coupling or cable 40 to the terminal section 35 of the current
collector plate 30. Terminal section 35 of current collector plate
30 is fitted into a U-shaped metal fitting 43, to which coupling or
cable 40 is soldered, and they are fastened together with a screw
44 going through hole 36.
[0059] In this embodiment, the fuel cell stack is clamped using a
clamping structure of bolts, springs and nuts, but other clamping
devices may be employed. The power output coupling or cable is
connected to the terminal section of the current collector plate by
making holes in the terminal section and connecting the metal
plates thereto with threaded fasteners and nuts, but it may be
connected by other methods. For example, it may be connected by
making a screw hole in the terminal section 35 and screwing a
pressure terminal, connected to the power output coupling or cable,
in the hole. Any other connecting methods capable of stable
electrical connection may also be employed.
[0060] Also, the power output coupling or cable and the metal
plates for connecting the coupling or cable are connected with
solder, but they may be connected by any method capable of
achieving good electrical connection, e.g., joining through
pressure by caulking. As a material of the metal plates for
connecting the coupling or cable, a metallic material having low
contact resistance may be used. For example, metal having low
electrical resistance and good workability, such as phosphor bronze
or copper, may be used.
[0061] FIG. 1B three-dimensionally shows the flow of the oxidant
gas through the cell stack of the fuel cell as illustrated in FIG.
1A. The front side of FIG. 1B corresponds to the upper side of FIG.
1A.
[0062] In FIG. 1B, 31A represents an oxidant gas inlet-side
manifold, and 31B represents an oxidant gas outlet-side manifold.
The inlet-side manifold 31A communicates with the inlet-side
manifold aperture of the pair of oxidant gas manifold apertures 31
of the cathode-side current collector plate 3a. The outlet-side
manifold 31B communicates with the oxidant gas outlet-side
aperture.
[0063] The oxidant gas, to be supplied to the fuel cell, is
introduced into the inlet-side manifold 31A of the cell stack from
the oxidant gas inlet formed in the end plate 5a. From the manifold
31A, the oxidant gas flows as indicated by the arrow OxA in FIG. 1B
and flows into the respective gas flow channels of the cells. That
is, in the foremost cell, the oxidant gas is introduced into the
gas flow channel of the current collector plate 3a (which
corresponds to 34 of FIG. 2), as indicated by the arrow C1 in FIG.
1B. In the rearmost cell, i.e., the cell adjacent to the current
collector plate 3b, the oxidant gas is introduced into the gas flow
channel of the cathode-side separator of this cell, as indicated by
the arrow Cn. From the gas flow channels of the respective cells,
the oxidant gas diffuses through the respective cathodes, where it
reacts electrochemically. The unreacted oxidant gas and the water
generated by the reaction gather into the outlet-side manifold 31B
from the gas flow channels of the cells, and they flow as indicated
by the arrow OxE and exit from the outlet 11 of the end plate
5a.
[0064] The fuel gas is introduced into an inlet-side manifold 32A
communicating with one of the pair of manifold apertures 32 of FIG.
2. Then, the fuel gas flows into the respective gas flow channels
of the cells and diffuses through the respective anodes, where it
reacts electrochemically. The unreacted gas gathers into an
outlet-side manifold 32B communicating with the other manifold
aperture 32 of FIG. 2, and exits from the outlet of the end plate
5a. Reference characters 33A and 33B represent an inlet-side
manifold and an outlet-side manifold, respectively, for cooling
water.
[0065] In FIG. 1B, the oxidant gas, fuel gas, and cooling water are
introduced from the end plate 5a side and discharged from the same
end plate 5a side.
[0066] FIG. 1C shows a different flow of gas from that of FIG. 1B.
That is, the fuel and oxidant gases and cooling water are
introduced from one of the end plates and discharged from the other
end plate. In this figure, the oxidant gas is introduced into an
inlet-side manifold 31A' from the front side, and the unreacted
gas, which has gathered into an outlet-side manifold 31B', is
discharged from the rear side. Likewise, the fuel gas is introduced
into an inlet-side manifold 32A' from the front side, and the
unreacted gas, which has gathered into an outlet-side manifold
32B', is discharged from the rear side. Reference characters 33A'
and 33B' represent an inlet-side manifold and an outlet-side
manifold, respectively, for cooling water.
[0067] The manifold apertures of the current collector plate that
are not related to the introduction and discharge of the gases to
and from the cell stack, as illustrated in FIGS. 1B and 1C, are
closed by the adjacent insulator plate located outside the current
collector plate. The current collector plate serving also as a
separator, as illustrated in FIG. 2, has inlet-side and outlet-side
manifold apertures for each of the fuel gas, oxidant gas and
cooling water. However, there is no need to provide a current
collector plate with gas manifold apertures, if the current
collector plate is not related to the introduction and discharge of
the gases. This also applies to cooling water manifold
apertures.
Embodiment 2
[0068] A method for reducing the resistance loss at the terminal
section of the current collector plate is now described.
[0069] FIG. 6 is a front view of the cathode side of a current
collector plate in this embodiment. A current collector plate 30A
has a metal film 50 of about 1 .mu.m in thickness formed on each
side of a terminal section 35. Except for this, plate 30A has the
same structure as the current collector plate 30 of FIG. 2. Metal
film 50 makes it possible to reduce the contact resistance, for
example, between terminal section 35 of the current collector plate
and the metal plate for connecting the power output coupling or
cable.
[0070] FIG. 7 shows still another example of the current collector
plate. A current collector plate 30B has a metal film 51 of about
1-100 .mu.m in thickness substantially on the whole surface of the
side facing insulator plate 4a. Metal film 51 makes it possible to
improve the conductivity in the plane direction of the current
collector plate and further reduce the resistance loss. In this
case, in order to prevent the performance deterioration caused by
the leaching of metal ions, it is desirable not to form the metal
film at locations contacting the oxidant gas, fuel gas and coolant.
In this case, the metal film is not formed around grooves 37, 38
and 39, which surround the respective manifold apertures and to
which O-rings are fitted As the metal forming the metal film, a
conductive material such as copper and aluminum may be used. The
film may be formed, for example, by vapor deposition or thermal
spraying, and thermal spraying is preferable because it can form a
film of a predetermined thickness in a short period of time. Except
for this, current collector plate 30B has the same structure as
collector plate 30 of Embodiment 1.
[0071] FIG. 8 illustrates an insulator plate to be disposed on the
backside of the current collector plate of FIG. 2 or FIG. 6. An
insulator plate 60 has a pair of oxidant gas manifold apertures 61,
a pair of fuel gas manifold apertures 62, and a pair of coolant
manifold apertures 63.
Embodiment 3
[0072] This embodiment describes a current collector plate that is
independent of a separator. The current collector plate and the
separator are separate pieces.
[0073] FIG. 9 is a front view of an anode-side separator, and FIG.
10 is a front view of a current collector plate in contact with the
anode-side separator. FIG. 12 is a front view of a cathode-side
separator, and FIG. 13 is a front view of a current collector plate
in contact with the cathode-side separator.
[0074] An anode-side separator 110 has a pair of oxidant gas
manifold apertures 111, a pair of fuel gas manifold apertures 112,
and a pair of coolant manifold apertures 113. Separator 110 further
has a fuel gas flow channel 116 communicating with the pair of
manifold apertures 112 on the anode facing side. A current
collector plate 120 to be disposed on the backside of the separator
110 has a pair of oxidant gas manifold apertures 121, a pair of
fuel gas manifold apertures 122, and a pair of coolant manifold
apertures 123. The current collector plate 120 has a terminal
section 125 in the vicinity of the inlet-side manifold aperture
(the upper left manifold aperture in the figure, as is clear from
the arrows in FIG. 12 showing the direction of the gas flow) of the
pair of fuel gas manifold apertures of the separator 110, the
terminal section 125 protruding outward. A coating layer 127
including a good electrical conductor is provided at the terminal
section 125 and its adjacent part, i.e. a region 126 corresponding
to the inlet-side manifold aperture of the separator 110 and the
inlet-side part of the gas flow channel communicating therewith.
Region 126 is thinner than the other part such that it becomes as
thick as the other part when the coating layer 127 is formed on
each side of region 126. Terminal section 125 has holes 128 which
are for mounting the metal plates and which are used for connecting
the power output coupling or cable.
[0075] A cathode-side separator 130 has a pair of oxidant gas
manifold apertures 131, a pair of fuel gas manifold apertures 132,
and a pair of coolant manifold apertures 133. Separator further has
an oxidant gas flow channel 134 communicating with the pair of
manifold apertures 131 on the cathode facing side. A current
collector plate 140 to be disposed on the backside of the separator
130 has a pair of oxidant gas manifold apertures 141, a pair of
fuel gas manifold apertures 142, and a pair of coolant manifold
apertures 143. Current collector plate 140 has a terminal section
145 in the vicinity of the inlet-side manifold aperture (the upper
right manifold aperture in the figure) of the pair of oxidant gas
manifold apertures 131 of separator 130, with terminal section 145
protruding outwardly. A coating layer 147 comprising a good
electrical conductor is provided at terminal section 145 and its
adjacent parts i.e., a region 146 corresponding to the inlet-side
manifold aperture of separator 130 and the inlet-side part of the
gas flow channel communicating therewith. Region 146 is thinner
than the other part such that it becomes as thick as the other part
when coating layer 147 is formed on each side of region 146.
Terminal section 145 has holes 148 for mounting the metal plates
for connecting the power output coupling or cable. As is seen in
FIGS. 12 and 13, the metal plate 147 constituting the coating layer
extends so as to overlap the separator 130 in the fuel cell stack,
enabling metal plate 147 to have applied thereto the clamping
pressure of the cell stack. Thus, a structural reinforcing effect
can be improved.
[0076] As is clear from FIGS. 9 and 10, coating layer 127 of
terminal section 125 of current collector plate 120 extends to the
part of current collector plate 120 corresponding to the inlet-side
part of gas flow channel 116 of separator plate 110. Coating layer
127 including a metal film or a metal plate has smaller electrical
resistance than the other part of current collector plate 120
formed mainly of the carbon material. Thus, when current is output
from terminal section 125 during power generation, the current
density is higher at the above-described part of current collector
plate 120 corresponding to the inlet-side part of gas flow channel
116 of separator plate 110. Thus, the electrode reaction of the
cell proceeds more actively on the inlet side of gas flow channel
116. Likewise, on the cathode side, it proceeds more actively on
the inlet side of gas flow channel 134. In this way, in the
respective cells, the amount of water generated by the reaction
becomes increased in the vicinity of the inlet-side gas manifold
aperture, so that the reaction gases supplied to its downstream are
humidified.
[0077] As illustrated in FIGS. 10 and 13, it is preferable that
terminal section 125 of the anode-side current collector plate and
terminal section 145 of the cathode-side current collector plate
face each other, i.e., the inlet-side fuel gas manifold aperture
and the inlet-side oxidant gas manifold aperture are preferably in
close proximity to each other.
[0078] FIGS. 15 to 18 show modified examples of the combination of
the separator and the current collector plate.
[0079] An anode-side separator 110A of FIG. 15 is the same as
separator 110 of FIG. 9 except that the position of oxidant
manifold apertures 111A is changed. Referring now to FIG. 16, a
current collector plate 120A to be disposed on the backside of
separator 110A is the same as current collector plate 120 of FIG.
10 except that the position of oxidant manifold apertures 121A is
changed and the shape of coating layers 127A is slightly
different.
[0080] Also, a cathode-side separator 130A of FIG. 17 is the same
as separator 130 of FIG. 12 except that the position of oxidant
manifold apertures 131A is changed. Referring now to FIG. 18, a
current collector plate 140A to be disposed on the backside of
separator 130A is the same as current collector plate 140 of FIG.
13 except that the position of oxidant manifold apertures 141A is
changed and the shape of coating layers 147A is slightly
different.
[0081] Each of coating layers 127, 127A, 147 and 147A may include a
metal film as described in Embodiment 2. However, in a more
preferable mode, the coating layer may include a metal plate.
[0082] It is preferable that part of the coating layer including a
metal plate is positioned inside the projected area of the
separator when stacked on the current collector plate, as
illustrated in FIG. 9. In other words, the metal plate overlaps the
separator in the fuel cell stack. In this case, the clamping load
of the stack is applied to the metal plate of the coating layer via
the separator and the current collector plate. As a result, the
metal plates of the coating layers are firmly secured to the extent
provided by the clamping load of the stack. Since the metal plates
also cover the terminal section of the current collector plate,
they can serve to effectively alleviate the stress applied to the
base portion of the terminal section by the coupling or cable
connected to the terminal section.
[0083] It is preferable that the metal plates be bonded to the
current collector plate with an adhesive having elasticity, such as
a conductive adhesive or a silicone adhesive. Insulating adhesives,
such as silicone adhesive, conveniently restrict the current
density of a specific part of the current collector plate when
interposed between the current collector plate and the metal
plate.
[0084] FIG. 19 shows an example of bonding metal plates 127 to the
region 126 of current collector plate 120 with a conductive
adhesive 129. As illustrated therein, when the metal plates are
fixed to the current collector plate with the adhesive such that
there are no gaps between the current collector plate and the metal
plates, the stress, mechanical or electrical, applied to the
terminal section is effectively alleviated. When the metal plates
are bonded to the current collector plate with the conductive
adhesive, it has been confirmed that the voltage between the
current collector plates at both ends of the stack is higher than
that for a similar structure without the adhesive, by about 5 mV,
at the time of an output of a current of 30 A by the terminal
sections of the current collector plates.
Embodiment 4
[0085] FIGS. 20 and 21 illustrate current collector plates of this
embodiment that are independent of a separator. The current
collector plate and the separator are separate pieces.
[0086] FIG. 20 is a front view of an anode-side current collector
plate 120B which has the same structure as the current collector
plate of FIG. 10 except that it does not have a coating layer 127
at a terminal section 1253 and its adjoining part, and it is
disposed on the backside of the anode-side separator 110 of FIG.
9.
[0087] FIG. 21 is a front view of a cathode-side current collector
plate. Current collector plate 140B has the same structure as the
current collector plate of FIG. 13 except that it does not have the
coating layer 147 at a terminal section 145B and its adjoining
part, and it is disposed on the backside of the cathode-side
separator 130 of FIG. 12.
[0088] Each of these current collector plates includes a molded
plate of a composite material of a conductive carbon material and a
binder. Therefore, during power generation, the current density
becomes higher in the vicinity of the terminal section, i.e., in
the vicinity of the inlet-side gas manifold aperture, which
produces the effect of humidifying the gases in the same manner as
in Embodiment 3. The binder is, for example, a thermoplastic resin,
such as polyphenylene sulfide or polypropylene, or a thermoplastic
resin, such as epoxy resin or phenol resin, or a mixture
thereof.
Embodiment 5
[0089] This embodiment is directed to an example of a current
collector plate serving also as a separator.
[0090] FIG. 22 is a front view of a current collector plate serving
also as an anode-side separator, and FIG. 23 is a back view
thereof. Current collector plate 150 has a pair of oxidant gas
manifold apertures 151, a pair of fuel gas manifold apertures 152,
and a pair of coolant manifold apertures 153, and has a fuel gas
flow channel 156 communicating with the pair of manifold apertures
152 on the anode facing side. Current collector plate 150 has a
terminal section 155 in the vicinity of the inlet-side manifold
aperture (the upper left manifold aperture in FIG. 22) of the pair
of fuel gas manifold apertures 152, and it has a coating layer 157
extending to the vicinity of the nearby manifold aperture 151 on
the backside. This coating layer has the same structure, for
example, as the coating layer of current collector plate 120 as
described in Embodiment 3 except it is formed only on the backside
of the current collector plate. The terminal section 155 has holes
158 which are for mounting the metal plates and which are used for
connecting the power output coupling or cable.
[0091] Although this embodiment has described the anode-side
current collector plate, it will be apparent to those skilled in
the art that a current collector plate serving as a cathode-side
separator can also be formed in the same manner.
Embodiment 6
[0092] This embodiment describes a current collector plate into
which a metal plate serving as a core member is buried. The current
collector plate of this embodiment may be independent of the
separator, as in the embodiments of FIGS. 9-21, or may also serve
as the separator as in the embodiments of FIGS. 2-7 and 22.
[0093] FIG. 24 is a front view of a current collector plate of this
embodiment, and FIG. 25 is a sectional view taken on line XXV-XXV
of FIG. 24. Current collector plate 160 is produced by molding a
molding material of a conductive carbon material and a binder so as
to surround a metal plate 167 serving as a core member. The binder
is, for example, a thermoplastic resin, such as polyphenylene
sulfide or polypropylene, or a thermoplastic resin, such as epoxy
resin or phenol resin, or a mixture thereof. Current collector
plate 160 has a pair of oxidant gas manifold apertures 161, a pair
of fuel gas manifold apertures 162, and a pair of coolant manifold
apertures 163, and further has a terminal section 165 protruding
sideward. A metal plate 167 buried in current collector plate 160
has a smaller external size than the current collector plate 160
such that metal plate 167 is not exposed outside. As illustrated in
FIG. 25, the metal plate 167 is so structured that, for example,
its apertures corresponding to manifold apertures 162 and 163 of
current collector plate 160 are larger than the manifold apertures
162 and 163. Therefore, no part of the metal plate is exposed to
the outside, even at its apertures.
[0094] FIG. 26 shows an example of forming a good electrical
conductor layer 169 on the surface of core metal plate 167. This
layer 169 makes it possible to reduce the contact resistance
between the layer comprising the molding material and the core
metal plate 167 and to improve the electrical characteristics of
current collector plate 160. Layer 169 can be formed by removing
the oxides on the surface of core metal plate 167 and forming a
layer of noble metal, conductive inorganic oxide, conductive
inorganic nitride, or conductive inorganic carbide on core metal
plate 167.
Example
[0095] The following describes an example of molding a current
collector plate performed using a molding conductive material of a
mixture of 80 percent by weight (wt %) graphite and 20 wt % phenol
resin, in which a core metal plate 167 was buried.
[0096] First, 50 g of a molding compound was evenly charged into a
mold and was compressed preliminarily at a mold clamping pressure
of 100 kgf/cm.sup.2. At this time, the temperature of the mold was
70.degree. C. Next, the mold was opened, and a metal plate was
inserted into the mold. Then, 50 g of the molding compound was
charged therein to embed the metal plate in the molding compound.
Then, the mold was clamped at a mold clamping pressure of 500
kgf/cm.sup.2, and the temperature was raised to 160.degree. C. for
a sufficient period of time to produce the current collector plate.
The resultant current collector plate had greater strength and
lower electrical resistance than the current collector plate molded
only of the conductive molding material (7 mm in thickness), and,
hence, it became possible to reduce the thickness of the current
collector plate to 4 mm.
[0097] As the core member, a brass plate of 2 mm in thickness was
used. The current collector plate had a pair of manifold apertures
for each of the oxidant gas, fuel gas and coolant, as illustrated
in FIG. 24. Since the inner faces forming the manifold apertures
were covered with the conductive molding material, the core metal
plate was prevented from coming in contact with the fluids flowing
through the respective manifold apertures.
[0098] A stack including these current collector plates was
assembled, and using pure water as the coolant, a power generation
test was performed for 100 hours. The number of stacked cells was
50. As a comparative example, a stack of 50 cells having current
collector plates made only of brass was also tested in the same
manner. As a result, corrosion was observed on the inner faces of
the coolant manifold apertures formed in the brass current
collector plates of the comparative example, but corrosion was not
observed on the inner faces of the manifold apertures in the
current collector plates of this example. The pure water used as
the coolant was analyzed after the test. As a result, from the
cooling water of the stack having the brass current collector
plates, copper ions of 100 ppm and zinc ions of 80 ppm were
detected. In contrast, from the coolant of the stack of this
example, no metal ions were detected. By covering a metal core
member with a conductive molding material, it becomes possible to
ensure the strength and electrical conductivity of the current
collector plate and reduce the cost and the leaching of
impurities.
[0099] Using the above process, a different wt % of graphite and
resin than that specified above may be used, and resins other than
phenol resins may be employed as the binder, to produce a molded
plate of a composite material of a conductive carbon material and a
binder according to this invention. With respect to phenol resin,
epoxy resin, unsaturated polyester resin, polyphenylene sulfide,
and liquid crystal polymer, when the resin is 65 to 85% by weight
and graphite is 35 to 15% by weight, preferable current collector
plates are obtained.
[0100] Examples of forming a good electrical conductor layer on the
surface of a core metal plate are specifically described below.
Examples
[0101] (1) A layer of platinum or gold having a thickness of 120
.ANG. was formed on the surface of a brass plate, having a
thickness of 1 mm, by a sputtering method using an RF-planar
magnetron. As the target, platinum (99%) or gold (99%) was used,
and the substrate temperature was 500.degree. C. The sputtering
atmosphere was Ar (99.9999%) of 4.times.10.sup.-2 Torr, the
sputtering power was 400 W, and the deposition rate was 1.5
.mu.m/hr.
[0102] (2) A TiN layer having a thickness of 1 .mu.m was formed on
the surface of a Ti plate, having a thickness of 1 mm, by a
sputtering method using an REF-planar magnetron. As the target, TiN
(99%) was used, and the substrate temperature was 500.degree. C.
The sputtering atmosphere was Ar (99.9999%) of 4.times.10.sup.-2
Torr, the sputtering power was 400 W, and the deposition rate was
1.5 .mu.m/hr. The resultant sputtered layer was identified as TiN
by structural analysis of X-ray diffraction. The resistivity of the
TiN layer obtained by this method was 2.times.10.sup.-4
.OMEGA.cm.
[0103] (3) A Ti--Al--N layer having a thickness of 1.2 .mu.m was
formed on the surface of an Al plate, having a thickness of 1 mm by
a sputtering method using an RF-diode. As the target, Ti--Al--N
(99%) was used, and the substrate temperature was 300.degree. C.
The sputtering atmosphere was Ar (99.999%) of 4.times.10.sup.-2
Torrr the sputtering power was 300 W, and the deposition rate was
1.0 .mu.m/hr. The resistivity of the Ti--Al--N layer obtained by
this method was 1.times.10.sup.-3 .OMEGA.cm.
[0104] (4) A method of forming an n-type doped SiC layer on a metal
substrate is described. The layer was formed by a high-frequency
glow discharge decomposition method of 14.56 MHz, and the gas to be
decomposed was a mixture of silane, methane (CH.sub.4) and diborane
(PH.sub.3) in such a ratio that P/(Si+C)=10 atomic %, the mixture
having a pressure of 10 Torr. The substrate temperature was
300.degree. C. At this time, by controlling the deposition time,
the resultant n-type doped SiC layer had a thickness of 1,000
.ANG.. After the formation of the layer, a gold electrode was
deposited on the SiC layer, and the resistivity of the SiC layer
was measured and turned out to be 50 .OMEGA.cm.
[0105] (5) A Pb layer having a thickness of 1 .mu.m was formed on
the surface of a stainless steel SUS 316 plate, having a thickness
of 1 mm, by a vacuum deposition method. The layer was deposited in
an Ar (99.9999%) atmosphere of 1.times.10.sup.-7 Torr at a
substrate temperature of 200.degree. C. Subsequently, a PbO layer
was formed on the Pb deposited surface of the Pb deposited
stainless steel plate by a sputtering method. The layer was formed
in an Ar (99.9999%) atmosphere having an oxygen partial pressure of
2.times.10.sup.-4 Torr at a substrate temperature of 200.degree.
C., and the sputtering power was controlled such that the
deposition rate was 3 .mu.m/hr. The resultant sputtered layer was
identified as PbO by structural analysis of X-ray diffraction, The
resistivity of the PbO layer obtained by this method was
5.times.10.sup.-5 .OMEGA.cm.
[0106] Also, in an example of using tin oxide, an In-doped tin
oxide layer having a thickness of 0.5 .mu.m was formed on the
surface of a stainless steel SUS 316 plate, having a thickness of 1
mm, by a vacuum electron beam deposition method. The deposition was
performed in an Ar gas atmosphere having a vacuum degree of
5.times.10.sup.-6 Torr at a substrate temperature of 300.degree.
C.
[0107] As described above, it has been confirmed that the current
collector plate molded of the carbon molding material in which the
surface-treated core metal plate is buried has better electrical
characteristics and smaller voltage loss than the current collector
plate having the untreated metal plate.
Embodiment 7
[0108] This embodiment describes an example of integrally forming a
current collector plate and an end plate for clamping the stack. In
this embodiment, the thickness of the current collector plate is
increased in the stacking direction of the stack in order to keep
the electrical resistance extremely low. Such plate is similar to
those of FIGS. 20 and 21 except having increased thickness to
provide an integral current collector plate serving also as an end
plate, as a one-piece element. This embodiment will be described by
way of the following example.
[0109] The current collector plate was made of a graphite plate
having a thickness of 70 mm and an electrical resistivity of 1
m.OMEGA.cm in the plane direction and 100 mcm in the thickness
direction. With the plate as thick as 70 mm, a cell stack including
the current collector plates was clamped by clamping members such
as bolts, nuts and springs at a predetermined load. In such
assembly, the clamping surface pressure applied to the electrode
was checked with pressure-sensitive paper beforehand, and it was
found that a surface pressure of 10 kgf/cm.sup.2 was applied to the
electrode and that the current collector plates had no cracking,
remarkable distortion, or the like. A 0.5 mm thick tape made of
polytetrafluoroethylene is wound around the bolt, and a 5 mm thick
spacer made of polyphenylene sulfide is interposed between the
current collector plate and the spring. In this way, a polymer
electrolyte fuel cell stack was formed.
[0110] The current collector plates have a terminal section at one
end, and a power output coupling or cable is connected to the
terminal section. The specific structure of the terminal section
can be the same as that of Embodiment 1.
[0111] The stack was tested by securing it to an evaluation table,
using a part of the clamping bolts, and an oxidant gas, a fuel gas
and a coolant were supplied to the stack to generate electric
power. As a result, it was confirmed that the stack could
successfully generate a current up to a current density of 0.3
A/cm.sup.2.
[0112] Embodiment 7 is directed to the example of a current
collector plate integrated with an end plate, but this current
collector plate may be made to serve also as a separator by forming
a gas flow channel on the anode or cathode facing side. Such plate
is similar to that of FIGS. 2 and 3 with a thickness to provide an
integral current collector plate and separator as one-piece
element.
[0113] The foregoing description illustrates and describes the
present invention with respect to only the preferred embodiments of
the invention. But it is to be understood that the invention is
capable of use in various other combinations, modifications, and
environments. Also, the invention is capable of change or
modification, within the scope of the inventive concept, that is
commensurate with the above teachings and the skill or knowledge of
one skilled in the relevant art.
[0114] The embodiments described herein are further intended to
explain best modes known of practicing the invention and to enable
others skilled in the art to utilize the invention in these and
other embodiments with various modifications that may be required
by the particular applications or uses of the invention.
Accordingly, the description is not intended to limit the invention
to the form disclosed herein.
INDUSTRIAL APPLICABILITY
[0115] The present invention provides a current collector plate
composed mainly of a conductive carbon material which is low-cost,
lightweight, and free from metal corrosion in manifold apertures.
Particularly, by providing a terminal section in the vicinity of an
inlet-side manifold aperture for a reaction gas, the electrodes are
humidified by water generated by the reaction on the inlet side of
the reaction gas supplied to the electrodes. As a result, the
durability of the electrodes is improved. Also, by forming a gas
flow channel on one side of the current collector plate, the
current collector plate can be integrated with the separator
positioned at the end, so that the number of parts and the power
generation loss due to the resistance components can be decreased.
Accordingly, it is possible to reduce the cost of a polymer
electrolyte fuel cell and improve the volume and weight efficiency
thereof.
[0116] This application is based on Japanese Patent Application No.
2002-114552 filed on Apr. 17, 2002 and PCT/JP03/04723 filed Apr.
14, 2003, the entire technical contents of which are expressly
incorporated by reference herein.
* * * * *