Technical Field
[0001] The present invention relates to a fuel cell formed by stacking an electrolyte electrode
assembly and a separator. The electrolyte electrode assembly includes an anode, a
cathode, and an electrolyte interposed between the anode and the cathode. Further,
the present invention relates to a fuel cell stack formed by stacking a plurality
of fuel cells.
Background Art
[0002] Typically, a solid oxide fuel cell (SOFC) having a seal free (sealless) structure
employs an electrolyte made up of an ion-conductive solid oxide such as stabilized
zirconia. The electrolyte is interposed between an anode and a cathode to form an
electrolyte electrode assembly. The electrolyte electrode assembly is interposed between
separators (bipolar plates). In use, a predetermined number of electrolyte electrode
assemblies and separators are stacked together to form a fuel cell stack.
[0003] The operating temperature of the fuel cell is high, about 800°C. Therefore, when
the consumed fuel gas (hereinafter also referred to as the off gas, wherein the off
gas contains unconsumed reactant gases therein) is discharged to an area around the
fuel cell stack, and is mixed with an oxygen-containing gas to induce combustion,
the temperature of the fuel cell stack becomes high locally. Under these circumstances,
operation of the fuel cell stack cannot be performed stably. Further, water produced
during combustion makes contact locally with the heated separator, causing corrosion
of the separator. As a result, durability of the separator becomes low. Moreover,
in the electrolyte electrode assembly, in particular, the locally heated anode is
oxidized. Thus; cracks occur in the electrolyte electrode assembly, and the performance
is degraded undesirably.
[0004] In this regard, a solid oxide fuel cell, as disclosed in Japanese Laid-Open Patent
Publication No.
2005-85520, is known. As shown in FIG. 24, the fuel cell is formed by stacking a power generation
cell 1, a fuel electrode current collector 2, an air electrode current collector 3,
and separators 4a, 4b. The power generation cell 1 includes a fuel electrode layer
1b, an air electrode layer 1c, and a solid electrolyte layer 1a interposed between
the fuel electrode layer 1b and the air electrode layer lc. The fuel electrode current
collector 2 is provided outside the fuel electrode layer 1b, and the air electrode
current collector 3 is provided outside the air electrode layer lc.
[0005] The separator 4a includes a fuel gas channel 5 for supplying a fuel gas substantially
from a center portion of the surface of the separator 4a, which faces the fuel electrode
collector 2. The separator 4b has an oxygen-containing gas channel 6 for supplying
an oxygen-containing gas substantially from a center portion of the separator 4b,
which faces the air electrode current collector 3.
[0006] Although not shown, a ring shaped metal cover covers the outer circumferential portion
of a circular porous metal body, wherein a large number of gas discharge holes 7 are
provided over the entire side portion of the cover.
[0007] In this structure, gas is discharged from the outer circumferential portion of the
fuel electrode current collector 2 only through the gas discharge holes 7. Thus, the
fuel gas diffuses into the porous metal body and is not emitted from the entire outer
circumferential portion of the fuel electrode current collector 2. According to the
disclosure, an amount of the fuel gas, which is not used during power generation,
and which is discharged from the outer circumferential portion, is suppressed, and
thus it is possible to prevent back diffusion of air toward the fuel electrode.
[0008] However, in the above conventional technique, the separator 4a is stacked on the
fuel electrode collector 2, whereby the exhaust gas discharged from the gas discharge
holes 7 is combusted near the separator 4a so as to produce water. Thus, the separator
4a and the power generation cell 1 are heated locally, and tend to be damaged easily
due to steam oxidation. Corrosion may also occur, which uneconomically degrades the
performance of the fuel cell.
[0009] EP 0355420 A1 discloses fuel cells formed by stacking an electrolyte electrode assembly and a separator.
A fuel gas channel is formed on one surface of the separator. An oxygen-containing
gas channel is formed on the other surface of the separator.
Disclosure of Invention.
[0010] In order to address and solve the above problems, an object of the present invention
is to provide a fuel cell and a fuel cell stack having a simple structure, in which
it is possible to reliably prevent an electrolyte electrode assembly and a separator
from contacting water vapor produced during the reaction, thereby effectively preventing
damage of the electrolyte electrode assembly and the separator.
[0011] The present invention relates to a fuel cell formed by stacking an electrolyte electrode
assembly and a separator. The electrolyte electrode assembly includes an anode, a
cathode, and an electrolyte interposed between the anode and the cathode. A fuel gas
channel for supplying a fuel gas along a surface of the anode is formed on one surface
of the separator, and an oxygen-containing gas channel for supplying an oxygen-containing
gas along a surface of the cathode is formed on the other surface of the separator.
[0012] The fuel gas channel has an end point at a position corresponding to an outer circumferential
portion of the electrolyte electrode assembly, wherein the end point of the fuel gas
channel is connected to a fuel gas discharge channel for emitting the fuel gas consumed
in the electrolyte electrode assembly, from a position spaced outwardly from the outer
circumferential portion of the electrolyte electrode assembly.
[0013] The fuel gas discharge channel comprises a through hole extending through the separator
and a discharge groove ember provided on the other surface of the separator, wherein
the discharge groove member is connected to the through hole and extends outwardly
from the electrolyte electrode assembly.
[0014] A ring shaped protrusion is provided on one surface of the separator in tight contact
with an outer circumferential portion of the anode. As a result of this structure,
it is possible to prevent entry of the exhaust gas (containing the consumed fuel gas
and the consumed oxygen-containing gas) into the outer circumferential portion of
the anode, so that degradation of the anode due to oxidation can be prevented.
[0015] Preferably, the fuel gas channel includes a channel unit provided on one surface
of the separator, wherein the channel unit is connected from a fuel gas inlet to the
fuel gas discharge channel.
[0016] Further, preferably, the fuel gas discharge channel is formed by a discharge groove
provided on one surface of the separator, and connected to the fuel gas channel, and
a lid member provided on one surface of the separator so as to cover the discharge
groove.
[0017] Further, preferably, the channel unit is formed by a groove, a plurality of protrusions,
or a deformable elastic channel member, which tightly contacts the anode.
[0018] Further, preferably, the oxygen-containing gas channel is formed by a deformable
elastic channel member, which is provided on the other surface of the separator in
tight contact with the cathode. As a result of this structure, the cathode tightly
and suitably contacts the separator, whereby an improvement in the performance of
collecting electricity from the fuel cell is achieved.
[0019] Further, preferably, an area where the elastic channels member is provided is smaller
than a power generation area of the anode. In this structure, even if the exhaust
gas flows around to the anode of the electrolyte electrode assembly, the power generation
area is not present within the outer circumferential edge of the cathode, which is
opposite to the outer circumferential edge of the anode. Thus, it is possible to prevent
losses in collected electricity, whereby an improvement in the performance of collecting
electricity from the fuel cell is achieved.
[0020] Further, preferably, the elastic channel member is an electrically conductive mesh
member or a felt member. In this case, a simplified and economical structure can be
provided.
[0021] Further, preferably, the oxygen-containing gas channel is formed by a plurality of
protrusions provided on the other surface of the separator. A load imposed in the
stacking direction is efficiently transmitted through the protrusions, whereby an
improvement in the performance of collecting electricity from the fuel cell is achieved.
[0022] Further, preferably, the protrusions are constituted by a plurality of solid portions,
which are formed on one surface of the separator by etching. Thus, the shape and the
positions of the protrusions can be changed arbitrarily and easily, whereby an improvement
in the performance of collecting electricity from the fuel cell is achieved.
[0023] Preferably, the fuel cell further comprises an exhaust gas channel for discharging
the fuel gas and the oxygen-containing gas, which are consumed during the reaction
in the electrolyte electrode assembly, as an exhaust gas in a stacking direction of
the electrolyte electrode assembly and the separator. Further, an oxygen-containing
gas supply unit is provided as a passage of the oxygen-containing gas before consumption,
for supplying the oxygen-containing gas in the stacking direction to the oxygen-containing
gas channel. A fuel gas supply unit is provided hermetically with respect to the oxygen-containing
gas supply unit, wherein a fuel gas supply channel connects the fuel gas channel and
the fuel gas supply unit, and is disposed along the separator surface so as to intersect
with the oxygen-containing gas supply unit that extends in the stacking direction.
In this structure, the fuel gas prior to consumption is heated beforehand by the heat
of the exhaust gas. Thus, an improvement in heat efficiency is achieved.
[0024] Further, preferably, the exhaust gas channel is provided around the separator. In
this structure, heat insulation is provided around the fuel cell, whereby an improvement
in heat efficiency is achieved.
[0025] Preferably, the fuel gas supply unit is provided hermetically at a center portion
of the separator, and the oxygen-containing gas supply unit is provided at an inner
region of the separator. In this structure, the oxygen-containing gas flows outwardly
from the inner region of the separator. Therefore, the exhaust gas is suitably discharged
to the outside of the separator. Further, preferably, the fuel gas inlet is provided
at the center of the electrolyte electrode assembly.
[0026] Preferably, the fuel cell further comprises an exhaust gas channel for discharging
the fuel gas and the oxygen-containing gas consumed during the reaction in the electrolyte
electrode assembly as an exhaust gas in a stacking direction of the electrolyte electrode
assembly and the separator. Further, an oxygen-containing gas supply unit is provided
as a passage of the oxygen-containing gas before consumption, for supplying the oxygen-containing
gas in the stacking direction to the oxygen-containing gas channel. The fuel gas supply
unit and the oxygen-containing gas supply unit are provided hermetically within the
exhaust gas channel, wherein the fuel gas supply channel connects the fuel gas channel
and the fuel gas supply unit, and is provided along the separator surface so as to
intersect with the exhaust gas channel that extends in the stacking direction, and
wherein the oxygen-containing gas supply channel connects the oxygen-containing gas
channel and the oxygen-containing gas supply unit, and is provided along the separator
surface so as to intersect with the exhaust gas channel.
[0027] Further, preferably, the fuel gas channel forms a fuel gas pressure chamber, such
that the anode is pressed when the fuel gas is supplied to the fuel gas channel, and
the oxygen-containing gas channel forms an oxygen-containing gas pressure chamber,
such that the cathode is pressed when the oxygen-containing gas is supplied to the
oxygen-containing gas channel.
[0028] Further, preferably, a plurality of electrolyte electrode assemblies are arranged
concentrically about the center of the separator. Thus, the fuel cell has a compact
structure, whereby the influenced of heat distortion thereon can be avoided.
[0029] Further, the present invention relates to a fuel cell stack formed by stacking a
plurality of fuel cells as described above.
[0030] After the fuel gas is supplied to the anode for causing a power generation reaction,
when the fuel gas is discharged from the anode as an exhaust gas, the exhaust gas
contains unconsumed gas therein. The exhaust gas containing the unconsumed gas is
referred to as an off gas.
[0031] According to the present invention, after the fuel gas has been consumed in the electrolyte
electrode assembly, the off gas is emitted from a position spaced outwardly from the
outer circumferential portion of the electrolyte electrode assembly. Thus, it is possible
to prevent the electrolyte electrode assembly and the separator from being heated
locally to a high temperature as a result of the reaction of the off gas and the oxygen-containing
gas. Further, the electrolyte electrode assembly and the separator do not come into
contact with water produced during the reaction.
[0032] Thus, it is possible to reliably prevent corrosion by steam oxidation, whereby the
durability of the separator is improved. Further, it is possible to prevent oxidation
of the electrolyte electrode assembly, and in particular, the anode. Consequently,
it is possible to prevent damage or degradation in the performance of the electrolyte
electrode assembly.
Brief Description of Drawings
[0033]
FIG. 1 is a partial cross sectional view showing a fuel cell system including a fuel
cell according to a first embodiment of the present Invention;
FIG. 2 is a perspective view schematically showing a fuel cell stack of a fuel cell
system;
FIG. 3 is an exploded perspective view showing a fuel cell of the fuel cell stack;
FIG. 4 is a partial exploded perspective view showing gas flows within the fuel cell;
FIG. 5 is a partial enlarged view showing one surface of the separator;
FIG. 6 is a view showing the other surface of the separator;
FIG. 7 is a cross sectional view schematically showing operation of the fuel cell;
FIG. 8 is a view showing another structure of a fuel gas discharge channel;
FIG. 9 is an exploded perspective view showing a fuel cell according to a second embodiment
of the present invention;
FIG. 10 is a front view showing a separator of the fuel call;
FIG. 11 is a cross sectional view schematically showing operation of the fuel cell;
FIG. 12 is an exploded perspective view showing a fuel cell according to a third embodiment
of the present invention:
FIG. 13 is a partial enlarged view showing one surface of the separator:
FIG. 14 is a cross sectional view schematically showing operation of the fuel cell:
FIG. 15 is an exploded perspective view showing a fuel cell according to a fourth
embodiment of the present invention;
FIG. 16 is a cross sectional view schematically showing operation of the fuel cell;
FIG. 17 is an exploded perspective view showing a fuel cell according to a fifth embodiment
of the present invention;
FIG. 18 is a cross sectional view schematically showing operation of the fuel cell;
FIG. 19 is a perspective view schematically showing a fuel cell stack formed by stacking
fuel cells in accordance with a sixth embodiment of the present invention:
FIG. 20 is an exploded perspective view showing the fuel cell;
FIG. 21 is a front view showing the fuel cell;
FIG. 22 is a cross sectional view taken along line XXII-XXII in FIG. 21;
FIG. 23 is an exploded perspective view showing a fuel cell according to a seventh
embodiment of the present invention; and
FIG. 24 is a view showing a conventional fuel cell.
Best Mode for Carrying Out the Invention
[0034] FIG. 1 is a partial cross sectional view showing a fuel cell system 10 including
a fuel cell 11 according to a first embodiment of the present invention. FIG. 2 is
a perspective view schematically showing a fuel cell stack 12 formed by stacking a
plurality of fuel cells 11 in a direction indicated by the arrow A.
[0035] The fuel cell system 10 is used in various applications, including stationary and
mobile applications. For example, the fuel cell system 10 may be mounted on a vehicle.
As shown in FIG. 1, the fuel cell system 10 includes the fuel cell stack 12. a heat
exchanger 14, a reformer 16, and a casing 18. The heat exchanger 14 heats an oxygen-containing
gas before it is supplied to the fuel cell stack 12. The reformer 16 reforms fuel
in order to produce a fuel gas. The fuel cell stack 12, the heat exchanger 14, and
the reformer 16 are disposed within the casing 18.
[0036] In the casing 18, a fluid unit 19, including at least the heat exchanger 14 and the
reformer 16, is disposed on one side of the fuel cell stack 12, and a load applying
mechanism 21, which applies a tightening load to the fuel cells 11 in the stacking
direction indicated by the arrow A, is disposed on the other side of the fuel cell
stack 12. The fluid unit 19 and the load applying mechanism 21 are provided symmetrically
with respect to a central axis of the fuel cell stack 12.
[0037] The fuel cell 11 is a solid oxide fuel cell (SOFC). As shown in FIGS. 3 and 4, the
fuel cell 11 includes electrolyte electrode assemblies 26. Each of the electrolyte
electrode assemblies 26 includes a cathode 2.2, an anode 24, and an electrolyte (electrolyte
plate) 20 interposed between the cathode 22 and the anode 24. For example, the electrolyte
20 is made of an ion-conductive solid oxide, such as stabilized zirconia. The electrolyte
electrode assembly 26 has a circular disk shape. A barrier layer (not shown) is provided
at least on the outer circumferential edge of the electrolyte electrode assembly 26
in order to prevent the entry and emission of the oxygen-containing gas and the fuel
gas.
[0038] A plurality of, e.g., eight, electrolyte electrode assemblies 26 are sandwiched between
a pair of separators 28 to form the fuel cell 11. The eight electrolyte electrode
assemblies 26 are concentric with respect to a fuel gas supply passage 30 that extends
through the center of the separators 28.
[0039] In FIG. 3, for example, each of the separators 28 comprises a single metal plate
of, e.g., a stainless alloy or a carbon plate. The separator 28 has a first small
diameter end portion (reactant gas supply unit) 32. The fuel gas supply passage 30
extends through the center of the first small diameter end portion 32. The first small
diameter end portion 32 is formed integrally together with circular disks (sandwiching
members) 36 through a plurality of first bridges 34. The first bridges 34 extend radially
outwardly from the first small diameter end portion 32 at equal angles (intervals).
[0040] The circular disk 36 and the electrolyte electrode assembly 26 are of substantially
the same size. A fuel gas inlet 38 for supplying the fuel gas is formed at the center
of the circular disk 36, or at an upstream position that is deviated from the center
of the circular disk 36 in the flow direction of the oxygen-containing gas. A plate
shaped extension 40 is provided at an outer end of the circular disk 36 (in the outer
circumferential portion of the separator 28). The plate shaped extension 40 protrudes
outwardly in the direction indicated by the arrow B.
[0041] Each of the circular disks 36 includes a fuel gas channel 46 on its surface 36a.
which contacts the anode 24 in order to supply a fuel gas along a surface of the anode
24. As show in FIG. 5, the fuel gas channel 46 includes a plurality of ring shaped
grooves (channel units) 48a to 48f formed concentrically around the fuel gas inlet
38 on the circular disk 36. The ring shaped groove 48a having the smallest diameter
is connected to the fuel gas inlet 38 through a straight groove 50. The diameters
of the ring shaped grooves become larger toward the outside, from the ring shaped
groove 48a to the ring shaped groove 48f. The ring shaped grooves 48a to 48f are connected
together through connection grooves 52, which are arranged on the front side and back
side alternately, in the direction indicated by the arrow B.
[0042] The ring shaped groove 48f having the largest diameter is connected to a discharge
hole (through hole) 54 at its front end in the direction indicated by the arrow B.
The fuel gas inlet 38 is connected to the fuel gas discharge channel 68, as described
later, by the ring shaped grooves 48a to 48f through the discharge hole 54. A ring
shaped protrusion 56 is provided in the outer circumferential region of each circular
disk 36. The ring shaped protrusion 56 makes tight contact with the outer circumferential
portion of the anode 24 of the electrolyte electrode assembly 26.
[0043] As shown in FIG. 6, each of the circular disks 36 has a planar surface 36b, which
contacts the cathode 22. A fuel gas supply channel 58 extends from the first small
diameter end portion 32 to the first bridge 34. The fuel gas supply channel 58 connects
the fuel gas supply passage 30 to the fuel gas inlet 38. For example, the fuel gas
supply channel 58 may be formed by etching.
[0044] As shown in FIG. 3, a channel member 60 is fixed to the separator 28, e.g., by brazing
or laser welding, on a surface facing the cathode 22. The channel member 60 has a
planar shape, and includes a second small diameter end portion 62. The fuel gas supply
passage 30 extends through the center of the second small diameter end portion 62.
Eight second bridges 64 extend radially from the second small diameter end portion
62. Each of the second bridges 64 is fixed to the separator 28, extending from the
first bridge 34 to the surface 36b of the circular disk 36, and covering the fuel
gas inlet 38 (see FIG. 7).
[0045] As shown in FIGS. 3 and 7, a discharge groove member 66 is fixed to the surface 36b
of the circular disk 36. The discharge groove member 66 covers the discharge hole
54 and the plate shaped extension 40. A discharge groove 66a, which is connected to
the discharge hole 54, is formed in the discharge groove member 66. A fuel gas discharge
channel 68 is formed by the discharge hole 54 and the discharge groove 66a.
[0046] The fuel gas discharge channel 68 is opened to the outside at the end of the discharge
groove member 66. The distance H between the end of the discharge groove member 66
and the outer circumferential surface of the electrolyte electrode assembly 26 is
determined such that the separator 28 and the electrolyte electrode assembly 26 can
suitably avoid being influenced by the combustion gas formed by a mixture of the off
gas and the oxygen-containing gas, and also avoid being influenced by water.
[0047] On the surface 36b of the circular disk 36, a deformable elastic channel member,
such as an electrically conductive mesh member 72, is provided. The elastically conductive
mesh member 72 forms an oxygen-containing gas channel 70 through which an oxygen-containing
gas is supplied along a surface of the cathode 22, wherein the electrically conductive
mesh member 72 is placed in tight contact with the cathode 22. Instead of the mesh
member 72, it also is possible to use a felt member, for example.
[0048] For example, the mesh member 72 is made of stainless steel wire rods, and has a circular
disk shape. The thickness of the mesh member 72 is determined such that the mesh member
72 can be deformed elastically when a load in the stacking direction (indicated by
the arrow A) is applied to the mesh member 72. The mesh member 72 directly contacts
the surface 36b of the circular disk 36, and has cutouts 72a, 72b, which serve as
spaces for providing the channel member 60 and the discharge groove member 66.
[0049] As shown in FIG. 7, the area in which the mesh member 72 is disposed is smaller than
the power generation area of the anode 24. The oxygen-containing gas channel 70, which
is formed in the mesh member 72, is connected to the oxygen-containing gas supply
passage (oxygen-containing gas supply unit) 74. The oxygen-containing gas is supplied
in the direction indicated by the arrow B, through the space between the inner circumferential
edge of the electrolyte electrode assembly 26 and the inner circumferential edge of
the circular disk 36. The oxygen-containing gas supply passage 74 extends in the stacking
direction among the respective circular disks 36 and the first bridges 34.
[0050] Insulating seals 76 for sealing the fuel gas supply passage 30 are provided between
the separators 28. For example, the insulating seals 76 may be made of a mica material,
or a ceramic material. An exhaust gas channel 78 for the fuel cells 11 is formed outside
of the circular disks 36.
[0051] As shown in FIGS. 1 and 2, the fuel cell stack 12 includes end plates 80a, 80b provided
at opposite ends of the fuel cells 11 in the stacking direction. The end plate 80a
has a substantially circular disk shape. A ring shaped portion 82 protrudes from the
outer circumferential end of the end plate 80a, and a groove 84 is formed around the
ring shaped portion 82. A columnar projection 86 is formed at the center of the ring
shaped portion 82. The columnar projection 86 protrudes in the same direction as the
ring shaped portion 82. A stepped hole 88 is formed within the projection 86.
[0052] Holes 90 and screw holes 92 are formed so as to lie within the same virtual circle
around the projection 86. The holes 90 and the screw holes 92 are arranged alternately,
while being spaced from each other at predetermined angles (intervals), at positions
corresponding to the respective spaces of the oxygen-containing gas supply passage
74 formed between the first and second bridges 34, 64. The diameter of the end plate
80b is larger than the diameter of the end plate 80a. Further, the end plate 80a is
an electrically conductive thin plate.
[0053] The casing 18 includes a first case unit 96a containing the load applying mechanism
21, and a second case unit 96b containing the fuel cell stack 12. The end plate 80b
and an insulating member are sandwiched between the first case unit 96a and the second
case unit 96b. The insulating member is provided on the side of the second case unit
96b. The joined portion between the first case unit 96a and the second case unit 96b
is tightened by screws 98 and nuts 100. The end plate 80b functions as a gas barrier,
which prevents hot exhaust gas or hot air from the fluid unit 19 from entering into
the load applying mechanism 21.
[0054] An end of a ring shaped wall plate 102 is joined to the second case unit 96b, and
a head plate 104 is fixed to the other end of the wall plate 102. The fluid unit 19
is disposed symmetrically with respect to the central axis of the fuel cell stack
12. Specifically, the substantially cylindrical reformer 16 is provided coaxially
inside of the substantially ring shaped heat exchanger 14.
[0055] A wall plate 106 is fixed to the groove 84 around the end plate 80a, so as to form
a channel member 108. The heat exchanger 14 and the reformer 16 are directly connected
to the channel member 108. A chamber 108a is formed in the channel member 108, wherein
the chamber 108a is temporarily filled with air heated by the heat exchanger 14. The
holes 90 form openings for supplying the air, which temporarily fills the chamber
108a, to the fuel cell stack 12.
[0056] A fuel gas supply pipe 110 and a reformed gas supply pipe 112 are connected to the
reformer 16. The fuel gas supply pipe 110 extends to the outside from the head plate
104. The reformed gas supply pipe 112 is inserted into the stepped hole 88 of the
end plate 80a, and is connected to the fuel gas supply passage 30.
[0057] An air supply pipe 114 and an exhaust gas pipe 116 are connected to the head plate
104. A channel 118 extending from the air supply pipe 114, and which is directly opened
to the channel member 108 through the heat exchanger 14, and another channel 120 extending
from the exhaust gas channel 78 of the fuel cell stack 12 to the exhaust gas pipe
116 through the heat exchanger 14, are provided in the casing 18.
[0058] The load applying mechanism 21 includes a first tightening unit 122a for applying
a first tightening load T1 to a region around (or near) the fuel gas supply passage
30, and a second tightening unit 122b for applying a second tightening load T2 to
the electrolyte electrode assemblies 26. The second tightening load T2 is smaller
than the first tightening load T1 (T1 > T2).
[0059] The first tightening unit 122a includes relatively short first tightening bolts 124a,
which are screwed into the screw holes 92 formed along one diagonal line of the end
plate 80a. The first tightening bolts 124a extend in the stacking direction of the
fuel cells 11. and engage with a first presser plate 126a. The first tightening bolts
124a also are provided in the oxygen-containing gas supply passage 74 extending through
the separators 28. The first presser plate 126a is formed by a narrow plate, and engages
with a central position of the separator 28 so as to cover the fuel gas supply passage
30.
[0060] The second tightening unit 122b includes relatively long second tightening bolts
124b, which are screwed into screw holes 92 formed along the other diagonal line of
the end plate 80a. Ends of the second tightening bolts 124b extend through a second
presser plate 126b having a curved outer section. Nuts 127 are fitted onto the ends
of the second tightening bolts 124b. The second tightening bolts 124b also are provided
in the oxygen-containing gas supply passage 74 extending through the separators 28.
Springs 128 and spring seats 129 are provided in respective circular portions of the
second presser plate 126b, at positions corresponding to the electrolyte electrode
assemblies 26 on the circular disks 36 of the fuel cell 11. The springs 128 are ceramic
springs, for example.
[0061] Next, operation of the fuel cell system 10 shall be described below.
[0062] As shown in FIG. 3, when assembling the fuel cell system 10, first, the channel member
60 is joined to the surface of the separator 28 facing the cathode 22. Thus, a fuel
gas supply channel 58, which is connected to the fuel gas supply passage 30, is formed
between the separator 28 and the channel member 60. The fuel gas supply channel 58
is connected to the fuel gas channel 46 through the fuel gas inlet 38 (see FIG. 7).
[0063] The discharge groove member 66 is joined to the surface 36b of each circular disk
36. Thus, the discharge hole 54 and the discharge groove 66a are connected together
so as to form the fuel gas discharge channel 68. The ring shaped insulating seal 76
is provided on each of the separators 28 around the fuel gas supply passage 30.
[0064] The separator 28 is fabricated in the following manner. Specifically, eight electrolyte
electrode assemblies 26 are interposed between a pair of the separators 28 in order
to form the fuel cell 11. As shown in FIGS. 3 and 4, the electrolyte electrode assemblies
26 are interposed between the surface 36a of one separator 28 and the surface 36b
of the other separator 28. The fuel gas inlet 38 is positioned substantially at a
center location in each of the anodes 24. The mesh member 72 is provided between the
surface 36b of the separator 28 and the electrolyte electrode assembly 26. The two
cutouts 72a, 72b of the mesh member 72 are provided at positions corresponding to
the channel member 60 and the discharge groove member 66.
[0065] A plurality of fuel cells 11 are stacked in the direction indicated by the arrow
A, and the end plates 80a, 80b are provided at opposite ends in the stacking direction.
As shown in FIGS. 1 and 2, the first presser plate 126a of the first tightening unit
122a is provided at the center of the fuel cell 11.
[0066] In this state, the short first tightening bolts 124a are inserted through the first
presser plate 126a and the end plate 80b toward the end plate 80a. Tip ends of the
first tightening bolts 124a are screwed and fitted into the screw holes 92, which
are formed along one of the diagonal lines of the end plate 80a. The heads of the
first tightening bolts 124a engage the first presser plate 126a. The first tightening
bolts 124a are rotated within the screw holes 92 in order to adjust the surface pressure
of the first presser plate 126a. In this manner, in the fuel cell stack 12, the first
tightening load T1 is applied to the region near the fuel gas supply passage 30.
[0067] Then, the springs 128 and the spring seats 129 are aligned axially with the electrolyte
electrode assemblies 26 at respective positions of the circular disks 36. The second
presser plate 126b of the second tightening unit 122b engage with the spring seats
129 provided at one end of the springs 128.
[0068] Then, the long second tightening bolts 124b are inserted through the second presser
plate 126b and the end plate 80b toward the end plate 80a. Tip ends of the second
tightening bolts 124b are screwed and fitted into the screw holes 92, which are formed
along the other diagonal line of the end plate 80a. The nuts 127 are fitted onto the
heads of the second tightening bolts 124b. Therefore, by adjusting the state of screw
engagement between the nuts 127 and the second tightening bolts 124b, the second tightening
load T2 is applied to the electrolyte electrode assemblies 26 via elastic forces of
the respective springs 128.
[0069] The end plate 80b of the fuel cell stack 12 is sandwiched between the first case
unit 96a and the second case unit 96b of the casing 18. The first case unit 96a and
the second case unit 96b are fixed together by screws 98 and nuts 100. The fluid unit
19 is mounted inside the second case unit 96b. The wall plate 106 of the fluid unit
19 is attached to the groove 84 around the end plate 80a. Thus, the channel member
108 is provided between the end-plate 80a and the wall plate 106.
[0070] In the fuel cell system 10, as shown in FIG. 1, a fuel (methane, ethane, propane,
or the like) and, as necessary, water, are supplied from the fuel gas supply pipe
110, and an oxygen-containing gas (hereinafter referred to simply as "air") is supplied
from the air supply pipe 114.
[0071] The fuel is reformed as it passes through the reformer 16, thereby producing a fuel
gas (hydrogen-containing gas). The fuel gas is supplied to the fuel gas supply passage
30 of the fuel cell stack 12. The fuel gas moves in the stacking direction, as indicated
by the arrow A, and flows into the fuel gas supply channel 58 through the separator
28 of each fuel cell 11 (see FIG. 7).
[0072] The fuel gas flows along the fuel gas supply channel 58 between the first and second
bridges 34, 64, and flows into the fuel gas inlets 38 of the circular disks 36. Thus,
the fuel gas is supplied to the fuel gas channel 46 on each of the circular disks
36. The fuel gas inlets 38 are formed at positions corresponding to substantially
central positions of the anodes 24 of the electrolyte electrode assemblies 26. Thus,
the fuel gas is supplied from the fuel gas inlets 38 and to substantially central
regions of the anodes 24, and flows outwardly from the central regions of the anodes
24.
[0073] Specifically, as shown in FIG. 5. the fuel gas channel 46 includes a plurality of
ring shaped grooves 48a to 48f. First, the fuel gas is supplied to the ring shaped
groove 48a through the straight groove 50 connected to the fuel gas inlet 38. After
the fuel gas flows through the ring shaped groove 48a, the fuel gas flows outwardly
temporarily through the connection groove 52, and then is supplied to the ring shaped
groove 48b outside the ring shaped groove 48a. Thus, the fuel gas then flows along
the ring shaped groove 48b.
[0074] Further, the fuel gas, which is supplied to the ring shaped groove 48c outside the
ring shaped groove 48b through the connection groove 52, flows along the other ring
shaped grooves 48d to 48f through the connection groove 52, until the fuel gas reaches
the discharge holes 54. Therefore, the fuel gas is supplied outwardly from the substantially
central region of the anode 24. After being consumed, the fuel gas is discharged through
the discharge hole 54.
[0075] As shown in FIG. 7, the consumed fuel gas, which is discharged through the discharge
hole 54, moves toward the surface 36b, and flows into the discharge groove 66a. Thus
the consumed fuel gas flows along the fuel gas discharge channel 68 in the direction
indicated by the arrow B. Then, the consumed fuel gas is discharged to the outside
from an outer end of the discharge groove member 66.
[0076] As shown in FIG. 1, air from the air supply pipe 114 flows through the channel 118
of the heat exchanger 14, and temporarily flows into the chamber 108a. The air flows
through the holes 90, which are connected to the chamber 108a, and is supplied to
the oxygen-containing gas supply passage 74, which is disposed substantially at the
center of the fuel cells 11. At this time, in the heat exchanger 14, as described
later, since the exhaust gas discharged to the exhaust gas channel 78 flows through
the channel 120, heat exchange is performed between the air before it is supplied
to the fuel cells 11 and the exhaust gas. Therefore, the air is heated to a desired
fuel cell operating temperature beforehand.
[0077] The oxygen-containing gas, which is supplied to the oxygen-containing gas supply
passage 74, flows into the space between the inner circumferential edge of the electrolyte
electrode assembly 26 and the inner circumferential edge of the circular disk 36,
in the direction indicated by the arrow B, and then flows toward the oxygen-containing
gas channel 70 formed by the mesh member 72. As shown in FIG. 7, in the oxygen-containing
gas channel 70, the oxygen-containing gas flows from an inner circumferential edge
(central region of the separator 28) toward an outer circumferential edge (outer region
of the separator 28) and, more specifically, from one end to the other end of the
outer circumferential region of the cathode 22 of the electrolyte electrode assembly
26.
[0078] Thus, in the electrolyte electrode assembly 26, the fuel gas flows from the central
region to the outer circumferential region of the anode 24, and the oxygen-containing
gas flows in one direction indicated by the arrow B along the electrode surface of
the cathode 22. At this time, oxygen ions flow through the electrolyte 20 toward the
anode 24, in order to generate electricity as a result of an electrochemical reaction
therebetween.
[0079] The exhaust gas (off gas), which is discharged to the outside of the respective electrolyte
electrode assemblies 26, flows through the exhaust gas channel 78 in the stacking
direction. When the exhaust gas flows through the channel 120 of the heat exchanger
14, heat exchange is carried out between the exhaust gas and the air. Then, the exhaust
gas is discharged into the exhaust gas pipe 116 (see FIG. 1).
[0080] In the first embodiment, as shown in FIG. 5, the fuel gas channel 46 has a start
point located at the fuel gas inlet 38 and opened to the central position of the electrolyte
electrode assembly 26. Further, the fuel gas channel 46 has an end point located at
a position corresponding to the outer circumferential edge of the electrolyte electrode
assembly 26. At the end point, the fuel gas channel 46 is connected to the discharge
hole 54, so as to discharge the fuel gas that is consumed in the electrolyte electrode
assembly 26 from the fuel gas channel 46.
[0081] As shown in FIG. 7, the off gas discharged from the discharge hole 54 flows into
the fuel gas discharge channel 68, including the discharge groove 66a provided in
the discharge groove member 66. The off gas moves within the fuel gas discharge channel
68, in the direction indicated by the arrow B, and the off gas is emitted (discharged)
to the outside at a position spaced outwardly by a predetermined distance H from the
outer circumferential portions of the separator 28 and the electrolyte electrode assembly
26.
[0082] Therefore, the area (reaction area) in which the off gas and the post-reaction oxygen-containing
gas are mixed together is spaced significantly away from the outer circumferential
portions of the electrolyte electrode assembly 26 and the separator 28. Thus, the
electrolyte electrode assembly 26 and the separator 28 are prevented from becoming
heated locally to a high temperature, as a result of the hot combustion gas formed
as a mixture of the off gas and air, or by any reaction of the combustion gas. Further,
the electrolyte electrode assembly 26 and the separator 28 do not come into contact
with water produced during the reaction.
[0083] Thus, it is possible to reliably prevent corrosion by steam oxidation, thereby improving
the durability of the separator 28. Further, oxidation of the electrolyte electrode
assembly 26, and in particular, the anode 24, can be prevented. Consequently, damage
or degradation in the performance of the electrolyte electrode assembly 26 can be
prevented.
[0084] In the first embodiment, as shown in FIGS. 3 and 7, the ring shaped protrusion 56
is provided on the surface 36a of each circular disk 36. The ring shaped protrusion56
contacts tightly with the outer circumferential portion of the anode 24. Therefore,
the exhaust gas does not enter the outer circumferential portion of the anode 24.
Thus, using a seal free (sealless) structure, it is possible to reliably prevent degradation
of the anode 24 by oxidation.
[0085] The cathode 22 of the electrolyte electrode assembly 26 contacts the mesh member
72. In this state, a load in the stacking direction, as indicated by the arrow A,
is applied to the components of the fuel cell 11. Since the mesh member 72 is deformable,
the mesh member 72 remains in tight contact with the cathode 22.
[0086] In this structure, dimensional errors or distortions, which may occur when producing
the electrolyte electrode assembly 26 or the separator 28, can suitably be absorbed
by elastic deformation of the mesh member 72. Thus, in the first embodiment, damage
that could occur when stacking the components of the fuel cell 11 is prevented. Since
the components of the fuel cell 11 are in contact with each other at many points,
an improvement in performance when collecting electricity from the fuel cell 11 can
be achieved.
[0087] Further, in the first embodiment, the fuel gas supply passage 30 is provided hermetically
inside of the oxygen-containing gas supply passage 74, and moreover, the fuel gas
supply channel 58 is provided along the separator surface. Therefore, the fuel gas
prior to consumption is heated by the hot oxygen-containing gas, which has been heated
through heat exchange in the heat exchanger 14. Thus, an improvement in heat efficiency
can be achieved.
[0088] Further, the exhaust gas channel 78 is provided around the separators 28. The exhaust
gas channel 78 is used for preventing heat radiation from the separators 28. Further,
the fuel gas inlet 38 is provided substantially at the center of the circular disk
36, or is provided at an upstream position that is deviated from the center of the
circular disk 36 in the flow direction of the oxygen-containing gas. Therefore, the
fuel gas, which is supplied from the fuel gas inlet 38, is diffused radially from
the center of the anode 24. Thus, a smooth and uniform reaction occurs, whereby an
improvement in the fuel utilization ratio can be achieved.
[0089] Further, the area occupied by the mesh member 72 is smaller than the power generation
area of the anode 24 (see FIG. 6). Therefore, even if the exhaust gas flows around
to the anode 24 from the outside of the electrolyte electrode assembly 26, the power
generation area does not exist along the outer circumferential edge of the cathode
22 opposite to the outer circumferential edge of the anode 24. Thus, fuel consumption
by the circulating current does not increase significantly, and a large electromotive
force can easily be collected. Accordingly, electricity collection performance is
improved, and an advantageous fuel utilization ratio can be achieved. Further, the
present invention can be carried out easily, simply by using the mesh member 72 as
an elastic channel member. Thus, the structure of the present invention is both simple
and cost effective.
[0090] In particular, even when an electrolyte electrode assembly 26 with small strength,
having a thin electrolyte 20 and a thin cathode 22 (i.e., a so called support membrane
type MEA) is used, stresses applied to the electrolyte 20 and the cathode 22 by the
mesh member 72 are moderate, thus advantageously reducing damage to the electrolyte
electrode assembly 26.
[0091] Further, eight electrolyte electrode assemblies 26 are arranged concentrically about
the center of the separator 28. Thus, since the overall size of the fuel cell 11 is
small, the influence of heat distortion can be avoided.
[0092] In the first embodiment, the fuel gas channel 46 includes a plurality of ring shaped
grooves 48a to 48f concentrically arranged with each other, wherein the connection
grooves 52 connect the ring shaped grooves 48a to 48f at respective diagonal positions.
However, the present invention is not limited in this respect. Various other shapes
can be adopted. For example, the grooves may have a spiral shape.
[0093] The fuel gas channel 46a may be used instead of the fuel gas channel 46, as shown
in FIG. 8. The fuel gas channel 46a includes a plurality of ring shaped grooves 48a
to 48f concentrically arranged with each other in the same manner as with the fuel
gas channel 46. Further, the ring shaped groove 48f has a dividing portion 49 providing
ends of the ring shaped groove 48f. Discharge holes 54a, 54b connected to the fuel
gas discharge channel 68 are formed at both ends of the ring shaped groove 48f, respectively.
[0094] FIG. 9 is an exploded perspective view showing a fuel cell 140 according to the second
embodiment of the present invention. Constituent elements that are identical to those
of the fuel cell 11 according to the first embodiment shall be labeled using the same
reference numerals, and detail descriptions of such features shall be omitted. Further,
in the third to sixth embodiments to be described later, constituent elements that
are identical to those of the fuel cell 11 according to the first embodiment shall
also be labeled using the same reference numerals, and detailed descriptions of such
features shall be omitted.
[0095] The fuel cell 140 has a separator 142, wherein an oxygen-containing gas channel 144
is formed on a surface of the separator 142 facing the cathode 22. The oxygen-containing
gas channel 144 is formed by a plurality of protrusions 146, which are formed on the
surface 36b of each circular disk 36 (see FIGS. 10 and 11).
[0096] The protrusions 146 are solid portions formed, for example, by etching on the surface
36b. Various shapes, such as a rectangular shape, a circular shape, or a triangular
shape, may be used for the cross sectional shapes of the protrusions 146. The positions
or density of the protrusions 146 can be changed arbitrarily, depending on the flow
state and/or fluidic conditions of the oxygen-containing gas or the like.
[0097] In the second embodiment, the load in the stacking direction is efficiently transmitted
through the protrusions 146 of the circular disk 36. Therefore, the fuel cells 140
can be stacked together with a small load, thereby reducing distortions in the electrolyte
electrode assemblies 26 and the separators 142.
[0098] The protrusions 146 on the surface 36b of the circular disk 36 are formed by etching
or the like as solid portions-Thus, the shape, positions, and density of the protrusions
146 can be changed arbitrarily and easily, depending on the flow state and/or fluidic
conditions of the oxygen-containing gas, whereby a desired flow of the fuel gas can
be achieved. Further, since the protrusions 146 are formed as solid portions, the
protrusions 146 cannot be deformed, and thus, the load is reliably transmitted through
the protrusions 146, and electricity is efficiently collected through the protrusions
146.
[0099] FIG. 12 is an exploded perspective view showing a fuel cell 160 according to a third
embodiment of the present invention.
[0100] The fuel cell 160 has a separator 162, wherein a fuel gas discharge channel 164 is
formed on a surface of the separator 162 facing the anode 24. As shown in FIGS. 12
and 13, a fuel gas discharge channel 164 is formed on the surface 36a of each circular
disk 36. The fuel gas discharge channel 164 includes a discharge groove 166 connected
to the fuel gas channel 46, and a lid member 168, which is provided on the surface
36a, for thereby closing the discharge groove 166.
[0101] The discharge groove 166 is provided in place of the discharge hole 54, at a position
corresponding to the discharge hole 54, along the plate shaped extension 40. The discharge
groove 166 includes a step (not shown), wherein the lid member 168 is provided on
the step. Thus, the surface of the lid member 168 and the surface of the ring shaped
protrusion 56 are both disposed in the same plane.
[0102] In the third embodiment, as shown in FIG. 14, the fuel gas flows through the fuel
gas channel 46, and is supplied to the anode 24 of the electrolyte electrode assembly
26. After the fuel gas has been consumed during the reaction, the fuel gas flows into
the discharge groove 166 near the outer circumferential end of the anode 24, and is
discharged along the fuel gas discharge channel 164, in the direction indicated by
the arrow B.
[0103] Accordingly, the fuel gas, after having been consumed, is emitted at a position spaced
outwardly by a predetermined distance H from the outer circumferential portion of
the electrolyte electrode assembly 26. Thus, the same advantages as those of the first
and second embodiments can be obtained. For example, damage or degradation of the
separator 162 or the electrolyte electrode assembly 26 can be prevented.
[0104] In the first to third embodiments, air serving as an oxygen-containing gas is supplied
outwardly from the center of the separators 28, 142, 162. However, the present invention
is not limited in this respect. Alternatively, the air may be supplied inwardly from
the outside of the separators 28, 142, 162.
[0105] FIG. 15 is an exploded perspective view showing a fuel cell 180 according to a fourth
embodiment of the present invention.
[0106] The fuel cell 180 includes a separator 182, wherein a fuel gas channel 46 is formed
on a surface of the separator 182 facing the anode 24. The fuel gas channel 46 is
formed by a plurality of protrusions 186, provided on a surface 36a of each circular
disk 36 (see FIGS. 15 and 16). The protrusions 146 are solid portions formed on the
surface 36a, for example, by etching.
[0107] FIG. 17 is an exploded perspective view showing a fuel cell 190 according to a fifth
embodiment of the present invention.
[0108] The fuel cell 190 has a separator 192, wherein a deformable elastic channel member,
such as an electrically conductive mesh member 196, is provided on a surface 36a of
the circular disk 36 of the separator 192. The electrically conductive mesh member
196 forms a fuel gas channel 46 through which the fuel gas is supplied along a surface
of the anode 24, wherein the electrically conductive mesh member 196 is in tight contact
with the anode 24 (see FIGS. 17 and 18).
[0109] FIG. 19 is a perspective view schematically showing a fuel cell stack 202, formed
by stacking fuel cells 200 in the direction indicated by the arrow A, according to
a sixth embodiment of the present invention.
[0110] As shown in FIG. 20, the fuel cell 200 is formed by sandwiching the electrolyte electrode
assembly 26 between a pair of separators 204. Each separator 204 includes first and
second plates 206, 208, and a third plate 210. For example, the first to third plates
206, 208, 210 are metal plates formed, for example, from a stainless alloy. The first
plate 206 and the third plate 210 are joined to both surfaces of the second plate
208 by brazing, for example.
[0111] As shown in FIGS. 20 and 21, the first plate 206 has a first small diameter end portion
(reactant gas supply unit) 212. A fuel gas supply passage 30, for supplying a fuel
gas in the direction indicated by the arrow A, extends through the first small diameter
end portion 212. The first small diameter end portion 212 is formed integrally with
a first circular disk (sandwiching member) 216 having a relatively large diameter,
through a narrow bridge 214. The first circular disk 216 and the anode 24 of the electrolyte
electrode assembly 26 are of substantially the same size.
[0112] A large number of first protrusions 220 are formed on a surface of the first circular
disk 216, which contacts the anode 24, in a central region thereof adjacent to an
outer circumferential region. A substantially ring shaped protrusion 222 is provided
on the outer circumferential region of the first circular disk 216. The first protrusions
220 contact the anode 24 of the electrolyte electrode assembly 26 such that a fuel
gas channel 46, for supplying the fuel gas to the anode 24, is formed between the
first protrusions 220 and the anode 24. The first protrusions 220 and the substantially
ring shaped protrusion 222 jointly form a current collector.
[0113] A fuel gas inlet 38 is provided at the center of the first circular disk 216, for
supplying the fuel gas toward a substantially central region of the anode 24. A plurality
of discharge holes (through holes) 224 are formed in the substantially ring shaped
protrusion 222 of the first circular disk 216. The first protrusions 220 may be formed
by a plurality of recesses provided in a surface that lies in the same plane as the
surface of the substantially ring shaped protrusion 222. A plurality of plate shaped
extensions 226 are provided at predetermined angles (intervals) in the outer circumferential
portion of the first circular disk 216.
[0114] As shown in FIG. 20, the third plate 210 includes a second small diameter end portion
(reactant gas supply unit) 228. An oxygen-containing gas supply passage 74, for supplying
an oxygen-containing gas in the direction indicated by the arrow A, extends through
the second small diameter end portion 228. The second small diameter end portion 228
is formed integrally with a second circular disk (sandwiching member) 232 having a
relatively large diameter, through a narrow bridge 230.
[0115] As shown in FIG. 22, a plurality of second protrusions 234 are formed over the entire
surface of the second circular disk 232, which contacts the cathode 22 of the electrolyte
electrode assembly 26. The second protrusions 234 contact the cathode 22 of the electrolyte
electrode assembly 26 such that an oxygen-containing gas channel 70, for supplying
the oxygen-containing gas to the cathode 22. is formed between the second protrusions
234 and the cathode 22. The second protrusions 234 function as a current collector.
An oxygen-containing gas inlet 236 is provided at the center of the second circular
disk 232, for supplying the oxygen-containing gas toward a substantially central region
of the cathode 22.
[0116] As shown in FIG. 20. the second plate 208 includes a third small diameter end portion
(reactant gas supply unit) 238 and a fourth small diameter end portion (reactant gas
supply unit) 240. The fuel gas supply passage 30 extends through the third small diameter
end portion 238, and the oxygen-containing gas supply passage 74 extends through the
fourth small diameter end portion 240. The third and fourth small diameter end portions
238, 240 are formed integrally with a third circular disk (sandwiching member) 246
having a relatively large diameter, through narrow bridges 242, 244. respectively.
The first through third circular disks 216, 232, 246 have the same diameter.
[0117] A plurality of plate shaped extensions 248 are provided at predetermined angles (intervals)
along the outer circumferential portion of the third circular disk 246. When the first
and third circular disks 216, 246 are stacked together, the plate shaped extensions
226, 248 form a substantially rectangular pipe shape, wherein a fuel gas discharge
channel 250, which is connected to the discharge holes 224, is formed between the
plate shaped extensions 226, 248 (see FIG. 22).
[0118] A fuel gas supply channel 58 is formed between the bridges 214. 242, and an oxygen-containing
gas supply channel 252 is formed between the bridges 230, 244. The oxygen-containing
gas supply channel 252 is connected to the oxygen-containing gas inlet 236.
[0119] A partition 254 is provided in a surface of the third circular disk 246 facing the
first plate 206. The partition 254 is disposed coaxially with respect to the center
of the third circular disk 246. The partition 254 is formed by a substantially ring
shaped protrusion, wherein the fuel gas supply channel 58 is divided into first and
second fuel gas channel units 58a, 58b by the partition 254. A plurality of third
protrusions 256 are provided on a surface of the third circular disk 246 inside the
partition 254.
[0120] As shown in FIG. 22, the first plate 206 is joined to the second plate 208 by brazing,
so as to form the fuel gas supply channel 58, which is connected to the fuel gas supply
passage 30 and the fuel gas inlet 38 between the first and second plates 206, 208.
[0121] When the fuel gas is supplied to the first fuel gas channel unit 58a, the first circular
disk 216 contacts the anode 24 under pressure. Specifically, the first fuel gas channel
unit 58a forms a first fuel gas pressure chamber 258a. The second fuel gas channel
unit 58b is provided around the first fuel gas pressure chamber 258a. When the fuel
gas is supplied to the second fuel gas channel unit 58b, the first circular disk 216
presses the anode 24 under pressure. Specifically, the second fuel gas channel unit
58b forms a second fuel gas pressure chamber 258b.
[0122] The second plate 208 is joined to the third plate 210 by brazing, so as to form an
oxygen-containing gas supply channel 252, which is connected to the oxygen-containing
gas supply passage 74 and the oxygen-containing gas inlet 236 between the second and
third plates 208, 210. When the oxygen-containing gas is supplied to the oxygen-containing
gas supply channel 252, the second circular disk 232 contacts the cathode 22 under
pressure. Specifically, the oxygen-containing gas supply channel 252 forms an oxygen-containing
gas pressure chamber 260. As shown in FIG. 20, insulating seals 76a, 76b are interposed
between the separators 204 around the fuel gas supply passage 30 and the oxygen-containing
gas supply passage 74.
[0123] As shown in FIG. 19, the fuel cell stack 202 includes end plates 270a, 270b, which
are provided at opposite ends of the fuel cells 200 in the stacking direction. The
end plate 270a, or the end plate 270b, is electrically insulated from the tightening
bolts 272. A first pipe 274 and a second pipe 276 extend through the end plate 270a.
The first pipe 274 is connected to the fuel gas supply passage 30 of the fuel cell
200, and the second pipe 276 is connected to the oxygen-containing gas supply passage
74 of the fuel cell 200.
[0124] In the fuel cell stack 202, a fuel gas is supplied to the first pipe 247, which is
connected to the end plate 270a, and the fuel gas flows from the first pipe 274 into
the fuel gas supply passage 30. An oxygen-containing gas (hereinafter referred to
simply as air) is supplied to the second pipe 276, which is connected to the end plate
270a, and the air flows from the second pipe 276 to the oxygen-containing gas supply
passage 74.
[0125] As shown in FIG. 22, after the fuel gas has flowed into the fuel gas supply passage
30, the fuel gas flows in the stacking direction, as indicated by the arrow A, and
is supplied to the fuel gas supply channel 58 in the separator 204 in each of the
fuel cells 200. The fuel gas flows along the fuel gas supply channel 58, and then
flows into the first fuel gas channel unit 58a. The fuel gas inlet 38 is formed at
the center of the first fuel gas channel unit 58a. The fuel gas flows into the fuel
gas inlet 38 and toward the fuel gas channel 46.
[0126] After the air has flowed into the oxygen-containing gas supply passage 74, the oxygen-containing
gas flows through the oxygen-containing gas supply channel 252 in the separator 28,
and is supplied to the oxygen-containing gas pressure chamber 260. The air flows into
the oxygen-containing gas inlet 236 substantially at the center of the second circular
disk 232.
[0127] In each of the electrolyte electrode assemblies 26, the oxygen-containing gas inlet
236 is provided at a position corresponding to the central position of the cathode
22. Therefore, as shown in FIG. 22, the air from the oxygen-containing gas inlet 236
is supplied to the oxygen-containing gas channel 70, and flows from the central region
of the cathode 22 toward the outer circumferential region of the cathode 22.
[0128] Thus, in each of the electrolyte electrode assemblies 26, the fuel gas is supplied
from a central region of the anode 24 to the outer circumferential region of the anode
24, whereas the air is supplied from the central region of the cathode 22 to the outer
circumferential region of the cathode 22, thereby generating electricity. After the
fuel gas and the air have been consumed as a result of power generation, the fuel
gas and the air are discharged as an exhaust gas into the exhaust gas channel 78.
[0129] In the sixth embodiment, the fuel gas channel 46 has a start point at the fuel gas
inlet 38, which is opened at the center of the electrolyte electrode assembly 26,
and further, the fuel gas channel 46 has an end point located at the substantially
ring shaped protrusion 222, at a position corresponding to the outer circumferential
region of the electrolyte electrode assembly 26. The end point of the fuel gas channel
46 is connected to the discharge holes 224, so as to discharge the fuel gas that is
consumed in the electrolyte electrode assembly 26 from the fuel gas channel 46.
[0130] The off gas, which is discharged into the discharge holes 224, flows into the fuel
gas discharge channel 250 formed between the plate shaped extensions 226, 248. The
off gas moves through the discharge channel 250 in the direction indicated by the
arrow B. The off gas is emitted from a position that is spaced outwardly by a predetermined
distance from the outer circumferential portions of the separator 204 and the electrolyte
electrode assembly 26.
[0131] Therefore, the area (reaction area) where the off gas and the post-reaction oxygen-containing
gas are mixed together is spaced significantly outwardly from the outer circumferential
portions of the electrolyte electrode assembly 26 and the separator 204. Thus, the
same advantages as those of the first to fifth embodiments can be obtained. For example,
the electrolyte electrode assembly 26 and the separator 204 are not heated locally
to a high temperature by the combustion gas, which constitutes a mixed gas of the
off gas and air, or by any reaction of the combustion gas. Thus, the durability of
the separator 204 can be improved.
[0132] FIG. 23 is an exploded perspective view showing a fuel cell 280 according to a seventh
embodiment of the present invention. Constituent elements, which are identical to
those of the fuel cell 200 according to the sixth embodiment, have been labeled using
the same reference numerals, and thus the descriptions thereof shall be omitted.
[0133] The fuel cell 280 has a separator 282, including first to third plates 284, 286,
210. The first and second plates 284, 286 have ring shaped skirts 288, 290, instead
of the plate shaped extensions 226, 248 provided in the sixth embodiment.
[0134] The skirts 288, 290 protrude outwardly a predetermined distance from the outer ends
of the first and third circular disks 216, 246. and a fuel gas discharge channel 292
is formed between the skirts 288, 290. Thus, in the seventh embodiment, similar advantages
to the case of the sixth embodiment can be obtained.
1. A fuel cell (11) formed by stacking an electrolyte electrode assembly (26) and a separator
(28), said electrolyte electrode assembly (26) including an anode (24), cathode (22),
and an electrolyte (20) interposed between said anode (24) and said cathode (22),
said fuel cell (11) comprising:
a fuel gas channel (46) formed on one surface of said separator (28) for supplying
a fuel gas along a surface of said anode (24); and
an oxygen-containing gas channel (70) formed on the other surface of said separator
(28), for supplying an oxygen-containing gas along a surface of said cathode (22),
wherein said fuel gas channel (46) has an end point disposed at a position corresponding
to an outer circumferential portion of said electrolyte electrode assembly (26), and
wherein the end point of said fuel gas channel (46) is connected to a fuel gas discharge
channel (68) for emitting the fuel gas consumed in said electrolyte electrode assembly
(26), from a position spaced outwardly from the outer circumferential portion of said
electrolyte electrode assembly (26);
characterised in that said fuel gas discharge channel (68) comprises a through hole (54) extending through
said separator (28), and a discharge groove member (66) provided on the other surface
of said separator (28), said discharge groove member (66) being connected to said
through hole (54) and extending outwardly from said electrolyte electrode assembly
(26), and
a ring shaped protrusion (56) is provided on one surface of the separator (28) in
tight contact with an outer circumferential portion of the anode (24).
2. A fuel cell according to claim 1, wherein said fuel gas channel (46) includes a channel
unit (48a) provided on one surface of said separator (28), said channel unit (48a)
being connected from a fuel gas inlet (38) that supplies the fuel gas to said fuel
gas channel (46) to said fuel gas discharge channel (68).
3. A fuel cell according to claim 1 or 2, wherein said fuel gas discharge channel (164)
comprises a discharge groove (166) disposed on one surface of said separator (162)
and being connected to said fuel gas channel (46), and a lid member (168) disposed
on one surface of said separator (162) so as to cover said discharge groove (166).
4. A fuel cell according to claim 2, wherein said channel unit comprises a groove (48a).
5. A fuel cell according to claim 2, wherein said channel unit comprises a plurality
of protrusions (186).
6. A fuel cell according to claim 2, wherein said channel unit comprises a deformable
elastic channel member (196) disposed in tight contact with said anode (24).
7. A fuel cell according to claim 1, wherein said oxygen-containing gas channel (70)
comprises a deformable elastic channel member (72) disposed on the other surface of
said separator (28) in tight contact with said cathode (22).
8. A fuel cell according to claim 7, wherein an area in which said elastic channel member
(72) is disposed is smaller than a power generation area of said anode (24).
9. A fuel cell according to claim 8, wherein said elastic channel member comprises one
of an electrically conductive mesh member (72) and a felt member.
10. A fuel cell according to claim 1, wherein said oxygen-containing gas channel (144)
comprises a plurality of protrusions (146) disposed on the other surface of said separator
(142).
11. A fuel cell according to claim 10, wherein said protrusions (146) comprise a plurality
of solid portions formed by etching on one surface of said separator (142).
12. A fuel cell according to claim 2, further comprising:
an exhaust gas channel (78) for discharging the fuel gas and the oxygen-containing
gas, which are consumed during the reaction in said electrolyte electrode assembly
(26), as an exhaust gas in a stacking direction of said electrolyte electrode assembly
(26) and said separator (28);
an oxygen-containing gas supply unit (74), serving as a passage for the oxygen-containing
gas before consumption, and for supplying the oxygen-containing gas in the stacking
direction to said oxygen-containing gas channel (70); and
a fuel gas supply channel (58) provided on one surface or on the other surface of
said separator (28), said fuel gas supply channel (58) being connected to a fuel gas
supply unit (32), serving as a passage for the fuel gas before consumption, and to
said fuel gas inlet (38),
wherein said fuel gas supply unit (32) is disposed hermetically within said oxygen-containing
gas supply unit (74), and
wherein said fuel gas supply channel (58) connects said fuel gas channel (46) and
said fuel gas supply unit (32), and is provided along the separator surface so as
to intersect with said oxygen-containing gas supply unit (74) extending in the stacking
direction.
13. A fuel cell according to claim 12, wherein said exhaust gas channel (78) is disposed
around said separator (28).
14. A fuel cell according to claim 12, wherein said fuel gas supply unit (32) is disposed
hermetically at a center portion of said separator (28), and said oxygen-containing
gas supply unit (74) is disposed in an inner region of said separator (28).
15. A fuel cell according to claim 12, wherein said fuel gas inlet (38) is disposed at
a center portion of said electrolyte electrode assembly (26).
16. A fuel cell according to claim 2, further comprising:
an exhaust gas channel (78) for discharging the fuel gas and the oxygen-containing
gas, which are consumed during the reaction in said electrolyte electrode assembly
(26), as an exhaust gas in a stacking direction of said electrolyte electrode assembly
(26) and said separator (204); and
an oxygen-containing gas supply unit (240), serving as a passage for the oxygen-containing
gas before consumption, and for supplying the oxygen-containing gas in the stacking
direction to said oxygen-containing gas channel (70),
wherein said fuel gas supply unit (238) and said oxygen-containing gas supply unit
(240) are disposed hermetically within said exhaust gas channel (78),
wherein said fuel gas supply channel (58) connects said fuel gas channel (46) and
said fuel gas supply unit (238), and is disposed along the separator surface so as
to intersect with said exhaust gas channel (78) extending in the stacking direction,
and
wherein said oxygen-containing gas supply channel (252) connects said oxygen-containing
gas channel (70) and said oxygen-containing gas supply unit (240), and is disposed
along the separator surface so as to intersect with said exhaust gas channel (78).
17. A fuel cell according to claim 16, wherein said fuel gas channel (46) forms a fuel
gas pressure chamber (258a), such that said anode (24) is pressed when the fuel gas
is supplied to said fuel gas channel (46); and
said oxygen-containing gas channel (70) forms an oxygen-containing gas pressure chamber
(260), such that said cathode (22) is pressed when said oxygen-containing gas is supplied
to said oxygen-containing gas channel (70).
18. A fuel cell according to claim 1, wherein said electrolyte electrode assembly (26)
comprises a plurality of electrolyte electrode assemblies arranged concentrically
about the center of said separator (28).
19. A fuel cell (11) formed by stacking an electrolyte electrode assembly (26) and a separator
(28), said electrolyte electrode assembly (26) including an anode (24), a cathode
(22), and an electrolyte (20) interposed between said anode (24) and said cathode
(22),
said separator (28) comprising:
a sandwiching member (36) sandwiching said electrolyte electrode assemblies (26),
and having a fuel gas inlet (38) for supplying a fuel gas along a surface of said
anode (24), or an oxygen-containing gas inlet for supplying an oxygen-containing gas
along a surface of said cathode (22);
a bridge (34) connected to said sandwiching member (36), and having a reactant gas
supply channel (58) therein, for supplying the fuel gas to said fuel gas inlet (38),
or for supplying the oxygen-containing gas to said oxygen-containing gas inlet; and
a reactant gas supply unit (32) integrally connected to said bridge (34), and having
a reactant gas supply passage (30) therein, for supplying the fuel gas or the oxygen-containing
gas to said reactant gas supply channel (58),
wherein a fuel gas discharge channel (68) is disposed in said sandwiching member (36),
said, fuel gas discharge channel (68) being connected to a fuel gas channel (46) for
emitting the fuel gas consumed within said electrolyte electrode assembly (26), from
a position spaced outwardly from an outer circumferential portion of said electrolyte
electrode assembly (26),
characterised in that said fuel gas discharge channel (68) comprises a through hole (54) extending through
said separator (28), and a discharge groove member (66) provided on the other surface
of said separator (28), said discharge groove member (66) being connected to said
through hole (54) and extending outwardly from said electrolyte electrode assembly
(26); and
a ring shaped protrusion (56) is provided on one surface of the separator (28) in
tight contact with an outer circumferential portion of the anode (24).
20. A fuel cell stack formed by stacking a plurality of fuel cells (11) as claimed in
claim 1.
21. A fuel cell stack according to claim 20, wherein a fuel gas supply channel (58) is
disposed on one surface or on the other surface of said separator (28), said fuel
gas supply channel (58) being connected to a fuel gas supply unit (32), serving as
a passage for the fuel gas before consumption, and to a fuel gas inlet (38) that supplies
the fuel gas into said fuel gas channel (46).
1. Brennstoffzelle (11), die durch Stapeln einer Elektrolyt-Elektroden-Anordnung (26)
und eines Separators (28) gebildet ist, wobei die Elektrolyt-Elektroden-Anordnung
(26) eine Anode (24), eine Katode (22) und einen Elektrolyt (20), der zwischen die
Anode (24) und die Katode (22) eingefügt ist, enthält, wobei die Brennstoffzelle (11)
aufweist:
einen Brenngaskanal (46), der an einer Oberfläche des Separators (28) ausgebildet
ist, zum Zuführen eines Brenngases entlang einer Oberfläche der Anode (24); und
einen Kanal (70) für sauerstoffhaltiges Gas, der an der anderen Oberfläche des Separators
(28) ausgebildet ist, zum Zuführen eines sauerstoffhaltigen Gases entlang einer Oberfläche
der Katode (22),
wobei der Brenngaskanal (46) einen Endpunkt enthält, der in einer Position angeordnet
ist, die einem äußeren Umfangsabschnitt der Elektrolyt-Elektroden-Anordnung (26) entspricht,
und wobei der Endpunkt des Brenngaskanals (46) mit einem Brenngasauslasskanal (68)
zum Ausleiten des Brenngases, das in der Elektrolyt-Elektroden-Anordnung (26) verbraucht
wird, von einer Position, die vom äußeren Umfangsabschnitt der Elektrolyt-Elektroden-Anordnung
(26) nach außen beabstandet ist, verbunden ist;
dadurch gekennzeichnet, dass der Brenngasauslasskanal (68) ein Durchgangsloch (54), das sich durch den Separator
(28) erstreckt, und ein Auslassnutelement (66), das an der anderen Oberfläche des
Separators (28) vorgesehen ist, enthält, wobei das Auslassnutelement (66) mit dem
Durchgangsloch (54) verbunden ist und sich von der Elektrolyt-Elektroden-Anordnung
(26) nach außen erstreckt, und
ein ringförmiger Vorsprung (56) an einer Oberfläche des Separators (28) in engem Kontakt
mit einem äußeren Umfangsabschnitt der Anode (24) vorgesehen ist.
2. Brennstoffzelle nach Anspruch 1, wobei der Brenngaskanal (46) eine Kanaleinheit (48a)
enthält, die an einer Oberfläche des Separators (28) vorgesehen ist, wobei die Kanaleinheit
(48a) von einem Brenngaseinlass (38) aus, der das Brenngas zum Brenngaskanal (46)
zuführt, mit dem Brenngasauslasskanal (68) verbunden ist.
3. Brennstoffzelle nach Anspruch 1 oder 2, wobei der Brenngasauslasskanal (164) eine
Auslassnut (166), die an einer Oberfläche des Separators (162) angeordnet ist und
mit dem Brenngaskanal (46) verbunden ist, und ein Deckelelement (168), das an einer
Oberfläche des Separators (162) angeordnet ist, um die Auslassnut (166) zu bedecken,
enthält.
4. Brennstoffzelle nach Anspruch 2, wobei die Kanaleinheit eine Nut (48a) enthält.
5. Brennstoffzelle nach Anspruch 2, wobei die Kanaleinheit mehrere Vorsprünge (186) enthält.
6. Brennstoffzelle nach Anspruch 2, wobei die Kanaleinheit ein verformbares elastisches
Kanalelement (196) enthält, das in engem Kontakt mit der Anode (24) angeordnet ist.
7. Brennstoffzelle nach Anspruch 1, wobei der Kanal (70) für sauerstoffhaltiges Gas ein
verformbares elastisches Kanalelement (72) enthält, das an der anderen Oberfläche
des Separators (28) in engem Kontakt mit der Katode (22) angeordnet ist.
8. Brennstoffzelle nach Anspruch 7, wobei ein Bereich, in dem das elastische Kanalelement
(72) angeordnet ist, kleiner ist als ein Leistungserzeugungsbereich der Anode (24).
9. Brennstoffzelle nach Anspruch 8, wobei das elastische Kanalelement entweder ein elektrisch
leitfähiges Netzelement (72) oder ein Filzelement enthält.
10. Brennstoffzelle nach Anspruch 1, wobei der Kanal (144) für sauerstoffhaltiges Gas
mehrere Vorsprünge (146) enthält, die an der anderen Oberfläche des Separators (142)
angeordnet sind.
11. Brennstoffzelle nach Anspruch 10, wobei die Vorsprünge (146) mehrere massive Abschnitte
enthalten, die durch Ätzen an einer Oberfläche des Separators (142) ausgebildet sind.
12. Brennstoffzelle nach Anspruch 2, die außerdem enthält:
einen Abgaskanal (78) zum Auslassen des Brenngases und des sauerstoffhaltigen Gases,
die während der Reaktion in der Elektrolyt-Elektroden-Anordnung (26) verbraucht werden,
als Abgas in einer Stapelrichtung der Elektrolyt-Elektroden-Anordnung (26) und des
Separators (28);
eine Zuführungseinheit (74) für sauerstoffhaltiges Gas, die als Durchgang für das
sauerstoffhaltige Gas vor dem Verbrauch und zum Zuführen des sauerstoffhaltigen Gases
in der Stapelrichtung zum Kanal (70) für sauerstoffhaltiges Gas dient; und
einen Brenngaszuführungskanal (58), der an einer Oberfläche oder an der anderen Oberfläche
des Separators (28) vorgesehen ist, wobei der Brenngaszuführungskanal (58) mit einer
Brenngaszuführungseinheit (32), die als Durchgang für das Brenngas vor dem Verbrauch
dient, und mit dem Brenngaseinlass (38) verbunden ist,
wobei die Brenngaszuführungseinheit (32) innerhalb der Züführungseinheit (74) für
sauerstoffhaltiges Gas hermetisch angeordnet ist, und
wobei der Brenngaszuführungskanal (58) den Brenngaskanal (46) und die Brenngaszuführungseinheit
(32) verbindet und entlang der Separatoroberfläche so vorgesehen ist, dass er die
Zuführungseinheit (74) für sauerstoffhaltiges Gas, die sich in der Stapelrichtung
erstreckt, schneidet.
13. Brennstoffzelle nach Anspruch 12, wobei der Abgaskanal (78) um den Separator (28)
angeordnet ist.
14. Brennstoffzelle nach Anspruch 12, wobei die Brenngaszuführungseinheit (32) in einem
mittleren Abschnitt des Separators (28) hermetisch angeordnet ist, und die Zuführungseinheit
(74) für sauerstoffhaltiges Gas in einem inneren Bereich des Separators (28) angeordnet
ist.
15. Brennstoffzelle nach Anspruch 12, wobei der Brenngaseinlass (38) in einem mittleren
Abschnitt der Elektrolyt-Elektroden-Anordnung (26) angeordnet ist.
16. Brennstoffzelle nach Anspruch 2, die außerdem enthält:
einen Abgaskanal (78) zum Auslassen des Brenngases und des sauerstoffhaltigen Gases,
die während der Reaktion in der Elektrolyt-Elektroden-Anordnung (26) verbraucht werden,
als Abgas in einer Stapelrichtung der Elektrolyt-Elektroden-Anordnung (26) und des
Separators (204); und
eine Zuführungseinheit (240) für sauerstoffhaltiges Gas, die als Durchgang für das
sauerstoffhaltige Gas vor dem Verbrauch und zum Zuführen des sauerstoffhaltigen Gases
in der Stapelrichtung zum Kanal (70) für sauerstoffhaltiges Gas dient,
wobei die Brenngaszuführungseinheit (238) und die Zuführungseinheit (240) für sauerstoffhaltiges
Gas innerhalb des Abgaskanals (78) hermetisch angeordnet sind,
wobei der Brenngaszuführungskanal (58) den Brenngaskanal (46) und die Brenngaszuführungseinheit
(238) verbindet und entlang der Separatoroberfläche so angeordnet ist, dass er den
Abgaskanal (78), der sich in der Stapelrichtung erstreckt, schneidet, und
wobei der Zuführungskanal (252) für sauerstoffhaltiges Gas den Kanal (70) für sauerstoffhaltiges
Gas und die Zuführungseinheit (240) für sauerstoffhaltiges Gas verbindet und entlang
der Separatoroberfläche so angeordnet ist, dass er den Abgaskanal (78) schneidet.
17. Brennstoffzelle nach Anspruch 16, wobei der Brenngaskanal (46) eine Brenngasdruckkammer
(258a) bildet, so dass die Anode (24) gepresst wird, wenn das Brenngas zum Brenngaskanal
(46) zugeführt wird; und
der Kanal (70) für sauerstoffhaltiges Gas eine Druckkammer (260) für sauerstoffhaltiges
Gas bildet, so dass die Katode (22) gepresst wird, wenn das sauerstoffhaltige Gas
zu dem Kanal (70) für sauerstoffhaltiges Gas zugeführt wird.
18. Brennstoffzelle nach Anspruch 1, wobei die Elektrolyt-Elektroden-Anordnung (26) mehrere
Elektrolyt-Elektroden-Anordnungen enthält, die konzentrisch um die Mitte des Separators
(28) angeordnet sind.
19. Brennstoffzelle (11), die durch Stapeln einer Elektrolyt-Elektroden-Anordnung (26)
und eines Separators (28) gebildet ist, wobei die Elektrolyt-Elektroden-Anordnung
(26) eine Anode (24), eine Katode (22) und einen Elektrolyt (20), der zwischen die
Anode (24) und die Katode (22) eingefügt ist, enthält,
wobei der Separator (28) aufweist:
ein Einlege- bzw. Sandwichelement (36), das die Elektrolyt-Elektroden-Anordnungen
(26) einlegt und einen Brenngaseinlass (38) zum Zuführen eines Brenngases entlang
einer Oberfläche der Anode (24) oder einen Einlass für sauerstoffhaltiges Gas zum
Zuführen eines sauerstoffhaltigen Gases entlang einer Oberfläche der Katode (22) enthält;
eine Brücke (34), die mit dem Einlegeelement (36) verbunden ist und einen Reaktionsgaszuführungskanal
(58) darin zum Zuführen des Brenngases zum Brenngaseinlass (38) oder zum Zuführen
des sauerstoffhaltigen Gases zum Einlass für sauerstoffhaltiges Gas enthält; und
eine Reaktionsgaszuführungseinheit (32), die einteilig mit der Brücke (34) verbunden
ist und einen Reaktionsgaszuführungsdurchgang (30) darin zum Zuführen des Brenngases
oder des sauerstoffhaltigen Gases zum Reaktionsgaszuführungskanal (58) enthält,
wobei ein Brenngasauslasskanal (68) in dem Einlegeelement (36) angeordnet ist, wobei
der Brenngasauslasskanal (68) mit einem Brenngaskanal (46) zum Aussenden des innerhalb
der Elektrolyt-Elektroden-Anordnung (26) verbrauchten Brenngases von einer Position,
die von einem äußeren Umfangsabschnitt der Elektrolyt-Elektroden-Anordnung (26) nach
außen beabstandet ist, verbunden ist,
dadurch gekennzeichnet, dass der Brenngasauslasskanal (68) ein Durchgangsloch (54), das sich durch den Separator
(28) erstreckt, und ein Auslassnutelement (66), das an der anderen Oberfläche des
Separators (28) vorgesehen ist, enthält, wobei das Auslassnutelement (66) mit dem
Durchgangsloch (54) verbunden ist und sich von der Elektrolyt-Elektroden-Anordnung
(26) nach außen erstreckt; und
ein ringförmiger Vorsprung (56) an einer Oberfläche des Separators (28) in engem Kontakt
mit einem äußeren Umfangsabschnitt der Anode (24) vorgesehen ist.
20. Brennstoffzellenstapel, der durch Stapeln von mehreren Brennstoffzellen (11) nach
Anspruch 1 gebildet ist.
21. Brennstoffzellenstapel nach Anspruch 20, wobei ein Brenngaszuführungskanal (58) an
einer Oberfläche oder an der anderen Oberfläche des Separators (28) angeordnet ist,
wobei der Brenngaszuführungskanal (58) mit einer Brenngaszuführungseinheit (32), die
als Durchgang für das Brenngas vor dem Verbrauch dient, und mit einem Brenngaseinlass
(38), der das Brenngas in den Brenngaskanal (46) zuführt, verbunden ist.
1. Pile à combustible (11) formée en empilant un ensemble à électrolyte et électrodes
(26) et un séparateur (28), ledit ensemble à électrolyte et électrodes (26) incluant
une anode (24), une cathode (22) et un électrolyte (20) interposé entre ladite anode
(24) et ladite cathode (22), ladite pile à combustible (11) comportant :
un canal de gaz combustible (46) formé sur une surface dudit séparateur (28) pour
délivrer un gaz combustible le long d'une surface de ladite anode (24) ; et
un canal de gaz contenant de l'oxygène (70) formé sur l'autre surface dudit séparateur
(28), pour délivrer un gaz contenant de l'oxygène le long d'une surface de ladite
cathode (22),
dans laquelle ledit canal de gaz combustible (46) a un point d'extrémité disposé sur
une position correspondant à une portion circonférentielle extérieure dudit ensemble
à électrolyte et électrodes (26), et dans laquelle le point d'extrémité dudit canal
de gaz combustible (46) est relié à un canal d'évacuation de gaz combustible (68)
pour émettre le gaz combustible consommé dans ledit ensemble à électrolyte et électrodes
(26), à partir d'une position espacée vers l'extérieur par rapport à la portion circonférentielle
extérieure dudit ensemble à électrolyte et électrodes (26) ;
caractérisée en ce que ledit canal d'évacuation de gaz combustible (68) comporte un trou traversant (54)
s'étendant à travers ledit séparateur (28), et un élément à gorge d'évacuation (66)
agencé sur l'autre surface dudit séparateur (28), ledit élément à gorge d'évacuation
(66) étant relié audit trou traversant (54) et s'étendant vers l'extérieur à partir
dudit ensemble à électrolyte et électrodes (26), et
une saillie en forme d'anneau (56) est agencée sur une surface du séparateur (28)
en contact étroit avec une portion circonférentielle extérieure de l'anode (24).
2. Pile à combustible selon la revendication 1, dans laquelle ledit canal de gaz combustible
(46) inclut une unité de canal (48a) agencée sur une surface dudit séparateur (28),
ladite unité de canal (48a) étant reliée, à partir d'une entrée de gaz combustible
(38) qui délivre le gaz combustible audit canal de gaz combustible (46), audit canal
d'évacuation de gaz combustible (68).
3. Pile à combustible selon la revendication 1 ou 2, dans laquelle ledit canal d'évacuation
de gaz combustible (164) comporte une gorge d'évacuation (166) disposée sur une surface
dudit séparateur (162) et étant reliée audit canal de gaz combustible (46), et un
élément de couvercle (168) disposé sur une surface dudit séparateur (162) de manière
à recouvrir ladite gorge d'évacuation (166).
4. Pile à combustible selon la revendication 2, dans laquelle ladite unité de canal comporte
une gorge (48a).
5. Pile à combustible selon la revendication 2, dans laquelle ladite unité de canal comporte
une pluralité de saillies (186).
6. Pile à combustible selon la revendication 2, dans laquelle ladite unité de canal comporte
un élément de canal élastique déformable (196) disposé en contact étroit avec ladite
anode (24).
7. Pile à combustible selon la revendication 1, dans laquelle ledit canal de gaz contenant
de l'oxygène (70) comporte un élément de canal élastique déformable (72) disposé sur
l'autre surface dudit séparateur (28) en contact étroit avec ladite cathode (22).
8. Pile à combustible selon la revendication 7, dans laquelle une aire dans laquelle
ledit élément de canal élastique (72) est disposé est plus petite qu'une aire de production
d'énergie de ladite anode (24).
9. Pile à combustible selon la revendication 8, dans laquelle ledit élément de canal
élastique comporte un élément parmi un élément à mailles électriquement conducteur
(72) et un élément en feutre.
10. Pile à combustible selon la revendication 1, dans laquelle ledit canal de gaz contenant
de l'oxygène (144) comporte une pluralité de saillies (146) disposées sur l'autre
surface dudit séparateur (142).
11. Pile à combustible selon la revendication 10, dans laquelle lesdites saillies (146)
comportent une pluralité de portions pleines formées par gravure sur une surface dudit
séparateur (142).
12. Pile à combustible selon la revendication 2, comportant en outre :
un canal de gaz d'échappement (78) pour évacuer le gaz combustible et le gaz contenant
de l'oxygène, qui sont consommés pendant la réaction dans ledit ensemble à électrolyte
et électrodes (26), comme un gaz d'échappement dans une direction d'empilement dudit
ensemble à électrolyte et électrodes (26) et dudit séparateur (28) ;
une unité d'alimentation en gaz contenant de l'oxygène (74), servant de passage pour
le gaz contenant de l'oxygène avant consommation, et pour délivrer le gaz contenant
de l'oxygène dans la direction d'empilement audit canal de gaz contenant de l'oxygène
(70) ; et
un canal d'alimentation en gaz combustible (58) agencé sur une surface ou sur l'autre
surface dudit séparateur (28),
ledit canal d'alimentation en gaz combustible (58) étant relié à une unité d'alimentation
en gaz combustible (32),
servant de passage pour le gaz combustible avant consommation, et à ladite entrée
de gaz combustible (38),
dans laquelle ladite unité d'alimentation en gaz combustible (32) est disposée hermétiquement
à l'intérieur de ladite unité d'alimentation en gaz contenant de l'oxygène (74), et
dans laquelle ledit canal d'alimentation en gaz combustible (58) relie ledit canal
de gaz combustible (46) et ladite unité d'alimentation en gaz combustible (32), et
est agencé le long de la surface de séparateur de manière à croiser ladite unité d'alimentation
en gaz contenant de l'oxygène (74) s'étendant dans la direction d'empilement.
13. Pile à combustible selon la revendication 12, dans laquelle ledit canal de gaz d'échappement
(78) est disposé autour dudit séparateur (28).
14. Pile à combustible selon la revendication 12, dans laquelle ladite unité d'alimentation
en gaz combustible (32) est disposée hermétiquement sur une portion centrale dudit
séparateur (28), et ladite unité d'alimentation en gaz contenant de l'oxygène (74)
est disposée dans une zone intérieure dudit séparateur (28).
15. Pile à combustible selon la revendication 12, dans laquelle ladite entrée de gaz combustible
(38) est disposée sur une portion centrale dudit ensemble à électrolyte et électrodes
(26).
16. Pile à combustible selon la revendication 2, comportant en outre :
un canal de gaz d'échappement (78) pour évacuer le gaz combustible et le gaz contenant
de l'oxygène, qui sont consommés pendant la réaction dans ledit ensemble à électrolyte
et électrodes (26), comme un gaz d'échappement dans une direction d'empilement dudit
ensemble à électrolyte et électrodes (26) et dudit séparateur (204) ; et
une unité d'alimentation en gaz contenant de l'oxygène (240), servant de passage pour
le gaz contenant de l'oxygène avant consommation, et pour délivrer le gaz contenant
de l'oxygène dans la direction d'empilement audit canal de gaz contenant de l'oxygène
(70),
dans laquelle ladite unité d'alimentation en gaz combustible (238) et ladite unité
d'alimentation en gaz contenant de l'oxygène (240) sont disposées hermétiquement à
l'intérieur dudit canal de gaz d'échappement (78),
dans laquelle ledit canal d'alimentation en gaz combustible (58) relie ledit canal
de gaz combustible (46) et ladite unité d'alimentation en gaz combustible (238), et
est disposé le long de la surface de séparateur de manière à croiser ledit canal de
gaz d'échappement (78) s'étendant dans la direction d'empilement, et
dans laquelle ledit canal d'alimentation en gaz contenant de l'oxygène (252) relie
ledit canal de gaz contenant de l'oxygène (70) et ladite unité d'alimentation en gaz
contenant de l'oxygène (240), et est disposé le long de la surface de séparateur de
manière à croiser ledit canal de gaz d'échappement (78).
17. Pile à combustible selon la revendication 16, dans laquelle ledit canal de gaz combustible
(46) forme une chambre sous pression de gaz combustible (258a), de telle sorte que
ladite anode (24) est pressée lorsque le gaz combustible est délivré audit canal de
gaz combustible (46) ; et ledit canal de gaz contenant de l'oxygène (70) forme une
chambre sous pression de gaz contenant de l'oxygène (260), de telle sorte que ladite
cathode (22) est pressée lorsque ledit gaz contenant de l'oxygène est délivré audit
canal de gaz contenant de l'oxygène (70).
18. Pile à combustible selon la revendication 1, dans laquelle ledit ensemble à électrolyte
et électrodes (26) comporte une pluralité d'ensembles à électrolyte et électrodes
agencés de manière concentrique autour du centre dudit séparateur (28).
19. Pile à combustible (11) formée en empilant un ensemble à électrolyte et électrodes
(26) et un séparateur (28), ledit ensemble à électrolyte et électrodes (26) incluant
une anode (24), une cathode (22) et un électrolyte (20) interposé entre ladite anode
(24) et ladite cathode (22),
ledit séparateur (28) comportant :
un élément d'enserrage (36) enserrant lesdits ensembles à électrolyte et électrodes
(26), et ayant une entrée de gaz combustible (38) pour délivrer un gaz combustible
le long d'une surface de ladite anode (24), ou une entrée de gaz contenant de l'oxygène
pour délivrer un gaz contenant de l'oxygène le long d'une surface de ladite cathode
(22) ;
un pont (34) relié audit élément d'enserrage (36), et ayant un canal d'alimentation
en gaz réactant (58) dans celui-ci,
pour délivrer le gaz combustible à ladite entrée de gaz combustible (38), ou pour
délivrer le gaz contenant de l'oxygène à ladite entrée de gaz contenant de l'oxygène
; et
une unité d'alimentation en gaz réactant (32) reliée d'un seul tenant audit pont (34),
et ayant un passage d'alimentation en gaz réactant (30) dans celle-ci, pour délivrer
le gaz combustible ou le gaz contenant de l'oxygène audit canal d'alimentation en
gaz réactant (58),
dans laquelle un canal d'évacuation de gaz combustible (68) est disposé dans l'élément
d'enserrage (38), ledit canal d'évacuation de gaz combustible (68) étant relié à un
canal de gaz combustible (46) pour émettre le gaz combustible consommé à l'intérieur
dudit ensemble à électrolyte et
électrodes (26), à partir d'une position espacée vers l'extérieur par rapport à une
portion circonférentielle extérieure dudit ensemble à électrolyte et électrodes (26),
caractérisée en ce que ledit canal d'évacuation de gaz combustible (68) comporte un trou traversant (54)
s'étendant à travers ledit séparateur (28), et un élément à gorge d'évacuation (66)
agencé sur l'autre surface dudit séparateur (28), ledit élément à gorge d'évacuation
(66) étant relié audit trou traversant (54) et s'étendant vers l'extérieur à partir
dudit ensemble à électrolyte et électrodes (26) ; et
une saillie en forme d'anneau (56) est agencée sur une surface du séparateur (28)
en contact étroit avec une portion circonférentielle extérieure de l'anode (24).
20. Empilement de piles à combustible formé en empilant une pluralité de piles à combustible
(11) telles que revendiquées dans la revendication 1.
21. Empilement de piles à combustible selon la revendication 20, dans lequel un canal
d'alimentation en gaz combustible (58) est disposé sur une surface ou sur l'autre
surface dudit séparateur (28), ledit canal d'alimentation en gaz combustible (58)
étant relié à une unité d'alimentation en gaz combustible (32), servant de passage
pour le gaz combustible avant consommation, et à une entrée de gaz combustible (38)
qui délivre le gaz combustible dans ledit canal de gaz combustible (46).