JP2003272666A - Fuel cell - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To make an efficient cooling without looking for a larger size for a fuel cell, as both cooling and film moistening are maintained by a simultaneous supply of air and cooling water. <P>SOLUTION: The fuel cell is provided with a separator between adjacent unit cells 10A. The separator is provided with an air flow channel S1 at least at a surface side of a unit cell contacting an air electrode 12, and a cooling space S2 arranged at a back side connected to the air flow channel through a through-hole 143 and supplied with air and water to cool down the unit cell with latent heat of the water evaporated by heat of the unit cell transmitted to the cooling space. With this, while the unit cell is cooled down through the separator, an occlusion due to infiltration of water from the cooling space to the air flow channel is prevented. <P>COPYRIGHT: (C)2003,JPO

Description

Detailed Description of the Invention

[0001]

TECHNICAL FIELD The present invention relates to a fuel cell,
In particular, it relates to a cooling technique for a fuel cell using a separator inserted between the unit cells.

[0002]

2. Description of the Related Art A unit cell of a PEM type fuel cell, which is one type of fuel cell, includes a fuel electrode (also called a hydrogen electrode because hydrogen gas is generally used as a fuel) and an oxidizer electrode (also an oxidizer). Since air, which is a gas containing oxygen, is used, this is hereinafter referred to as an air electrode) and a solid polymer electrolyte membrane is sandwiched between the air electrode and the solid electrolyte membrane. Each of the fuel electrode and the air electrode is composed of a catalyst layer containing a catalyst substance, and an electrode base material having a function of supporting the catalyst layer and transmitting a reaction gas, and further functioning as a current collector. On the outer side of the fuel electrode and the air electrode, hydrogen and air as reaction gases are uniformly supplied from the outside of the cell to the electrode surface, and excess gas of the reaction gas is discharged to the outside of the cell (generally electrode A separator (connector plate) provided with a groove whose surface is open is stacked. This separator is
The gas is prevented from permeating and the current is collected to take out the generated current to the outside. One unit cell is composed of the unit cell and the separator as described above.

In an actual fuel cell, a stack is formed by stacking a large number of such unit cells in series. In such a fuel cell, in order to maintain sufficient power generation efficiency,
It is necessary to keep the solid polymer electrolyte membrane in the unit cell in a sufficiently wet state, and in general, the water produced by the electrolytic reaction is insufficient in water content, so a unit for supplying humidifying water to each unit cell is required. To do. Further, since the electrolysis reaction generates a heat amount of heat substantially equivalent to the generated electric power, a cooling means is provided to prevent the fuel cell main body from excessively heating up.

Various cooling means for a fuel cell have been proposed, and there is a cooling means for wetting the electrolyte membrane together with cooling (see, for example, Patent Document 1). In this technique, air to which water has been added in advance is supplied, and after cooling by evaporating water in the cooling gas passage,
A configuration is adopted in which the air containing the evaporated water is circulated in the air flow path.

In addition, a hollow portion which is separated from the gas passage is formed in the separator, and cooling water is circulated in the hollow portion, and this cooling water supplies steam to the air passage through the porous wall surface. Those that have been proposed have also been proposed (for example, refer to Patent Document 2).

[0006]

[Patent Document 1] Japanese Patent Laid-Open No. 10-247505

[Patent Document 2] Japanese Patent Laid-Open No. 6-338338

[0007]

By the way, according to the prior art, it is difficult to achieve both the cooling and the maintenance of the wetness of the film. For example, according to the one described in Patent Document 1, once the liquid water is cooled in the cooling gas passage. In order to circulate the air containing the vaporized water vapor in the air passage again, it is difficult to maintain the temperature of the cooling gas passage in the circulation passage. When the temperature rises in the flow channel, moisture is taken from the electrolyte membrane in the air flow channel, and it is difficult to keep the membrane wet.

Further, in the one described in Patent Document 2, although water vapor is supplied through the porous wall surface, it is not always said that sufficient water vapor can be supplied by the water oozing out from the porous material, and the cooling water channel However, since cooling is performed only by sensible heat, mechanical equipment and energy for circulating the cooling water may be enormous in order to perform sufficient cooling.

The present invention has been devised in view of the above circumstances, and an object thereof is to achieve both cooling and maintenance of film wetting. Furthermore, the present invention provides a fuel cell capable of efficient cooling without increasing the size of the fuel cell.

[0010]

The above-mentioned object is defined in claim 1.
In the fuel cell in which a separator is arranged between the unit cells adjacent to each other, the separator has an air flow path on the surface side in contact with at least the air electrode of the unit cell, and the air on the back side. A cooling space supplied with water is provided, and the air passage and the cooling space are communicated with each other through a through hole penetrating the separator, and air is supplied from the cooling space to the air passage through the through hole. This is achieved by a structure characterized by including an air supply structure.

In the above structure, as described in claim 2, the air supply structure is a flow passage in which the air flow passage is closed at one end thereof, and the flow passage extends from the closed end to the open end. It is effective that the through hole communicates with the cooling space at an intermediate portion.

[0012]

In the structure according to the first aspect, the heat transmitted from the unit cell that generates heat due to the electrolytic reaction to the separator evaporates water in the cooling space, and the latent heat cools the separator to cool the unit cell through the separator. To do. By this action, the unit cell can be cooled without supplying water in a water droplet state to the air flow path. Further, vapor generated by evaporation in the cooling space is ejected from the through hole to the air flow path, is supplied to the unit cell in contact with the air flow path, is absorbed, and water is added to the unit cell.

Further, according to the second aspect of the invention, water does not enter the air flow path in the form of water droplets, and only water is supplied to the air flow path in the vapor state. Therefore, the air can be smoothly supplied to the air passage without being disturbed by the water droplets.

[0014]

BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of the present invention will be described below with reference to the drawings. First, FIGS. 1 to 6 show the first embodiment of the present invention.
An embodiment is shown. FIG. 1 is a cross-sectional view showing a structure of a unit cell 10 as a unit which constitutes a fuel cell stack (hereinafter, referred to as
The vertical and horizontal relationships will be described in accordance with the arrangement posture of the unit cells), and the unit cells 10 are arranged adjacent to each other.
A separator 10B including current collecting members 14 and 15 and frames 16 and 17 is arranged between A and A.

As shown in the enlarged sectional view of FIG. 2, the unit cell 10A has a solid polymer electrolyte membrane 11 sandwiched between it and an air electrode 12, which is an oxidant electrode, stacked on one side and the other side. The fuel electrode 13 is stacked. Of these, the air electrode 12 and the fuel electrode 13 are sized to match the storage portions R1 and R2 formed in the separator 10B shown in FIG. 1, and the solid polymer electrolyte membrane 11 has the storage portions R1 and R2.
It is one size larger. In addition, the thickness of the solid polymer electrolyte membrane 11 of the unit cell 10A is set so that the collector members 14 and 15 and the frame body 16 which form the separator 10B,
Since it is extremely thin as compared with the thickness of 17, the unit cell 10 has the same size as the air electrode 12 and the fuel electrode 13 in other drawings except FIG.
The outer shape of A is shown, and the unit cell 10A is displayed as an integral member.

As shown in exploded view in FIG. 3, the separator 1
0B is a current collecting member 1 forming a pair for contacting the air electrode 12 and the fuel electrode 13 of the unit cell 10A to take out an electric current to the outside.
4 and 15 and frame bodies 16 and 17 that are superposed on them and support the unit cell 10A. Current collector 1
In this embodiment, 4 and 15 are thin metal plates, for example, having a plate thickness of about 0.1 mm. This constituent metal is a metal having conductivity and corrosion resistance, and examples thereof include stainless steel, nickel alloys, titanium alloys, and the like that have been subjected to corrosion-resistant conductive treatment.

One current collecting member 14 is made of a horizontally long rectangular plate material, and a plurality of convex portions 141 are extruded and formed by press working. These convex portions 141 are arranged in a continuous straight line and are arranged at equal intervals in parallel to the vertical sides (short sides in the illustrated form) of the plate material so as to completely cut the plate surface in the vertical direction.
Although the cross-sectional shape of these convex portions 141 is roughly shown as a rectangular wave-shaped cross section in FIG. 1 for the sake of convenience, it is more practical to have a shape in which the base side is slightly flared due to the die-cutting relationship of the press work. is there. Defined between these convex portions 141,
The groove-shaped space S1 of which the side facing the air electrode 12 (see FIG. 2) of the unit cell 10A is open is used as an air flow path for circulating air to the air electrode 12 side, as described later in detail.
The flat surface of the top portion 142 of each convex portion 141 is an abutting portion with which the air electrode 12 comes into contact. Further, the groove-shaped space S2 defined on the back side of the convex portion 141 is also used as a cooling space (in this embodiment, a flow path) which will be described later in detail. A large number of through holes 143 that penetrate the current collecting member 14 are formed in order to partially communicate the air flow path S1 and the cooling space S2. The opening positions of these through holes 143 are arbitrary, but both side surfaces of the convex portion 141 are common sense. Further, an oval hole 144 that is long in the vertical direction is formed near both ends of the current collector 14 in the lateral direction (long side in the illustrated embodiment). The elliptical hole 144 connects the current collecting member 14 to the current collecting member 15
When the separator 10B is laminated on the frame 16 and the frame 16 and 17, the hydrogen flow path L that matches and penetrates each of these members.
1 and L2.

The other current collecting member 15 is made of a rectangular plate material that matches the current collecting member 14, and a plurality of convex portions 151 are extruded by press working. The convex portion 151 is
The top portion 152 is flat, and the cross-sectional shape is substantially rectangular wave-like as in the case of the above-mentioned convex portion 141, but the convex portions 151 in this case are provided intermittently in the vertical direction. . That is, in the convex portion 151, the arrangement pitch in the horizontal direction (long side direction) is matched with the arrangement pitch of the convex portion 141 of the current collecting member 14, and the arrangement pitch in the vertical direction (short side direction) is set to an appropriate interval. It is a circular or rectangular protrusion. The cross section of the left half in FIG. 1 represents a cross section in the array portion of these convex portions 151, and the cross section of the right half represents the cross section between the array portions. Vertical and horizontal spaces S3 formed between these convex portions 151
Defines a planar space in which the side of the unit cell 10 facing the fuel electrode 13 (see FIG. 2) is open, and serves as a hydrogen flow path through which hydrogen as fuel flows. The flat surfaces of the tops 152 of the protrusions 151 are contact portions with which the fuel electrode 13 comes into contact. Further, the back side of the convex portion 151 is a short cylindrical space S4 having an open side facing the current collecting member 14, which is aligned with the space S2 of the current collecting member 14 and, as a result, through the cooling space S2. Thus, both ends are provided with openings that open to the long sides of the plate material. Similar to the current collecting member 14, the current collecting member 15 has an elliptical hole 153 that is long in the short side direction near both ends in the long side direction.
When the collector 10B is formed and the separator 10B is laminated on the current collecting members 14 and 15 and the frame bodies 16 and 17, the hydrogen flow paths L1 and L2 are formed so as to match and penetrate these members.
In this embodiment, the convex portion 151 is formed into a columnar shape that intermittently abuts the fuel electrode 13 with a small area, whereby a hydrogen flow path S3 for wetting the columnar convex portion 151 is formed vertically and horizontally. This is aimed at suppressing the retention and stagnation of the gas flow. Further, by doing so, the contact area of the hydrogen gas with respect to the fuel electrode 13 becomes large, so that improvement in power generation efficiency can be expected.

Current collecting members 14, 15 having the above-mentioned structure
Are superposed and fixed such that the respective convex portions 141 and 151 are on the outside. At this time, the convex portions 141 and 151
Thus, the plate surface portion not formed, that is, the back side surface of the hydrogen flow path S3 and the back side surface of the air flow path S1 are in contact with each other, and mutually energizable. Further, the current collecting members 14 and 15
By superimposing the space S2 between them
And a space S4 are combined to form a cooling space. Also,
When the unit cell 10A is fitted to the current collecting member 14, the open surface side of the space S1 is closed to form a tubular air passage, and a part of the wall surrounding this passage is formed of the air electrode 12. Become. Then, from this air flow path S1, the unit cell 1
Air and water are supplied to the 0 A air electrode 12. Similarly, when the unit cell 10A is fitted to the current collecting member 15, the space S
The open surface side of 3 is closed to form a planar fuel flow path,
A part of the wall surrounding this flow path is configured by the fuel electrode 13. Then, from this fuel flow path S3, the unit cell 10A
Hydrogen is supplied to the fuel electrode 13 of the.

Frames 16 and 17 are respectively stacked on the current collecting members 14 and 15 having the above-described structure. As shown in FIG. 1 and FIG. 3, the frame body 16 that is stacked on the current collecting member 14
Has a shape which is slightly larger in the vertical direction than the current collecting member 14,
The vertical frame portions 161 on both sides are connected by the upper and lower horizontal frame portions 162 and 163, and a window 164 for accommodating the convex portion 141 of the current collecting member 14 is defined in the center surrounded by these frames. . In addition, also in this frame 16, near both ends thereof,
An oval hole 165 having a position and shape that match the oval hole 144 of the current collector 14 is formed. Horizontal frame portion 16 of frame body 16
2, 163 and the vertical frame part 161 of the part where these are connected
Is thinner than the entire thickness of the vertical frame portion 161, and the horizontal frame portions 162 and 163 on the surface on which the current collecting member 14 is overlapped have a convex portion forming range of the current collecting member 14 due to the relationship between these thicknesses. At a position corresponding to, a surface receding from the contact surface with the current collecting member 14 is formed over the entire short side direction. Therefore,
In the state where the frame body 16 is superposed on the current collecting member 14, the convex portion 141 of the current collecting member 14 has the unit cell 10A inside the window 164.
In the portion that comes into contact with the air electrode 12 and faces the lateral frame portions 162 and 163, they are in contact with them. Thus,
Between the current collecting member 14 and the frame 16, the current collecting member 1 is provided on the upper side.
4 on the inner surface of the convex portion 141 and the horizontal frame portion 162, and the window 164, the convex portion 141 of the current collecting member 14 and the air electrode 1 of the unit cell 10A.
The convex portion 141 and the lateral frame portion 163 of the current collecting member 14 on the two surfaces and the lower portion.
A plurality of tubular spaces surrounded by the inner surface of the air passage define an air passage that extends completely in the longitudinal direction.

The frame body 17 to be overlaid on the current collecting member 15 is also configured to have the same size as the frame body 16, and in this case, the main body portion 1
An opening larger in the lateral direction than the window 171 is formed in 70. The height of this opening defines the height of the window 171, and the width of the opening is set to a width that matches the width between the outer ends of the elliptical holes 153 at both ends of the current collector 15. A pair of vertical frame portions 172 are provided near both ends of this opening in the width direction. The width between the vertical frame portions 172 is the width of the window 171.
The width defined by the vertical frame portions 172 and the width of the opening of the main body portion 170 is determined to match the horizontal width of the oval holes 153 at both ends of the current collector 15, and is substantially the same. An oblong hole 173 is formed that matches the position and shape of the oblong hole 153. The vertical frame portion 172 is thinner than the main body portion 170, and due to the thicknesses thereof, the convex portion of the current collecting member 15 is provided at the position where the vertical frame portion 172 on the surface on which the current collecting member 15 is stacked is provided. A surface that is recessed from the contact surface is formed by an amount corresponding to the height of the portion 151. Therefore, in the state where the frame body 17 is superposed on the current collecting member 15, the convex portion 151 of the current collecting member 15 has a portion facing the vertical frame portion 172.
The abutting relationship with the fuel electrode 72 of the unit cell 10 </ b> A in the window 171. In this way, long hole 1
In the portion sandwiched by 73, a planar hydrogen flow path S3 is formed uniformly so as to cover the convex portion 151.

The inner wall surfaces of the air flow path S1 and the cooling space S2 are hydrophilically treated. Specifically, the surface treatment may be performed so that the contact angle between the inner wall surface and water is 40 ° or less, preferably 30 ° or less. As a treatment method, a method of applying a hydrophilic treatment agent on the surface is adopted. Examples of the treatment agent applied include polyacrylamide, polyurethane resin, titanium oxide (TiO2), and the like. Other hydrophilic treatments include treatments for roughening the roughness of the metal surface. For example, plasma treatment is an example. It is preferable that the hydrophilic treatment is applied to a portion where the temperature becomes the highest, for example, the unit cell 10
The cooling space inner wall surface F1 on the back side of the top 142 of the convex portion 141 in contact with A, the air passage side wall surface F2 on the front side of the convex portion 141, the cooling space side wall surface F3 on the back side, and the air passage bottom surface F4.
It is desirable that they are processed in order of priority. Further, the inner wall surface F5 of the convex portion 151 forming a part of the cooling space S2 may be subjected to hydrophilic treatment. By applying the hydrophilic treatment, wetting of the inner wall surface is promoted and the effect of latent heat cooling of water is improved. Further, since the water will not be clogged, the air supply will not be hindered.

The separators 10B hold the current collecting members 14 and 15 by the frames 16 and 17 configured as described above.
The fuel cell stack 1 is configured by alternately stacking the separators 10B and the unit cells 10A. On the upper surface of the fuel cell stack 1 thus stacked, as shown in FIG. 4, a large number of openings of the air flow paths S1 and the cooling space S2 are formed.
The openings are alternately arranged side by side in the lateral direction, and the openings of the same arrangement are arranged in the stacking direction with an interval corresponding to the total thickness of the frame body 17 and the horizontal frame portion 162 of the frame body 16. A water intake is constructed. Further, on the lower surface of the fuel cell stack 1, air and water discharge portions having the same arrangement are also formed.

The fuel cell stack having such a structure operates as schematically shown in FIG. 5 by supplying air, water and hydrogen to each unit cell. In the case of this form, since air and water are uniformly supplied from the upper surface of the stack, the opening of the air flow path S1 is closed with a lid so that water does not directly enter the air flow path S1. Be present. That is, the air flow path S1 and the cooling space S2 are communicated with each other by the through hole 143 penetrating the separator 10B,
An air supply structure is provided so that air is supplied from the cooling space S2 to the air flow path S1 through the through holes 143. Specifically, in this air supply structure, the air flow path S1 is a flow path closed at its one end side, and the flow path communicates with the cooling space S2 by a through hole 143 at a portion in the middle of the flow path from the closed end to the open end. It consists of As shown in the figure, the air and water supplied to the cooling space S2 enter the upper part of the cooling space in a state where water droplets are mixed in the air stream in a mist state (hereinafter this state is referred to as a mixed stream). In the steady operation state of the fuel cell, the unit cell 10
Since A generates heat due to the reaction, the mixed flow in the cooling space S2 is heated. The water droplets in the mixed flow adhere to the wall surface of the cooling space S2 due to the hydrophilic treatment, evaporate by heating and take a heat from the wall surface to generate a latent heat cooling action. The water thus turned into steam passes through the through hole 143 as shown by the hatched arrow in the figure.
From the figure, the air flow path S together with the air whose flow is shown by the white arrow
1, and adheres to the air electrode 12 side of the unit cell 10A to wet the air electrode 12. Then, the excess air and steam that have entered the air flow path S1 are discharged from the air flow path opening below the cell stack. In addition, the air and water that did not enter the air flow path S1 are discharged from the opening of the cooling space S2 below the cell stack.

On the other hand, hydrogen is supplied to the fuel flow path S3 by passing through both sides of each unit cell 10 in the stacking direction thereof.
1, L2 (see FIG. 1), through one of the spaces between the vertical frame portion 172 and the convex portion 151, the fuel flow path S connected to it
It starts from 3. As a result, hydrogen is supplied to the fuel electrode 13 of the unit cell 10A. On the side of the fuel electrode 13, the excess hydrogen that has entered the fuel flow path S3 is discharged to the hydrogen flow path on the opposite side, and is discharged or collected by a pipe (not shown) connected to this hydrogen flow path.

From the above-mentioned action, in the case of this form,
Since mist-like water droplets do not directly enter the air flow into the air flow path S1, the flow of the air flow is blocked by the water drops even by the extremely thin air flow path S1 formed by press working. The advantage is that there is no fear of

Further, the air flow paths S1 and the cooling spaces S2 are alternately arranged in parallel along the electrode surface, and the convex portions 141 are mutually arranged.
Since the air and water flow along the side wall, the side wall also functions as a cooling fin. By thus alternately arranging the air flow paths S1 and the cooling spaces S2 in parallel, the cooling efficiency of the fuel cell is improved and uniform cooling is possible.

By the way, when the separator 10B is made thin and a space is provided inside the convex portion 141, the portion in contact with the unit cell 10A which is generating heat and the unit cell 10
The temperature difference between the part away from A becomes large. Therefore, even in the air flow path S1, there is a partial difference in the amount of water vapor required to reach the saturated state. For example, a portion on the electrode side having a high temperature requires a larger amount of water vapor to reach a saturated state than a portion separated from the electrode. Such a temperature difference may cause the air electrode 12 to dry. On the other hand, according to the present embodiment, by making the space the cooling space S2, the separator 10B
By uniformly cooling the whole, it is possible to suppress the occurrence of a partial temperature difference and maintain the inside of the air flow path S1 in a uniform saturated state. As a result, the air electrode 12 can be maintained in a wet state. it can.

Further, in this embodiment, the air and water flowing in from the upper opening of the separator 10B cool the current collecting members 14 and 15 mainly by latent heat cooling on the cooling space S2 side. It is not separated by the air flow path S1, but is on the back side of the portion where the current collecting members 14 and 15 are in direct contact with the electrodes. Therefore, the cooling space S
2, the tops 142 and 152 of the both convex portions 141 and 151 are closest to the electrodes and receive heat.
Since that portion is directly cooled, this portion can be cooled efficiently. In addition, the convex portion 151 has a cooling space S2.
Since a part of the fuel electrode 13 is formed, the contact surface contacting the fuel electrode 13 can be directly cooled from the back side of the convex portion 151, which is the same cooling space, to cool the fuel electrode 13. It also realizes simplification of the cooling flow path, which eliminates the need to provide a special flow path separately.

The convex portions 141 and 151 of the current collecting members 14 and 15 described above are all provided at equal intervals, and therefore, the air flow passage S1, the cooling space S2 and the fuel flow passage S3 are evenly arranged at equal intervals. However, the arrangement interval is not limited to such a configuration, and the arrangement interval may be appropriately changed depending on the distribution of air or hydrogen flowing. In addition, the arrangement direction of the air flow path S1 and the fuel flow path S3 is also along the gas flow direction.
It may be changed in any direction such as a radial arrangement.
For example, when water is supplied from the jet nozzle, water is jetted in the radial direction around the jet port of the jet nozzle. Therefore, when the tip of the nozzle is set as the radial center along the jet direction. You may arrange | position the convex part 141 along the radial direction of. Alternatively, at a position close to the injection nozzle, the interval of the convex portions 141 is narrow (width of the air flow path is narrow), and at a position away from the injection nozzle is wide (width of the air flow path is wide).
It may be configured.

FIG. 6 shown below shows a structural example of a vehicle fuel cell system using the fuel cell stack 1 according to the present invention. This fuel cell system is roughly composed of a fuel cell stack 1, a fuel supply system 2 including a hydrogen storage alloy 21 as a hydrogen supply means, an air supply system 3, a water supply system 4, and a load system 5.

In the fuel supply system 2, hydrogen released from the hydrogen storage alloy 21 via the hydrogen supply passage 20 is sent to the hydrogen passage of the fuel cell stack 1 of the fuel cell. The hydrogen supply passage 20 is provided with a hydrogen primary pressure sensor 22, a hydrogen pressure regulating valve 23, a hydrogen supply solenoid valve 24, and a hydrogen secondary pressure sensor 25 from the hydrogen storage alloy 21 side toward the fuel cell stack 1 side. . The hydrogen pressure on the hydrogen storage alloy 21 side is monitored by the hydrogen primary pressure sensor 22. The hydrogen pressure regulating valve 23 regulates the pressure suitable for supplying to the fuel cell stack 1. Also, by opening and closing the hydrogen supply solenoid valve 24,
When the supply of hydrogen to the fuel cell stack 1 is electrically controlled and hydrogen gas is not supplied, this solenoid valve 2
4 is closed and the supply of hydrogen gas is stopped. Further, the hydrogen secondary pressure sensor 25 monitors the hydrogen gas pressure immediately before being supplied to the fuel cell stack 1.

The flow of hydrogen in the fuel cell stack 1 is
As described above. In the fuel supply system 2, the hydrogen gas discharged from the hydrogen passage of the fuel cell stack 1 is released to the atmosphere via the hydrogen exhaust passage 27. The hydrogen exhaust passage 27 is provided with a check valve 28 and a solenoid valve 29. The check valve 28 prevents air from entering the fuel electrode of the fuel cell stack 1 via the hydrogen exhaust passage 27. The solenoid valve 29 is intermittently driven to achieve complete combustion of hydrogen.

In the water supply system 4, the water in the tank 40 is pressure-fed by the pump 41 to the nozzle 45 arranged in the air manifold 34, and from there, the air manifold 34.
It is ejected continuously or intermittently. As described above, this water is sent to the air flow path S1 and the cooling space S2 via the upper opening of the fuel cell stack 1. Here, the latent heat is preferentially taken from the water, so that the evaporation of the water from the electrolyte membrane 11 on the air electrode 12 side is prevented. Therefore, the electrolyte membrane 11 does not dry on the side of the air electrode 12, and always maintains a uniform wet state with the produced water. Further, the vapor supplied to the surface of the air electrode 12 is
The heat is also taken from itself and cooled, and the water flowing into the cooling space S2 also takes the heat. As a result, the fuel cell stack 1
You can control the temperature of.

That is, the fuel cell stack 1 can be sufficiently cooled without adding a cooling water system to the fuel cell stack 1. The output of the pump 41 is controlled according to the temperature of the exhaust air detected by the exhaust temperature sensor 37 to maintain the temperature of the fuel cell stack 1 at a desired temperature. A filter 42 is provided on the suction side of the pump 41, and an electromagnetic valve 43 is provided between the nozzle 45 and the pump 41. The electromagnetic valve 43 controls the injection amount from the nozzle 45. The water in the tank 40 is supplied to the surface of the fuel cell stack 1 from the nozzle 45 arranged in the air manifold 34, and this water is collected by the water condenser 46 and returned to the tank 40 by the pump 44. Tank 4
The water temperature of 0 is monitored by the water temperature sensor 47, and the water level is monitored by the water level sensor 48.

The load system 5 outputs the output of the fuel cell stack 1 to
It is taken out through the inverter 51 and drives a load such as the motor 52. The load system 5 is provided with a relay 53 for a switch. In addition, the load system 5 includes
A battery 54 is connected between the relay 53 and the inverter 51. The battery 54 accumulates the regenerative current of the motor 52 and supplements the output of the fuel cell when the output is insufficient.

The characteristic of this system is that the air flow path S1 and the cooling flow path S2 in the fuel cell stack 1 can be arranged in a unified flow path, and at the same time, air and water can be circulated. There is no need to provide a separate device.

In the first embodiment described above, the fuel electrode 1
The projections 151 of the current collecting member 15 connected to the fuel electrode 13 are formed in a columnar shape with an intermittent arrangement in order to make the flow path on the 3 side planar, but this flow path has a groove shape like the air flow path S1. In the case of the flow path of, the convex portion 151 may be a continuous ridge. The second embodiment shown in FIGS. 7 to 12 below has such a configuration. FIG. 7 is a front view of the fuel cell separator as seen from the side where the fuel electrodes are overlapped, FIG. 8 is a partial cross-sectional view of the fuel cell stack using this separator (AA cross-sectional view in FIG. 1), and FIG. 9 is the same. 1 is a partial vertical cross-sectional view of the fuel cell stack (BB cross-sectional view in FIGS. 1 and 2), FIG.
0 is a partial vertical sectional view of another portion of the fuel cell stack (see FIG.
2 is a rear view of the fuel cell separator as seen from the side where the air electrode is superposed, and FIG. 12 is a partial top view of the fuel cell stack.

Also in this embodiment, as shown in FIG. 8, the separator 10B includes collector members 14 and 15 for contacting the electrodes of the unit cell 10A to take out an electric current, and the collector members 14 and 15. Frame bodies 16 and 17 to be mounted on the peripheral end portion of 15
It has and. The current collecting members 14 and 15 are made of metal plates. The constituent metals are the same as those in the first embodiment. The current collecting member 15 contacts the fuel electrode of the unit cell 10A, and the current collecting member 14 contacts the air electrode. Current collecting member 15
As shown in FIG. 7, it is made of a rectangular plate material, and a plurality of convex portions 151 are formed by pressing. The convex portions 151 are linearly formed continuously on the short side of the plate material and are arranged at equal intervals. A groove is formed between the convex portions 151 to form a hydrogen flow path S1 through which hydrogen as fuel flows. The surface of the apex of the convex portion 151 is a contact portion 152 with which the fuel electrode comes into contact.
Further, the back side of the convex portion 151 is a groove 15a,
As shown in FIG. 9, both ends of the groove 15a do not extend to the edge portions of the plate material and are in a closed state.
Holes 153 are formed at both ends of the current collecting member 15, and when the separator 10B is laminated, the holes 153 form a hydrogen supply path.

As shown in FIG. 11, the current collecting member 14 is made of a rectangular plate material and has a plurality of convex portions 141 formed by press working. The convex portions 141 are linearly formed continuously in parallel with the short sides of the plate material and are arranged at equal intervals. A groove is formed between the convex portions 141, and an air flow path S1 through which air flows is formed. The surface of the apex portion of the convex portion 141 is a contact portion 142 with which the air electrode contacts. Further, the back side of the convex portion 141 is a groove-shaped hollow portion, and the cooling passage S2 is formed by this hollow portion. Air channel S1 and cooling channel S2
Reaches the end of the plate, and both ends are provided with openings that open at the edges of the plate. At both ends of the current collecting member 14,
When the holes 144 are formed and the separator 10B is laminated, the holes 144 form a hydrogen supply path.

The current collecting members 14 and 15 as described above are stacked and fixed so that the convex portions 141 and 151 are on the outside. At this time, the back side surface 15b of the hydrogen flow path S3 and the back side surface 14a of the air flow path S1 are in contact with each other, so that they can be energized mutually. Further, the current collecting members 14 and 15
As shown in FIG. 9, the cooling channels S2 are formed by overlapping the grooves 15a with the cooling channels S2.
Form part of. Further, as shown in FIGS. 8 and 10, the air flow path S1 is superposed on the unit cell 10A, and the opening 14b of the groove is closed to form a tubular flow path, and one of the inner walls is closed. The part is composed of an air electrode. From this air flow path S1, oxygen and water are supplied to the air electrode of the unit cell 10A.

The opening on one end side of the air flow path S1 serves as an inlet P1 through which air and water flow in, and the opening at the other end serves as an outlet P2 through which air and water flow out. The opening on one end side of the cooling flow path S2 is an inflow opening P3 into which air and water flow in, and the opening on the other end is an outflow opening P4 from which air and water flow out. In the above configuration,
The air flow paths S1 and the cooling flow paths S2 are alternately arranged in parallel and are adjacent to each other with the side wall 14c interposed therebetween. Therefore, the inlets P1 and the inflow openings P3 are also arranged alternately, and the outlets P2 and the outflow openings P4 are also arranged alternately. Further, since air and water flow along the side wall 14c, the side wall 14c also functions as a cooling fin. By arranging the air flow paths S1 and the cooling flow paths S2 alternately and in parallel, the cooling efficiency of the fuel cell is improved and uniform cooling is possible.

The current collecting members 14 and 15 include frames 16 and 17, respectively.
Are overlaid on each other. As shown in FIG. 7, the frame 17 to be stacked on the current collecting member 15 has the same size as the current collecting member 15, and a window 171 for accommodating the convex portion 151 is formed in the center. ing. Also, near both ends,
A hole 173 is formed at a position corresponding to the hole 153 of the current collecting member 15, and a concave portion is formed between the hole 173 and the window 171 on the flat surface on the side in contact with the current collecting member 15, so that the hydrogen flow is prevented. A route L3 is provided. Further, on the plane opposite to the surface in contact with the current collecting member 15, the contour is the window 17
1 is formed along with the concave portion to form the unit cell 10A.
A storage portion R2 is provided for storing the.

As shown in FIGS. 7, 9 and 10, there is a gap between the end of the convex portion 151 and the inner wall of the edge of the window 171 of the frame body 17. A hydrogen flow path S3 ′ is formed along the long side direction of the current collecting member 15. Hydrogen is supplied to each hydrogen flow path S3 by this hydrogen flow path S3 '. Also in the hydrogen flow path S3 ′,
Hydrogen is supplied to the fuel electrode.

The frame body 16 overlaid on the current collecting member 14 has the same size as the frame body 17, and has a convex portion 14 at the center.
A window 164 for storing 1 is formed. Further, in the vicinity of both ends, the holes 16 are provided at positions matching the holes 173 of the frame body 17.
5 is formed. Grooves are formed on the surface of the frame body 17 on the side where the current collecting members 14 are overlapped, along a pair of opposing long sides of the frame body 17, and by overlapping the current collecting members 14 and 15, the air flow passage L4 is formed. , L5 are configured. One end of the air flow passage L4 is connected to the opening P5 formed in the end surface on the long side of the frame body 17, and the other end is the air flow path S.
1 is connected to the inlet P1 and the inflow opening P3 of the cooling flow path S2.

The air flow passage L4 at the upstream portion gradually decreases in cross-sectional area from the opening P5 side toward the air flow path S1 side.
The inner wall of the end portion has the tapered surface 16a, which facilitates the intake of the mist-like water sprayed from the air manifold 34 described above. On the other hand, one end of the downstream air flow passage L5 is connected to the outlet P2 of the air flow passage S1 and the inflow opening P3 of the cooling flow passage S2, and the other end is formed on the long side end surface of the frame body 17. It is connected to the opened opening P6. Air flow passage L
In No. 5, the inner wall at the end is a tapered surface 16b so that the cross-sectional area gradually decreases from the opening P6 side toward the air flow path S1 side. Even when the fuel cell stack 1 is tilted, the tapered surface 16b maintains the discharge of water. Also,
A recessed portion having a contour formed along the window 164 is formed on a plane opposite to the surface of the frame body 16 that contacts the current collecting member 14, and a storage portion R1 for storing the unit cell 10A is formed. It is provided.

The configuration of the unit cell 10A in this case is the same as the configuration described in the first embodiment with reference to FIG. Further, the method of hydrophilic treatment applied to each part of the flow path and the treatment site thereof are the same as in the case of the first embodiment.

The separators 10B hold the current collecting members 14 and 15 by the frame bodies 16 and 17 configured as described above.
The fuel cell stack 1 is configured by alternately stacking the separators 10B and the unit cells 10A. 12
FIG. 3 is a partial plan view of the fuel cell stack 1. On the upper surface of the fuel cell stack 1, a large number of inlets P1 and inlet / outlet openings P1 are provided.
3 alternately open, and the inlet P1 and the inflow opening P3
In addition, as described above, the air flows in from the air manifold 34 and the water jetted from the nozzle 45 flows in at the same time. The side wall 14c is arranged in the air flow passage and also acts as a cooling fin.

When the separator is made thin and a space (S2) is provided inside the convex portion 141, the unit cell 1 which is generating heat is generated.
The temperature difference becomes large between the portion in contact with 0A and the portion separated from the unit cell 10A. Therefore, even in the air flow path, there is a partial difference in the amount of water vapor required to reach the saturated state. For example, a portion on the electrode side having a high temperature requires a larger amount of water vapor to reach a saturated state than a portion separated from the electrode. Such a temperature difference may lead to drying of the air electrode, but the cooling flow path S2 uniformly cools the entire separator to suppress the occurrence of a partial temperature difference, and the inside of the air flow path S1 is suppressed. Can be uniformly saturated, and as a result, the cathode can be maintained in a wet state.

The air and water flowing in through the inlet P1 and the inflow opening P3 provide oxygen to the air electrode in the air passage S1 and cool the current collecting members 14, 15 by latent heat cooling. Further, the air and water that have flowed in from the inflow opening P3 also cool the current collecting members 14 and 15 by latent heat cooling. Here, in the cooling flow path S2, the inner wall 14d is closest to the electrode and is where heat is generated, but by flowing air and water through the cooling flow path S2, this portion can be efficiently cooled. Further, since the groove 15a constitutes a part of the cooling flow path S2, the contact surface 152 which is in contact with the hydrogen electrode can also be directly cooled from the back side and also from the hydrogen electrode side. The cooling efficiency is further improved.

All of the convex portions 141 and 151 of the current collecting members 14 and 15 described above are provided at equal intervals, so that the air flow path S1, the cooling flow path S2 and the hydrogen flow path S3 are also provided at equal intervals. However, it is not limited to such a configuration,
The arrangement interval may be changed appropriately according to the distribution of air flow and the like. Further, the air flow passages S1 and the hydrogen flow passages S3 are not necessarily arranged in parallel, but may be arranged in any direction such as radial arrangement along the gas flow direction. For example, when water is supplied from the jet nozzle, water is jetted in the radial direction around the jet port of the jet nozzle. Therefore, when the tip of the nozzle is set as the radial center along the jet direction. The convex portions 141 may be arranged along the radial direction of. Alternatively, at a position close to the injection nozzle, the interval of the convex portions 141 may be narrowed (the width of the air passage is narrowed), and the position separated from the injection nozzle may be widened (the width of the air passage is widened). Good.

In the case of the second embodiment described above, the air flow path S1 and the cooling flow path S2 can be arranged in the same air circulation path, and at the same time, air and water can be circulated. The feature is that there is no need to separately provide.

As a modified example of the second embodiment, the flow path on the fuel electrode side may have another structure. In the modification shown in FIG. 13, the convex portion 151 of the current collecting member 15 connected to the fuel electrode is linearly formed along the long side of the current collecting member 15. With this configuration,
The hydrogen flow path S3 is arranged along the flow direction of the hydrogen gas, and has an advantage of reducing stagnation and retention due to the flow of the hydrogen gas.

In each of the above embodiments, the separator is mainly composed of a press-molded product, but the present invention is also applicable to a case where the separator is a machined product such as carbon black. . The third embodiment shown below has such a configuration. FIG.
As shown in FIG. 3, in the case of the third embodiment, the unit unit of the fuel cell includes a solid polymer electrolyte membrane 11 and an air electrode which is an oxidant electrode stacked on both side surfaces of the solid polymer electrolyte membrane 11. A unit cell including 12 and a fuel electrode 13,
Separator 14A stacked on the air electrode 12 of the unit cell
And a separator 15A stacked on the fuel electrode 13. That is, the solid polymer electrolyte membrane 11 is attached to the air electrode 12.
The fuel cell 15 and the fuel electrode 15 sandwich the unit cell, and the separators 14A and 15A sandwich the unit cell.

The separators 14A and 15A are made of a material having conductivity and corrosion resistance. For example, a metal having conductivity and corrosion resistance, graphite or the like is used. As the metal having conductivity and corrosion resistance, for example,
Examples include stainless steel, nickel alloys, titanium alloys, and the like that have been subjected to anticorrosion conductive treatment.

In the separator 14A, a plurality of oxidant gas supply grooves are formed in parallel with each other on the surface (one end surface) on the side contacting the air electrode 12, and the oxidant gas supply grooves are superposed on the air electrode 12. The air supply path S1 is formed.
The air supply path S1 is formed from one long side of the separator 14A toward the other long side, and both ends are open at each long side. A partition wall is formed by the convex portion 141 between the air supply passages S1, and an upper end portion 142 thereof is in contact with the air electrode 12.

The separator 14A has a plate-shaped main body 140 provided with an air supply passage S1 and a partition wall 141, and inside the main body 140, an air supply passage S which is an oxidant gas supply groove.
The cooling flow path S2 formed along 1 is provided.
Water flows through the cooling flow path S2 as a cooling medium for cooling the fuel cell. The cooling passages S2 are formed along the plurality of air supply passages S1 formed in the separator 14A, respectively, and as shown in FIG. 16, the cooling passages S2 are formed.
One end of 2 is connected to the supply path L6, and the other end is connected to the discharge path L7. The supply path L6 is connected to a supply line 40a of a water supply system 4 which will be described later provided outside the fuel cell stack 1, and the discharge path L7 is connected to the conversion line 40b and is not supplied to the air supply path S1. The water is returned to the water tank 40, and cooling water circulates between the fuel cell stack 1 and the water tank 40. In this way, the cooling water flows from one end of the side edge portion of the separator 14A to the other end.

A through hole 143 is connected between the air supply passage S1 and the cooling flow passage S2 as a passage which is a supply means for supplying water to the air supply passage S1. The through hole 143 is
A plurality of cooling water provided at equal intervals and flowing in the cooling flow path S2 flows into the air supply path S1 via the through holes 143. The water supplied from the through hole 143 to the air supply path S1 exerts a cooling effect due to latent heat at the time of evaporation, prevents the air electrode 13 from drying, and can always maintain a wet state.

Here, the cooling water flowing in the cooling flow passage S2 does not necessarily have to be filled in the cooling flow passage S2 without a gap, and has such a flow rate as to flow along the inner wall of the cooling flow passage S2. Good. Therefore, for example, the through hole 14
3 flows through the side surface 14e in which water is formed, water flows out from the through hole 143 to the air supply passage S1, but when it flows along a different side surface, water does not flow out to the air supply passage S1. In some cases. However, if the water flows along the inner wall of the cooling flow path S2, the separator 14A is cooled, and a sufficient cooling effect can be obtained.

In the separator 15A on the fuel electrode 13 side, a gas supply passage S3 for circulating the fuel gas is formed.
The gas supply passage S3 is formed in a direction orthogonal to the air supply passage S1 in a state where it constitutes a unit unit.
A flow path similar to the cooling flow path S2 through which the cooling medium is provided in the separator 14A may be provided in the separator 15A.

In this embodiment, the air supply passage S1 is arranged along the vertical direction when the fuel cell unit is set in the used state. With this configuration, the cooling water supplied to the air supply passage S1 can be dropped and easily discharged from the air supply passage S1.

As shown in FIG. 17, the fuel cell stack 1 is constructed by stacking a plurality of fuel cell unit units constructed as described above, that is, connecting them in series. In addition, in the configuration of the separator 14A, the cooling water may flow in a direction opposite to the air flow direction in the air supply passage S1.

As the structure of the fuel cell separator 14A described above, it is possible to adopt other structures as exemplified below. As a first modified example, the discharge water L7 is not provided, and the cooling water supplied to the cooling flow path S2 has the through holes 14
It is also possible to adopt a configuration in which all the air flows out to the air supply path S1 via In this case, for example, as shown in FIG. 19, along the parallel facing edges (upper side and lower side) of the separator 14A, the supply paths L6a and L6b are respectively provided.
And the cooling channels S2a and S2b are alternately connected to each of the supply channels L6a and L6b. In this configuration, the cooling water flows from the upper side to the lower side in the cooling flow path S2a, and the cooling water flows from the lower side to the upper side in the cooling flow path S2b. That is, the cooling water flows in the opposite directions. Since the cooling water flows in the flow path while exchanging heat, the temperature of the cooling water increases toward the downstream side and the cooling effect decreases. However, as in this embodiment, the separators 14A can be cooled more uniformly by alternately setting the circulation directions of the cooling water to the opposite directions.

Alternatively, as a second modification, the discharge passage L7 is not provided and the lower end of the cooling passage S2 is entirely separated by the separator 1.
The cooling water may be discharged to the outside from the lower end side of 4A. In this case, the waste water can be collected in a water collecting tray provided on the lower side of the fuel cell stack 1 and returned to the tank 40 described later.

As a third modification, as shown in FIG. 20, the cooling passage S2c may be formed in a direction intersecting with the air supply passage S1.

As a fourth modification, as shown in FIG. 21, a cooling passage S2 can be formed in the partition wall 141. Since the partition wall 141 contacts the air electrode 12, when the cooling flow path S2 is formed in the partition wall 141, the position of the refrigerant approaches the air electrode 12 and the cooling effect is improved. Further, in this case, the through hole 14 communicating with the air supply passage S1
3 will be formed on the side wall surface 14c of the air supply path S1. By providing the through hole 143 in the side wall surface 14c, the cooling water supplied to the air supply path S1 can be supplied to the air electrode 12.
It becomes easier to contact the electrode, and the effect of maintaining the electrode in a wet state can be surely exhibited.

As a fifth modification, as shown in FIG. 22, a cooling passage S2 is formed in the partition wall 141,
A through hole 143 may be formed in the upper end portion (contact surface) 142 of the partition wall 141 with the air electrode 12. In this configuration, the cooling water is directly supplied to the air electrode 12 from the through hole 143, and the air electrode 1
2 can be prevented from drying.

As a sixth modification, as shown in FIG. 23, a separator 14A is superposed on the air supply path constituting member 14Aa having a corrugated flat section and on the back side thereof. It is also possible to adopt a configuration including a flat plate-shaped back member 14Ab. A planar cooling flow path S2 is formed in the gap between the back surface member 14Ab and the air supply path forming member 14Aa, and a groove-like flow path S is formed in the partition wall 141.
2'is formed. With such a configuration, the range filled with cooling water is increased and the cooling effect is improved. Further, the through hole 143 has a bottom surface 14f in the air supply passage S1.
And can be formed on any of the side wall surfaces 14c of the air supply path S1.

Next, the structure of the fuel cell system using the fuel cell stack 1 having the above structure will be described. As shown in FIG. 24, this fuel cell system is roughly composed of a fuel cell stack 1, a fuel supply system 2 including a hydrogen storage alloy 21, an air supply system 3, a water supply system 4 and a load system 5.

In the fuel supply system 2, hydrogen released from the hydrogen storage alloy 21 via the hydrogen supply passage 20 is sent to the hydrogen gas passage S3 of each unit of the fuel cell stack 1. A hydrogen pressure regulating valve 23 is arranged in the hydrogen supply passage 20 to regulate the pressure of hydrogen gas released from the hydrogen storage alloy 21. Reference numeral 24 is a hydrogen supply solenoid valve, which controls opening / closing of the hydrogen supply passage 20. The hydrogen gas pressure immediately before being supplied to the fuel cell stack 1 is monitored by the hydrogen pressure sensor 25.

In the fuel supply system 2, the hydrogen gas discharged from the fuel cell stack 1 is discharged to the atmosphere via the hydrogen discharge passage 27. The hydrogen discharge passage 27 is provided with a check valve 28 and a solenoid valve 29. The check valve 28 is the hydrogen exhaust passage 2
It is possible to prevent air from entering the fuel electrode of the fuel cell stack 1 via 7. The solenoid valve 29 is intermittently driven to achieve complete combustion of hydrogen.

The air supply system 3 supplies air from the atmosphere to the air flow path S1 of the fuel cell stack 1,
The air discharged from the air passes through the water condenser 46 and is discharged. The air supply path 30 is provided with a fan 31 and sends air from the atmosphere to the air manifold 34. Air flows from the manifold 34 into the air supply path S1 of the fuel cell stack 1 to supply oxygen to the air electrode 12. Water discharged from the fuel cell stack 1 is condensed and recovered by the water condenser 46 and is discharged to the atmosphere. The temperature discharged from the fuel cell stack 1 is monitored by the exhaust temperature sensor 37.

From the cooling water flow passage S2 to the air supply passage S1
Most of the cooling water sent to reaches the water condenser 46 while maintaining the liquid state, and is sent to the tank 40 as it is for recovery. Part of the supplied water evaporates and the water condenser 4
It is condensed and recovered at 6. It is considered that some of the water vapor contained in the exhaust air is caused by the reaction water accompanying the power generation reaction of the fuel cell stack 1.

The water supply system 4 pumps the water in the tank 40 into the pump 4
1, the cooling water supply path L6 of each fuel cell unit is
A part of the cooling water that has been pressure-fed through the pipe 40a to the pipe 40 is supplied from the discharge path L7 of each fuel cell unit.
It collects in the tank 40 via b. In each fuel cell unit, the water supplied from the through hole 143 to the air supply path S1 is recovered by the water condenser 46 and returned to the tank 40. Of course, since it is impossible to completely close the water supply system 4, the water level of the tank 40 is monitored by the water level sensor 48, and when this water level exceeds a predetermined threshold value, water is replenished from the outside. A heater 49 and an antifreezing electromagnetic valve 40c are attached to the tank 40 so that the water in the tank 40 does not freeze in winter. An electromagnetic valve 40d is attached to a pipe connecting the water condenser 46 and the tank 40.
It prevents the water inside from evaporating. Exhaust temperature sensor 3
It is possible to control the output of the pump 41 according to the temperature of the exhaust air detected in 7 and adjust the amount of circulating cooling water to maintain the temperature of the fuel cell stack 1 at a desired temperature.

The load system 5 takes out the output of the fuel cell stack 1 to the outside and drives the load such as the motor 52. The load system 5 is provided with a relay 53 for a switch and a secondary battery 54 serving as an auxiliary output source, and a rectifying diode 55 is interposed between the secondary battery 54 and the relay 53. The output of the fuel cell stack 1 itself is constantly monitored by the voltage sensor 56. Based on the monitor result, the opening / closing of the hydrogen exhaust solenoid valve 29 is controlled by a control circuit (not shown).

[0076]

According to the structure of claim 1 of the present invention, the air passage and the cooling space are separated from each other on the front and back sides of the separator, so that the separator is provided with a special separating means or a cooling plate. Is prevented from thickening. Also,
Since the separator is directly subjected to latent heat cooling on the cooling space side, the cooling efficiency is higher than in the case of cooling by the cooling plate, and uniform cooling can be performed. Further, conventionally, in the case of a system that simultaneously supplies air and cooling water, there is concern that water droplets of cooling water may adhere to the air electrode surface or that water may become clogged in the air flow path. The cross-sectional area is wide, and the height of the grooves that make up the air flow path is particularly high, which has been an obstacle to reducing the size and weight of the fuel cell. Since the water is supplied in this way, the supply of the air to the electrode is not obstructed by the water droplets even by the air passage having the small cross-sectional area. Therefore, with this configuration, it is possible to reduce the thickness of the separator,
Further, the fuel cell stack can be reduced in size and weight.

According to the second aspect of the invention, the air supplied into the cooling space and saturated with steam by latent heat cooling is supplied to the air flow path through the through hole. In the flow path, it is possible to prevent liquid water from being taken away from the air electrode, and it is possible to sufficiently keep the electrode wet.

[Brief description of drawings]

FIG. 1 is a partial transverse cross-sectional view of a unit cell constituting a fuel cell according to a first embodiment of the present invention.

FIG. 2 is a cross-sectional view of a unit cell that constitutes a unit cell.

FIG. 3 is an exploded perspective view of a separator that constitutes the unit cell of the first embodiment.

FIG. 4 is a partial top view of a fuel cell stack in which the unit cells of the first embodiment are stacked.

FIG. 5 is a schematic view showing a cooling mechanism by the separator of the first embodiment.

FIG. 6 is a configuration diagram of a fuel cell system.

FIG. 7 is an overall front view of a separator that constitutes a fuel cell according to a second embodiment of the present invention.

FIG. 8 is a partial cross-sectional view of a fuel cell stack according to a second embodiment.

9 is a vertical cross-sectional view taken along the line BB of FIG.

10 is a vertical cross-sectional view taken along line CC of FIG.

FIG. 11 is an overall rear view of the separator according to the second embodiment.

FIG. 12 is a partial top view of the fuel cell stack according to the second embodiment.

FIG. 13 is a front view showing a modification of the separator of the second embodiment.

FIG. 14 is a side sectional view of a fuel cell unit constituting a fuel cell according to a third embodiment of the present invention.

FIG. 15 is a partial cross-sectional view of a separator of a fuel cell according to a third embodiment.

FIG. 16 is an overall front view of a fuel cell separator according to a third embodiment.

FIG. 17 is a partially enlarged view of the separator of the fuel cell according to the third embodiment.

FIG. 18 is a partially enlarged perspective view of a fuel cell stack according to a third embodiment.

FIG. 19 is an overall front view of a fuel cell separator according to a modification of the third embodiment.

FIG. 20 is a partial cross-sectional view of a fuel cell separator according to another modification.

FIG. 21 is a partial cross-sectional view of a fuel cell separator according to another modification.

FIG. 22 is a partial cross-sectional view of a fuel cell separator according to another modification.

FIG. 23 is a partial cross-sectional view of a fuel cell separator according to another modification.

FIG. 24 is a configuration diagram of a fuel cell system according to a third embodiment.

[Explanation of symbols]

10A unit cell 10B separator 12 air poles 141 convex 143 through holes 34 manifold S1 air flow path S2 cooling space

   ─────────────────────────────────────────────────── ─── Continued front page    (72) Inventor Masataka Ueno             2-19-12 Sotokanda, Chiyoda-ku, Tokyo Stock             Inside the company Equus Research F-term (reference) 5H026 AA06 CC03 CC08                 5H027 AA06 CC06

Claims (2)

[Claims] 1. A fuel cell in which a separator is disposed between unit cells adjacent to each other, wherein the separator has an air flow path on at least a surface side of the unit cell which is in contact with an air electrode and air and water on a back side thereof. A cooling space supplied with, the air flow path and the cooling space are communicated by a through hole penetrating the separator,
A fuel cell comprising an air supply structure for supplying air from a cooling space to an air flow path through a through hole. 2. The air supply structure is a flow path in which the air flow path is closed at one end side thereof, and the flow path connects the cooling space to the cooling space at an intermediate part from the closed end to the open end. The fuel cell according to claim 1, wherein the fuel cell is configured by communicating with each other.