JP6345014B2 - Diffuser for fuel cell - Google Patents

Description

The present invention relates to a diffuser used in a polymer electrolyte fuel cell. That is, the present invention relates to a diffuser for adjusting and distributing the flow of a reaction gas supplied to a power generation region of a fuel cell.

A polymer electrolyte fuel cell uses a membrane such as an ion exchange resin having ionic conductivity as a polymer electrolyte membrane, and a cathode electrode (positive electrode) and an anode electrode (negative electrode) on both sides of the polymer electrolyte membrane. A membrane electrode assembly (MEA) is formed by arranging both electrodes, and for example, a fuel gas such as hydrogen gas is supplied to the negative electrode side, and an oxidizing gas such as oxygen gas or air is supplied to the positive electrode side to perform an electrochemical reaction. By causing it to occur, the chemical energy of the fuel gas is converted into electricity and electricity is generated. Usually, a separator is provided on both sides of the MEA to form a single cell.

A polymer electrolyte fuel cell is usually formed by laminating a plurality of single cells containing the MEA. In each single cell, the MEA and the separator are sealed so that fuel gas and oxidizing gas do not leak out. In order to increase the power generation efficiency of the battery, these reaction gases need to be distributed throughout the power generation region of the MEA. A coolant is circulated between the stacked single cells to cool the fuel cell.

In order to efficiently distribute the reaction gas over the entire power generation region of the MEA, a member for dispersing the reaction gas, such as a diffuser or a gas distribution unit, may be provided in the reaction gas flow path. The diffuser may be formed on the separator or may be formed on the MEA. Preferably, the diffuser is formed integrally with the separator or MEA.

Various techniques have been developed as a technique for integrally forming a diffuser for distributing such a reaction gas into a separator or MEA.
For example, in Patent Document 1, a gas inlet distribution unit (diffuser) is provided between a gas supply manifold and a power generation region, and the gas distribution unit extends in a direction perpendicular to the gas flow direction of the power generation region. A technique that includes n distribution ribs having a plurality of slits is disclosed. According to the gas inlet distributor, the reaction gas can be evenly distributed to the power generation region.

Republished patent WO2011 / 033745

The diffuser is provided to increase the power generation efficiency of the fuel cell, but there is still room for improvement from the viewpoint of improving the power generation efficiency. An object of the present invention is to provide a diffuser that can contribute to further improvement in power generation efficiency of a fuel cell.

The inventors have conducted various studies and tests to increase the power generation efficiency of the fuel cell by using the diffuser. During the test, the case where the power generation efficiency does not increase despite the installation of the diffuser, However, I found that there are cases where it declines. In the course of further examination and testing while changing the diffuser in various ways, the diffuser has a considerable influence on the degree of contact between the MEA electrode and the separator in the vicinity of the diffuser, which affects the power generation efficiency of the fuel cell. I found out that It has been found that the power generation efficiency of the fuel cell can be improved by ensuring the contact between the MEA electrode and the separator in the vicinity of the diffuser.

As a result of intensive studies based on the above findings, the inventors have found that the above object can be achieved by configuring a diffuser with a foamed rubber material having a predetermined hardness, and completed the present invention.

The present invention is a diffuser for distributing reaction gas supplied to a power generation region of a fuel cell, and the diffuser is mainly composed of foam rubber, and the hardness of the foam rubber is 10 to 50 in Asker C. A diffuser for a fuel cell (first invention).

In the present invention, it is formed so that 0.1 * Wm ≦ Hm ≦ 0.8 * Wm, where Wm is the minimum width dimension of the planar pattern of the diffuser and Hm is the height dimension of the minimum width portion of the diffuser. Is preferred (second invention). Furthermore, in the second invention, it is preferable to form a planar pattern in which 20 to 200 dots are scattered per square centimeter (third invention).

According to the diffuser of the present invention (first invention), the contact between the electrode of the membrane electrode assembly (MEA) and the separator in the vicinity of the diffuser is ensured, and the power generation efficiency of the fuel cell is increased.

Further, in the case of the second invention or the third invention, the function of distributing the reaction gas of the diffuser is high, and the power generation efficiency of the fuel cell is further increased.

The schematic longitudinal cross-sectional view of the single cell which comprises a polymer electrolyte fuel cell. The perspective view which shows the external appearance of a membrane electrode assembly. The top view which shows the external appearance of a membrane electrode assembly. The exploded view which shows the structure of a membrane electrode assembly. The figure which shows the example of the planar pattern of a diffuser. The figure which shows the example of the cross section of the diffuser integrally molded by the flame | frame. The schematic diagram which shows the process of integrally forming a diffuser in a flame | frame. The conceptual diagram which shows the example of the process of manufacturing a membrane electrode assembly.

Embodiments of the present invention will be described below with reference to the drawings. In addition, this invention is not limited to the separate embodiment shown below, The form can also be changed and implemented.

First, the configuration of the fuel cell will be described. FIG. 1 is a schematic longitudinal sectional view of a single cell 1 constituting a solid polymer fuel cell, and the fuel cell is usually configured as a laminate (not shown) in which a plurality of single cells 1 are stacked.

In FIG. 1, a single cell 1 is composed of a membrane electrode assembly (MEA) 2 and separators 5 and 6. The membrane electrode assembly (MEA) 2 has a polymer electrolyte membrane 21 and a cathode electrode 24 and an anode electrode 25 disposed on both sides of the polymer electrolyte membrane 21. FIG. 1 is a cross section of a single cell of a fuel cell in a plane perpendicular to the flow direction of a reaction gas. In the single cell 1, the cathode electrode 24 and the anode electrode 25 are provided so as to contact the cathode electrode side separator 5 and the anode electrode side separator 6, respectively. A groove 7 for supplying an oxidizing gas is provided on the electrode 24 side of the cathode electrode side separator 5, and a groove 8 for supplying a fuel gas is provided on the electrode 25 side of the anode electrode side separator 6. The groove 8 communicates with the gas supply manifold and the groove 8 communicates with the fuel gas supply manifold.

In the unit cell 1, in order to prevent the fuel gas and the oxidizing gas from leaking around the membrane electrode assembly (MEA) 2 composed of the polymer electrolyte membrane 21, the cathode electrode 24 and the anode electrode 25, Frame-shaped (loop-shaped) packings (seal) 9 and 9 are interposed between the separators 5 and 6. In FIG. 3 and FIG. 5, the example of the seal line of the packing 9 is shown with the broken line. In the present embodiment, the packing 9 is formed in a frame shape on the peripheral surfaces of the separators 5 and 6 in advance and integrated. Therefore, in the fuel cell assembly state shown in FIG. 1, the packings 9 and 9 are bonded and integrated with the separators 5 and 6, and contacted and pressed with the membrane electrode assembly 2, so that the peripheral portion Gas seal. In addition, what is necessary is just to perform by the well-known technique about the specific aspect of a seal | sticker.

The structure of the membrane electrode assembly (MEA) 2 will be described in more detail with reference to FIGS. 2 is a perspective view of the MEA, FIG. 3 is a front view, and FIG. 4 is an exploded view of the MEA. The MEA 2 is configured to include a polymer electrolyte membrane 21, a frame 22, a cathode electrode 24, an anode electrode 25, and a diffuser 23. The frame 22 is a resin film member formed in a frame shape. A polymer electrolyte membrane 21 is attached to a hole portion provided in the center of the frame 22, and a cathode electrode 24 and an anode electrode 25 are provided on both sides of the polymer electrolyte membrane 21 to constitute a main body of the MEA 2. Yes.

In the present embodiment, two frames 22 are provided, and the two are integrated so that the periphery of the polymer electrolyte membrane 21 is sandwiched therebetween. A catalyst layer is provided between the electrodes 24 and 25 and the polymer electrolyte membrane 21. A so-called Nafion membrane (NAFION is a registered trademark of DuPont) can be used as the polymer electrolyte membrane 21, and carbon felt or the like can be used as the electrodes 24 and 25. The integration of the polymer electrolyte membrane 21, the frame 22, and the electrodes 24 and 25 and the formation of the catalyst layer can be performed by a known technique.

The frame 22 is made of a resin film. Examples of the synthetic resin used as the material for the resin film include thermoplastic resins such as polyethylene terephthalate resin (PET resin), polyethylene naphthalate resin (PEN resin), polyimide resin (PI resin), and polyphenylene sulfide resin (PPS resin). The The resin material of the frame is required to have heat resistance enough to prevent deformation at the operating temperature of the fuel cell and the processing temperature of the sealing material and diffuser integration process. The frame 22 is formed in a frame shape in which a large hole is provided in the center for attaching the polymer electrolyte membrane 21. This hole becomes a power generation region of the fuel cell. Reactive gas manifolds 221 and 221 and cooling water manifolds 222 and 222 are provided on both sides of the frame 22. When a plurality of MEAs are stacked, the manifolds 221 and 222 become passages that communicate with each other in the stacking direction, and reaction gas and cooling water flow through the manifold. In each single cell, the reaction gas flows between the reaction gas manifolds arranged in a diagonal line of the substantially rectangular frame 22, and the reaction gas is supplied to the power generation region.

A diffuser 23 is formed on the frame 22. The diffuser 23 is provided in a partial region on the frame so as to face the separators 5 and 6 when the frame is incorporated into the MEA or single cell. The diffuser 23 is provided in a portion between the reaction gas manifold 221 and the power generation region. In other words, the diffuser 23 is provided in the reaction gas passage formed between the frame 22 and the separators 5 and 6 so as to be adjacent to the power generation region (polymer electrolyte membrane). Are distributed throughout the power generation area. In the present embodiment, the diffuser 23 is provided in the MEA 2 (frame 22), but the diffuser 23 may be provided in the separators 5 and 6.

In the present embodiment, the diffuser 23 is provided both upstream and downstream of the power generation region. Although the diffuser 23 may be provided only on the upstream side or only on the downstream side, it is preferable to provide the diffuser 23 on both sides from the viewpoint of improving the uniformity of the reaction gas distribution.

The form of the diffuser 23 is such that fine diffuser elements having a rod-like or dot-like shape are dispersedly arranged in a specific plane pattern. In the present embodiment, as shown in FIGS. 3 and 5A, rod-like diffuser elements are radially distributed from the reaction gas manifold 221 toward the power generation region. The reaction gas flows between the frame 22 and the separators 5 and 6 so as to avoid the diffuser element. Therefore, the reaction gas can be uniformly distributed from the reaction gas manifold 221 to the power generation region by adjusting the size, spacing, and arrangement of the diffuser elements. Specifically, the flow path portion between the diffuser elements is made relatively wide and straight in the portion where the reaction gas is more desired to flow, and the portion between the diffuser elements is less likely to flow the reaction gas. The distribution property of the reaction gas is adjusted so that the flow path portion is a relatively narrow and bent labyrinth.

FIG. 6 shows a cross section of the diffuser 23 and the frame 22. Each diffuser element is provided so as to protrude from the surface of the frame 22 at a height Hm. The height Hm of the diffuser element is preferably set to be larger than the gap between the frame 22 and the separators 5 and 6 in the single cell 1 and preferably about 5 to 50% larger than the gap dimension. . If it does so, each diffuser element will be provided like a pillar or a wall between the flame | frame 22 and the separators 5 and 6, and the distribution function of the reaction gas of the diffuser 23 will become more reliable. .

The planar pattern of the diffuser 23 may be another pattern. For example, a configuration in which a large number of dot-like diffuser elements are scattered like a diffuser 23b shown in FIG. The dot-like diffuser element may be in the form of a circle, an ellipse, a square, a triangle, or the like. Alternatively, as in the diffuser 23c shown in FIG. 5 (c), a plurality of rod-like diffuser elements are arranged so as to extend in a direction perpendicular to the overall flow direction of the reaction gas, and the space between the diffuser elements is a maze. It may be in the form of a (labyrinth) shape. Further, the rod-like diffuser element may be a linear element or a curved element.

Minimum width dimension Wm in the planar pattern of the diffuser 23 (in the case of a rod-like diffuser element as shown in FIGS. 5A and 5C, the width dimension Wm of the rod-like element, a dot-like diffuser as shown in FIG. 5B) If it is an element, the short dimension Wm) of the dot-like element is preferably 0.2 mm to 3 mm, and typically 0.3 mm to 1 mm.
Preferably, the minimum width dimension Wm of the planar pattern of the diffuser 23 and the height of the diffuser (particularly the height at the minimum width portion) Hm are 0.1 * Wm ≦ Hm ≦ 0.8 * Wm. It is preferable that a diffuser is formed, and the diffuser thus formed has a high reaction gas distribution function.
The height Hm of the diffuser is preferably set to 0.05 mm to 0.8 mm, more preferably 0.1 mm to 0.6 mm.

When the diffuser is a rod-like diffuser element as shown in FIGS. 5 (a) and 5 (c), the number of diffuser elements measured in a direction substantially orthogonal to the direction in which the diffuser element extends is It is preferable to be 4 pieces / cm to 15 pieces / cm. When the diffuser is a group of dot-shaped diffuser elements as shown in FIG. 5B, the number of diffuser elements is set to 20 / square cm to 200 / square cm. It is particularly preferable that 40 / square cm to 120 / square cm. It is preferable that the diffuser elements are fine and arranged at a high density because the function of distributing the reaction gas is enhanced.

Further, the diffuser element is provided such that the ratio of the area occupied by the diffuser element to the area of the partial region on the frame where the diffuser is provided is 5% to 50%, more preferably 10% to 30%. A larger proportion of the area occupied by the diffuser element tends to improve the reaction gas distribution function, but if the proportion is too large, the flow of the reaction gas becomes worse.

  The diffuser 23 is formed mainly of an elastomer having elasticity, particularly a crosslinked foamed rubber material. The rubber hardness of the foamed rubber material constituting the diffuser is 10 to 50, more preferably 20 to 40 by Asker C. When the hardness of the diffuser is within this range, the predetermined force of the diffuser can be maintained and its rectification and gas distribution function can be exhibited while sufficiently reducing the reaction force of the diffuser portion.

Examples of the rubber material forming the diffuser include isoprene rubber, hydrogenated isoprene rubber, ethylene propylene rubber, butadiene rubber, butyl rubber, urethane rubber, and silicone rubber. Hydrogenated isoprene rubber is particularly preferable. The rubber material is preferably crosslinked with an isocyanate compound or an organic peroxide. As a foam material for making the rubber material forming the diffuser into a foamed rubber, a heat-expandable microcapsule (for example, a liquid that is expanded by heating, which is sold under a trade name such as expander or microsphere) is used as a polymer shell. Examples include chemical foaming agents such as encapsulated microcapsules), azodicarbonamide (ADCA), oxybisbenzenesulfonyl hydrazide (OBSH), dinitrosopentamethylenetetramine (DPT), and sodium bicarbonate. In particular, foaming with a thermally expandable microcapsule is preferable because the residue of the foamed material is not eluted when the fuel cell is used and the catalyst is not poisoned. Thermally expandable microcapsules are sold by Matsumoto Yushi Seiyaku Co., Ltd. under the trade name Matsumoto Microsphere, and from Nippon Ferrite Co., Ltd. under the trade name Expandan. When cracked gas, cracked residue, etc. are generated from the foamed material, it is preferable to remove them before incorporating them into the fuel cell.

In this embodiment, hydrogenated isoprene rubber blended with thermally expandable microcapsules as a foaming material is crosslinked with an isocyanate compound to form the diffuser 23. More specifically, 1-10 parts by weight of heat-expandable microcapsules having a foaming start temperature of 110-170 ° C. are blended with 100 parts by weight of rubber material, and heated to expand / crosslink, whereby the Asker C hardness is 30 Thus, the diffuser 23 is formed as foamed rubber having a foaming ratio of 4 times. The diffuser 23 is preferably formed using screen printing, as will be described later.

A method for manufacturing a membrane electrode assembly including the above diffuser will be described. FIG. 7 shows a series of steps (diffuser forming step) for integrally forming the diffuser 23 on the frame 22 (or the resin film PF processed into the frame).

First, an uncrosslinked liquid rubber material blended with a foam material is prepared. The uncrosslinked rubber to be used is blended with a foaming material, a crosslinking agent, etc., and the viscosity is adjusted to obtain an uncrosslinked liquid rubber material applicable to screen printing described later. The viscosity is adjusted by adjusting the amount of the filler and solvent so as to obtain a so-called paste or liquid level. As the filler, carbon black such as furnace black, acetylene black and thermal black, and white filler such as silica, talc and clay can be used. In the present embodiment, carbon black is preferably used.

A screen printing mask M provided with openings corresponding to the planar pattern of the diffuser to be formed is prepared. The opening pattern of the mask is preferably slightly smaller than the size of the diffuser element of the diffuser in consideration of the degree of foaming.

A diffuser 23 is formed at a predetermined position of the frame 22 using screen printing. The screen printing process may be performed on the frame 22 that has already been processed into a frame shape, or may be performed on the resin film PF that has not been processed into a frame.
First, as shown in FIG. 7A, a mask M is overlaid and brought into close contact with a position where a diffuser of the frame 22 (resin film PF) is to be formed.

In this state, as shown in FIG. 7B, an uncrosslinked liquid rubber material blended with a foam material is placed on the mask M, and the liquid rubber material is pressed against the mask by the squeegee SQ. Is filled with a liquid rubber material. Thereafter, as shown in FIG. 7C, when the mask M is removed from the frame 22 (resin film PF), the liquid rubber material filled in the openings of the mask M is moved to the frame 22 (resin film PF) side. Remaining, a diffuser precursor 23P having a diffuser planar pattern is formed of uncrosslinked rubber. That is, the diffuser precursor 23P having a predetermined pattern is formed by an uncrosslinked and unfoamed rubber material by screen printing.

Since the diffuser precursor 23P is unfoamed, its height Hs is smaller than the height Hm of the diffuser 23 to be finally formed. The height Hs of the diffuser precursor can be adjusted by setting the thickness of the mask M. The ratio of Hm to Hs is set to 1.2 to 5 times, more preferably 1.5 to 4 times.

Thereafter, the diffuser precursor 23P is foamed and crosslinked. Foaming is typically performed by heating to the foaming temperature of the foamed material. Crosslinking is performed by heating to the decomposition temperature of peroxide in the case of organic peroxide crosslinking, irradiation of radiation in the case of radiation crosslinking, and irradiation of ultraviolet rays in the case of ultraviolet crosslinking. The ratio between the height Hs of the diffuser precursor and the height Hm of the diffuser can be adjusted by adjusting the blending amount of the foam material, the starting conditions for foaming and crosslinking, and the like. In this embodiment, the foaming / crosslinking is carried out at 150 ° C. for 10 minutes for primary crosslinking and for 1 hour at 120 ° C. for secondary crosslinking.

By performing foaming and crosslinking, the diffuser precursor 23P expands to become a diffuser 23 having a height Hm, and a frame 22 (resin film PF) in which the diffuser 23 is integrally formed is obtained.

In FIG. 8, the example of the manufacturing process in which the membrane electrode assembly (MEA) 2 is manufactured is shown. In this example, a frame is manufactured after a screen is continuously printed on a resin film to form a diffuser.

The resin film PF is continuously supplied from the film supply roll to the screen printing apparatus. In the screen printing process, as described above, the diffuser precursor 23P is formed on the resin film PF by the uncrosslinked liquid rubber material blended with the foam material.

In a state where the diffuser precursor 23P is formed, the resin film PF is supplied to a foaming / crosslinking device, and the diffuser precursor 23P is foamed and crosslinked to become the diffuser 23.

Then, if the resin film PF on which the diffuser 23 is formed is punched into a frame shape, a frame 22 in which the diffuser 23 is integrally formed is obtained. When there is a distinction between the anode side frame and the cathode side frame in the frame, each frame is prepared individually.

The raw material of the polymer electrolyte membrane is cut to a predetermined size to prepare the polymer electrolyte membrane 21, and carbon felt or the like is cut to a predetermined size to prepare the electrodes 24 and 25. While forming the catalyst layer on the surface of the polymer electrolyte membrane 21, the electrodes 24 and 25 are integrated, and the polymer electrolyte membrane 21 is sandwiched between the frames 22 and 22, so that the frame, the polymer electrolyte membrane, and the electrode are integrated. A membrane electrode assembly (MEA) 2 is obtained. FIG. 8 shows an example in which the polymer electrolyte membrane 21 and the electrodes 24 and 25 are integrated and then integrated into the frame 22. The electrodes 24 and 25 may be integrated after the polymer electrolyte membrane 21 and the frame 22 are integrated. In addition, a well-known manufacturing method can be utilized about formation of a catalyst layer, and integration of a flame | frame and an electrode.

The effect of the diffuser 23 of the said embodiment is demonstrated. The diffuser 23 causes the reaction gas to flow along the planar pattern, thereby appropriately distributing the reaction gas. And the said diffuser 23 is comprised with foamed rubber, The hardness is 10-50 in Asker C, and is very flexible. Therefore, even if the diffuser 23 is sandwiched between the MEA frame 22 and the separators 5 and 6 and compressed, the reaction force is very small.

Therefore, due to the reaction force of the diffuser, the contact between the MEA electrodes (carbon felt) 24 and 25 and the separators 5 and 6 in the vicinity of the diffuser is prevented from becoming insufficient. The contact between the electrodes 24 and 25 and the polymer electrolyte membrane 21 can be ensured. As a result, power generation is performed in the entire power generation region of the fuel cell, and power generation efficiency is improved.

Further, a diffuser that satisfies 0.1 * Wm ≦ Hm ≦ 0.8 * Wm is formed, where Wm is the minimum width dimension of the planar pattern of the diffuser and Hm is the height dimension of the minimum width portion of the diffuser. Forming a diffuser in a pattern in which 20 to 200 dots per 1 square centimeter are scattered is also particularly effective in improving power generation efficiency. This is because the function of rectifying and distributing the flow of the diffuser reaction gas having a predetermined height while having such a fine planar pattern is high, and the reaction gas can be distributed to the entire power generation region. Such a diffuser can be efficiently manufactured by a manufacturing method using screen printing.

Further, as described in the method for manufacturing a membrane electrode assembly, in manufacturing such a diffuser, after forming a diffuser on a resin film to be a frame, the resin film is processed into a frame shape to form a frame. If the polymer electrolyte membrane is integrated into the frame, the diffuser formation process can be performed in a state where the resin film is continuous, and the screen printing process and the foaming / crosslinking process can be performed continuously. It can be a process. Such a continuous process does not require the labor of handling the members in the printing process, the crosslinking process, etc., and is particularly advantageous for increasing the production efficiency and mass production.

The present invention is not limited to the above embodiment, and can be implemented with various modifications. Other embodiments of the present invention will be described below. However, in the following description, portions different from the above embodiment will be mainly described, and detailed descriptions of the same portions will be omitted. Further, the embodiments described below can be implemented by combining some of them or replacing some of them.

The planar pattern of the diffuser formed on the frame is not limited to the form illustrated in FIG. 5, and may be another form. The interval between the rod-shaped elements and the dot-shaped elements can be appropriately adjusted so as to improve the distribution of the reaction gas. A diffuser having a planar pattern in which dot-like elements are dispersed is preferable because the distribution of the reaction gas can be easily adjusted by adding dots or changing the size of the dots. The size, shape, and spacing of the diffuser elements may be different depending on each part of the diffuser.

Further, the diffuser may have a laminated structure. For example, as a diffuser having a two-layer structure, the lower layer may be a foamed rubber layer having a predetermined hardness, and the upper layer may be an adhesive layer. When the upper layer is an adhesive layer, the adhesive layer adheres to the mating member when the fuel cell is assembled. Therefore, even if the foamed rubber layer is soft, the shape can be reliably maintained over a long period of time.

In addition, in the case of a diffuser having a laminated structure, if the lowermost layer is a non-foamed layer and the foamed layer is laminated thereon, it is prevented that the width of the element of the planar pattern of the diffuser is widened, This is effective in increasing the accuracy of the shape of the fine diffuser element.

In the description of the above embodiment, the case where the seal material is integrated with the separators 5 and 6 has been described, but the seal may be integrated with the MEA.

In the above embodiment, an example in which the diffuser forming process is performed prior to the frame forming process and the frame and polymer electrolyte membrane integrating process has been described. However, the order of these processes may be changed. Good. For example, the frame punching step may be preceded, followed by the diffuser forming step, and then proceeding to the polymer electrolyte membrane integration step. Alternatively, the diffuser molding step may be performed after the frame and the polymer electrolyte membrane are integrated.

Further, the field of use of the fuel cell is not limited to that for automobiles, and can be applied to other technical fields other than automobiles, such as household generators.

According to the diffuser of the fuel cell of the present invention, the power generation efficiency of the fuel cell can be increased, and the industrial utility value is high.

1 Fuel cell unit cell 2 Membrane electrode assembly (MEA)
21 Polymer electrolyte membrane 22 Frame 23 Diffuser 24 Cathode electrode 25 Anode electrode 5 Cathode electrode side separator 6 Anode electrode side separator 7, 8 Groove 9 Packing

Claims (3)

A diffuser provided between the reaction gas manifold and the power generation region to distribute the reaction gas supplied to the power generation region of the fuel cell,
The diffuser is mainly composed of foam rubber, and diffuser elements in the form of rods or dots are distributed in a plane pattern,
A diffuser for a fuel cell, wherein the foamed rubber has a hardness of 10 to 50 in Asker C. 2. The diffuser according to claim 1, wherein the diffuser plane pattern is formed to satisfy 0.1 * Wm ≦ Hm ≦ 0.8 * Wm, where Wm is the minimum width dimension of the planar pattern of the diffuser and Hm is the height dimension of the minimum width portion of the diffuser. Diffuser for fuel cells. The diffuser for a fuel cell according to claim 2, wherein the diffuser is formed in a planar pattern in which 20 to 200 dots are scattered per square centimeter.

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