JP6270791B2 - Gas diffusion layer for fuel cells - Google Patents

Description

  The present invention relates to a fuel cell gas diffusion layer laminated on a membrane electrode assembly and a method for forming the same.

  A fuel cell of a polymer electrolyte fuel cell includes a membrane electrode assembly (MEA) formed by forming a catalyst layer on both surfaces of an electrolyte membrane having hydrogen ion conductivity, and a catalyst layer of each membrane electrode assembly. It has a structure having a gas diffusion layer (gas diffusion layer for fuel cell) laminated thereon. Electricity is generated by supplying reaction gas (fuel gas, oxidant gas) to each gas diffusion layer.

  The catalyst layer is obtained by supporting platinum on carbon and further containing an electrolyte material (ionomer), and constitutes an electrode layer that generates a power generation reaction by the supplied reaction gas. The catalyst layer formed on one surface of the membrane electrode assembly (MEA) constitutes an anode (fuel electrode), and the catalyst layer formed on the other surface constitutes a cathode (air electrode).

  The gas diffusion layer is a layer formed in order to enhance the diffusibility of the reaction gas, and is disposed on each catalyst layer so that the reaction gas is uniformly supplied to the entire catalyst layer. . The gas diffusion layer also has a function for discharging generated water and humidified water from the catalyst layer and a function for efficiently taking out current from the catalyst layer. In recent years, for the purpose of further improving the functions of these gas diffusion layers, a conductive porous layer has been formed on the surface of the gas diffusion layer in contact with the catalyst layer.

  This conductive porous layer is made of a material having water repellency and conductivity, and is a porous layer in which countless fine holes are formed. Therefore, in addition to improving the drainage function of the generated water and humidified water, the function of extracting current from the catalyst layer is improved by increasing the contact area with the catalyst layer. The gas diffusion layer having such a conductive porous layer is, for example, a paste formed by mixing a conductive material and a water-repellent material on one surface of a diffusion layer substrate made of carbon paper or carbon cloth. It is created by applying a coating material in the form of a material and heating and baking it. The heated coating material becomes a conductive porous layer.

  In the fuel cell, the conductive porous layer of the gas diffusion layer is brought into contact with the respective catalyst layers of the membrane electrode assembly so that the membrane electrode assembly is sandwiched between the two gas diffusion layers. It is created by joining with a press or the like.

  Considering the adhesion between the conductive porous layer and the catalyst layer, it is desirable that the porosity of the conductive porous layer is small. On the other hand, considering the gas diffusibility of the conductive porous layer, the porosity of the conductive porous layer is preferably larger. In order to satisfy such mutually contradicting requirements, Patent Document 1 describes that the conductive porous layer has a two-layer structure, the porosity on the catalyst layer side is reduced, and the diffusion layer substrate side In this layer, a conductive porous layer having a large porosity is described. By setting it as such a structure, it becomes possible to improve the gas diffusion property of the whole electroconductive porous layer, improving the adhesiveness of an electroconductive porous layer and a catalyst layer.

JP 2009-016171 A

  By the way, since the carbon paper etc. used as a diffused layer base material are fibrous, many fuzz (carbon fiber) protrudes from the surface. It is known that such fluff may damage the electrolyte membrane of the membrane electrode assembly when the membrane electrode assembly is sandwiched between gas diffusion layers and hot pressed. When the fluff pierces the electrolyte membrane, a cross leak of the reaction gas occurs, and the power generation performance of the fuel cell is greatly reduced. Also, conduction between the anode and the cathode can occur.

  In particular, the conductive porous layer described in Patent Document 1 has a large porosity at the portion in contact with the diffusion layer substrate, so that the fluff easily enters from the diffusion layer substrate side. There is a high possibility of reaching the electrolyte membrane through the porous layer. As described above, in the conventional gas diffusion layer for a fuel cell, if it is intended to sufficiently improve the adhesion between the conductive porous layer and the catalyst layer and the gas diffusibility of the conductive porous layer, the durability against fluff is improved. It has the problem that property is impaired.

  This invention is made | formed in view of such a subject, The objective is making the adhesiveness of an electroconductive porous layer and a catalyst layer, and the gas diffusibility of an electroconductive porous layer sufficient. Another object of the present invention is to provide a fuel cell gas diffusion layer that does not impair durability against fluff, and a method for forming the same.

In order to solve the above problems, a gas diffusion layer for a fuel cell according to the present invention is formed by forming a conductive porous layer on one surface of a diffusion layer substrate formed into a sheet shape, A gas diffusion layer for a fuel cell, which is laminated on the membrane electrode assembly in a state where the porous layer is in contact with the catalyst layer of the membrane electrode assembly, wherein the conductive porous layer is the membrane electrode assembly. is formed so as to be distributed GaHitoshi one porosity along the stacking direction of the body, and the porous conductive member is the density GaHitoshi one along the stacking direction between the membrane electrode assembly, wherein A water repellent member dispersed and disposed throughout the interior of the conductive member, and exposing a proportion of the surface of the conductive member that is exposed without being covered with the water repellent member. When the rate is defined, the exposure rate on the catalyst layer side of the conductive porous layer is It is characterized by higher than the exposure rate in the diffusion layer base material side of the conductive porous layer.

  The fuel cell gas diffusion layer according to the present invention has a structure in which a conductive porous layer is formed on one surface of a diffusion layer base material formed in a sheet shape. And a porous conductive member, and a water-repellent member distributed throughout the interior of the conductive member. Specifically, the conductive member forms a porous aggregate, and a part of the surface of the aggregate is covered with the dispersed water-repellent members. With such a configuration, the conductive porous layer is a porous layer having conductivity and water repellency.

Conductive member, the stacking direction of the membrane electrode assembly, i.e., is formed such that the distribution GaHitoshi one porosity along the direction perpendicular to the surface of the diffusion layer substrate. For this reason, in the conductive porous layer, a layer in which larger voids are distributed than other layers is not formed, and the entire conductive porous layer is prevented from entering fuzz. The conductive member is formed to have a density GaHitoshi one along the stacking direction of the membrane electrode assembly.

On the other hand, the voids of the conductive porous layer need to be large enough to ensure sufficient gas diffusivity (gas permeability) of the conductive porous layer. As a result, in the case of a uniform one entire distribution of porosity as described above, the porosity of the catalyst layer side of a conventional (e.g., those described in the above patent document 1) becomes higher than For this reason, there is a concern that the adhesion between the catalyst layer and the conductive porous layer is lowered.

  Therefore, in the present invention, the state of the water-repellent member in the conductive porous layer is different between the diffusion layer base material side and the catalyst layer side, thereby ensuring the adhesion between the catalyst layer and the conductive porous layer. . That is, when the proportion of the surface of the conductive member that is exposed without being covered with the water repellent member is defined as the exposure rate, the exposure rate on the catalyst layer side of the conductive porous layer is It is higher than the exposure rate on the diffusion layer substrate side of the porous porous layer.

  According to the study by the present inventors, the catalyst layer and the conductive porous layer are formed by the affinity acting between the ionomer contained in the catalyst layer and the conductive member (for example, carbon) of the conductive porous layer. It has been found that they are bonded (adhered). In the present invention, the exposure rate is high on the catalyst layer side of the conductive porous layer, that is, in the vicinity of the surface opposite to the diffusion layer substrate, and the surface of the conductive member (the surface of the aggregate forming the porous material). ) Is exposed, the affinity is increased. As a result, the adhesion between the conductive porous layer and the catalyst layer is sufficiently improved.

  As described above, in the gas diffusion layer for a fuel cell according to the present invention, the adhesion between the conductive porous layer and the catalyst layer and the gas diffusibility of the conductive porous layer are sufficient, while preventing fuzz. Durability is also sufficiently secured.

The fuel cell gas diffusion layer according to the present invention is characterized in that the Young's modulus on the diffusion layer base material side of the conductive porous layer is higher than the Young's modulus on the catalyst layer side of the conductive porous layer. .

Thus, since the Young's modulus of the conductive porous layer is inclined in the thickness direction, the strain generated in the conductive porous layer when vibration is applied to the fuel cell is not uniform, and the diffusion layer The size is different on the substrate side and the opposite side. Specifically, when a vibration is applied to the fuel cell and a force in the shear direction is applied to the conductive porous layer, a small strain occurs in the direction on the diffusion layer substrate side having a large Young's modulus, and the Young's modulus is small. Large distortion occurs in the direction on the cathode electrode side. That is, in the conductive porous layer, the vicinity of the cathode electrode side is greatly mutated in the shearing direction than the vicinity of the diffusion layer base material side, and thus a force that bends against the fluff works. As a result, the fluff is cut inside the conductive porous layer, and the fluff is prevented from reaching the membrane electrode assembly. Thus, the cathode side gas diffusion layer has a function of cutting the fluff inside.

  According to the present invention, the fuel cell gas does not impair the durability against fluff while ensuring sufficient adhesion between the conductive porous layer and the catalyst layer and gas diffusibility of the conductive porous layer. A diffusion layer and a method for forming the diffusion layer can be provided.

It is sectional drawing of the fuel cell containing the gas diffusion layer for fuel cells which is one Embodiment of this invention. It is an exploded view for demonstrating the manufacturing method of the fuel battery cell shown in FIG. It is a figure for demonstrating typically a mode that a fluff is cut inside the gas diffusion layer for fuel cells.

  Hereinafter, embodiments of the present invention will be described with reference to the accompanying drawings. In order to facilitate the understanding of the description, the same constituent elements in the drawings will be denoted by the same reference numerals as much as possible, and redundant description will be omitted.

  FIG. 1 is a cross-sectional view of a fuel cell including a fuel cell gas diffusion layer according to an embodiment of the present invention. The fuel cell 1 is a so-called flat plate type polymer electrolyte fuel cell (PEFC), and is formed in a rectangular shape in plan view. As shown in FIG. 1, the fuel cell 1 includes a membrane electrode assembly 10, a pair of gas diffusion layers 20, and a pair of separators 30.

  The membrane electrode assembly 10 has a cathode electrode 12a and an anode electrode 12b on both surfaces of an electrolyte membrane 11 having hydrogen ion conductivity, respectively, and is so-called MEA. Both the cathode electrode 12a and the anode electrode 12b are formed on both surfaces of the electrolyte membrane 11 as catalyst layers (electrode layers) in which platinum particles are supported on carbon particles and an electrolyte (ionomer) is further contained. The cathode electrode 12a is a catalyst layer that reacts with an oxidant gas (for example, air), and the anode electrode 12b is a catalyst layer that reacts with a fuel gas (for example, hydrogen).

  The gas diffusion layer 20 is a layer for improving the diffusibility of the reaction gas, and is disposed so as to sandwich the membrane electrode assembly 10 from both sides. That is, the fuel cell 1 has two gas diffusion layers 20 including a cathode side gas diffusion layer 20a and an anode side gas diffusion layer 20b. A cathode side gas diffusion layer 20 a is laminated on the cathode electrode 12 a of the electrolyte membrane 11, and an anode side gas diffusion layer 20 b is laminated on the anode electrode 12 b of the electrolyte membrane 11.

  These two gas diffusion layers 20 are both conductive porous layers formed of a material having conductivity and water repellency on one surface of a diffusion layer substrate (22a, 22b) made of carbon paper. (21a, 21b). The gas diffusion layer 20 is arranged with the surface on the conductive porous layer (21a, 21b) side facing the membrane electrode assembly 10 side. Therefore, the conductive porous layer 21a is in contact with the cathode electrode 12a, and the conductive porous layer 21b is in contact with the anode electrode 12b. The gas diffusion layer 20 has a function of enhancing the diffusibility of the reaction gas, a function of discharging generated water and humidified water from the membrane electrode assembly 10 side, and an efficient flow of current from the cathode electrode 12a and the anode electrode 12b. It also has a function to take out. A specific configuration and manufacturing method of the gas diffusion layer 20 will be described in detail later.

  The separator 30 is a conductive layer disposed on the outermost side of the fuel cell 1 and is made of carbon. The separator 30 includes a cathode side separator 30a disposed adjacent to the cathode side gas diffusion layer 20a and an anode side separator 30b disposed adjacent to the anode side gas diffusion layer 20b. These are the same as each other. It has a shape.

  A plurality of grooves 31a having a rectangular cross section are formed in parallel with each other on the surface of the cathode side separator 30a in contact with the diffusion layer base material 22a. These grooves 31a are channels for sharing the oxidant gas from the outside with respect to the diffusion layer base material 22a. Similarly, a plurality of grooves 31b having a rectangular cross section are formed in parallel with each other on the surface of the anode separator 30b in contact with the diffusion layer base material 22b. These grooves 31b are flow paths for sharing the fuel gas from the outside with respect to the diffusion layer base material 22b.

  Although FIG. 1 shows only one fuel cell 1 (single cell), in an actual fuel cell device, a plurality of fuel cells 1 are stacked and electrically connected in series via a separator 30. (Cell stack). Although the power generation voltage of one fuel cell 1 is about 1V, a high voltage of several hundreds V can be output by connecting a plurality of fuel cells 1 in series as described above. As described above, the separator 30 has a role of electrically connecting the plurality of fuel cells 1 and a role of supplying a reaction gas to each fuel cell 1. Note that a refrigerant flow path for cooling the fuel cell 1 may be formed between the cathode side separator 30a and the anode side separator 30b adjacent to each other.

  A method of manufacturing the fuel cell 1 having the above-described configuration will be briefly described with reference to FIG. FIG. 2 is an exploded view for explaining a manufacturing method of the fuel battery cell 1. As shown in FIG. 2, first, the membrane electrode assembly 10 in which the cathode electrode 12a and the anode electrode 12b are formed on the electrolyte membrane 11, the cathode side gas diffusion layer 20a, and the anode side gas diffusion layer 20b are individually provided. Created on.

  Thereafter, the conductive porous layer 21a is brought into contact with the cathode electrode 12a of the membrane electrode assembly 10, and the conductive porous layer 21b is brought into contact with the anode electrode 12b of the membrane electrode assembly 10. To do. That is, the membrane electrode assembly 10 is sandwiched between the cathode side gas diffusion layer 20a and the anode side gas diffusion layer 20b from both sides.

  In this state, hot pressing is performed to join and integrate the cathode side gas diffusion layer 20a, the membrane electrode assembly 10, and the anode side gas diffusion layer 20b. Thereafter, this is sandwiched between the cathode side separator 30a and the anode side separator 30b. In the state of the fuel cell 1 alone, the separator 30 and the gas diffusion layer 20 are not particularly joined. These are fixed by holding the whole fuel cell 1 so as to be compressed along the stacking direction in a state where a plurality of fuel cells 1 are stacked to form a cell stack.

  Next, a specific manufacturing method of the cathode side gas diffusion layer 20a will be described. The anode-side gas diffusion layer 20b has substantially the same structure and manufacturing method as the cathode-side gas diffusion layer 20a, and will not be described.

  First, as a raw material for the conductive porous layer 21a, a paste-like coating material obtained by mixing a conductive material and a water repellent material is prepared (preparation step). In this example, carbon particles were used as the conductive material, and fibrous PTFE resin was used as the water repellent material. A solvent is added to these and mixed well to obtain a coating material in which the carbon particles and the PTFE resin are uniformly dispersed.

  Then, the diffusion layer base material 22a which is carbon paper is prepared, and the said coating material is apply | coated on the one surface (application | coating process). The coating material is coated so that the thickness after coating is uniform as a whole, and a layer to be fired is formed on the surface of the diffusion layer base material 22a. The layer to be fired is a layer that becomes the conductive porous layer 21a by being heated in a subsequent firing step.

  The fired layer formed in the coating process has a uniform thickness as described above, and the carbon particles and the PTFE resin are uniformly dispersed. That is, the density distributions of the carbon particles and the PTFE resin are uniform both in the direction along the surface of the layer to be fired and in the thickness direction.

  Thereafter, the diffusion layer base material 22a in which a layer to be fired is formed on one surface is placed in a heating furnace, and the whole is heated (firing step). The solvent of the layer to be fired (coating material) is removed by heating, and the carbon particles become a three-dimensional network structure aggregate to form a porous layer. The PTFE resin is in a state of being dispersed and arranged inside the porous layer, and each dispersed PTFE resin is in a state of covering a part of the aggregate (carbon).

  In the firing step, the whole is not heated at a uniform temperature, but is heated while maintaining a state in which there is a temperature difference on both sides of the layer to be fired. Specifically, the temperature of the portion of the layer to be fired that is in contact with the diffusion layer base material 22a is maintained higher than the temperature of the surface of the layer to be fired opposite to the diffusion layer base material 22a. Heat.

  In the present embodiment, the temperature of the portion of the layer to be fired that is in contact with the diffusion layer base material 22a is heated while maintaining a temperature higher than 327 ° C., which is the melting point of the PTFE resin. Moreover, it heated, maintaining the temperature of the surface on the opposite side to the diffused layer base material 22a among the to-be-fired layers in the state lower than 327 degreeC. For heating while maintaining such a temperature difference, for example, a heater is disposed only on one side of the layer to be fired (on the diffusion layer base material 22a side) in the heating furnace, or on the other side of the layer to be fired (diffusion layer) It can be performed by cooling the side opposite to the substrate 22a.

  The conductive porous layer 21a formed through the firing process as described above has substantially the same distribution of porosity. In other words, the density of carbon, which is a porous aggregate, is substantially uniform as a whole. Similarly, the density of the PTFE resin dispersed and arranged inside the conductive porous layer 21a is substantially uniform as a whole.

  On the other hand, the state of the PTFE resin in the conductive porous layer 21a differs between the diffusion layer base material 22a side and the opposite side (cathode electrode 12a side). That is, on the diffusion layer base material 22a side that is maintained at a relatively high temperature, the PTFE resin is melted and has a low viscosity. As a result, most of the carbon surface as an aggregate is covered with the PTFE resin. On the other hand, on the cathode electrode 12a side that is maintained at a relatively low temperature, the viscosity of the PTFE resin does not decrease so much, so the fluidity of the PTFE resin is low, and much of the surface of carbon as an aggregate is covered with the PTFE resin. Without being exposed.

  Here, the ratio of the surface exposed without being covered with the PTFE resin in the surface of the carbon as the aggregate is defined as the exposure rate. As described above, the exposure rate on the cathode electrode 12a side (the side opposite to the diffusion layer base material 22a) of the conductive porous layer 21a is the exposure rate on the diffusion layer base material 22a side of the conductive porous layer 21a. Higher than.

  The effect of varying the exposure rate on both surfaces of the conductive porous layer 21a as described above will be described. According to the study by the present inventors, the cathode electrode 12a and the conductive porous layer 21a act between the ionomer contained in the cathode electrode 12a and the carbon forming the aggregate of the conductive porous layer 21a. It has been found to bind (adhere) by affinity. In the present embodiment, the exposure rate is high on the cathode electrode 12a side of the conductive porous layer 21a, that is, in the vicinity of the surface opposite to the diffusion layer base material 22a, and a large amount of carbon (aggregate) surface is exposed. Therefore, the affinity is increased. As a result, the adhesion between the conductive porous layer 21a and the cathode electrode 12a is sufficiently improved.

  In the present embodiment, the porosity of the conductive porous layer 21a is uniform as a whole (at least in the thickness direction), and in particular, the porosity in the vicinity of the cathode electrode 12a is smaller than other portions. I don't mean. For this reason, in view of securing a certain (high) porosity in order to ensure gas diffusibility of the conductive porous layer 21a, the contact area between the cathode electrode 12a and the conductive porous layer 21a is It is in a smaller state than before. However, in this embodiment, the adhesion between the cathode electrode 12a and the conductive porous layer 21a is sufficiently secured by adjusting the exposure rate as described above.

  On the other hand, since the porosity of the conductive porous layer 21a is uniform as a whole (at least in the thickness direction), the porosity in the vicinity of the diffusion layer base material 22a is larger than other portions. I don't mean. For this reason, entry of fluff from the diffusion layer base material 22a, which is a carbon cloth, into the conductive porous layer 21a is suppressed.

  As described above, in the cathode-side gas diffusion layer 20a according to the present embodiment, the adhesion between the conductive porous layer 21a and the cathode electrode 12a and the gas diffusion property of the conductive porous layer 21a are sufficient. However, sufficient durability against fluff is secured.

  The cathode-side gas diffusion layer 20a according to the present embodiment suppresses the fluff from being cut and reaching the membrane electrode assembly 10 even if the fluff has entered the conductive porous layer 21a. It has a function to do. This will be described with reference to FIG. FIG. 3 is a diagram schematically illustrating how the fluff is cut inside the cathode-side gas diffusion layer 20a.

  As shown in FIG. 3A, the cathode-side gas diffusion layer 20a may be in a state where fluff 50 (carbon fiber) is stuck from the diffusion layer base material 22a. Such intrusion of the fluff 50 occurs not only when the fuel cell 1 is hot-pressed, but also when the fuel cell device equipped with the fuel cell 1 is used due to externally applied vibration. There is also. When the state where the fluff 50 is stuck from the diffusion layer base material 22a side (upper side in FIG. 3) continues as shown in FIG. 3 (A), the fluff 50 is directed to the membrane electrode assembly 10 side (lower side in FIG. 3). However, since there is a possibility that the membrane electrode assembly 10 may be damaged, it is not preferable.

  As already described, the cathode-side gas diffusion layer 20a according to the present embodiment is heated while maintaining a temperature difference state in the firing step. As a result, the Young's modulus is relatively large on the diffusion layer base material 22 side (the upper side in FIG. 3) that has been maintained at a high temperature in the conductive porous layer 21a. On the other hand, the Young's modulus is relatively small on the cathode electrode 12a side (the lower side in FIG. 3) maintained at a low temperature in the conductive porous layer 21a.

  As described above, since the Young's modulus of the conductive porous layer 21a is inclined in the thickness direction, the strain generated in the conductive porous layer 21a when vibration is applied to the fuel cell 1 is not uniform. The diffusion layer substrate 22a side and the opposite side have different sizes. Specifically, when vibration is applied to the fuel cell 1 and shearing force (forces indicated by arrows AR1 and AR2 in FIG. 3) is applied to the conductive porous layer 21a, the Young's modulus A small strain occurs in the direction on the large diffusion layer base material 22a side, and a large strain occurs in the direction on the cathode electrode 12a side with a small Young's modulus. That is, the conductive porous layer 21a is sheared in the direction closer to the cathode electrode 12a (lower side in FIG. 3) than in the vicinity of the diffusion layer base material 22a (upper side in FIG. 3). Direction), and a force that bends the fluff 50 acts. As a result, as shown in FIG. 3B, the fluff 50 is cut inside the conductive porous layer 21a, and the fluff 50 is suppressed from reaching the membrane electrode assembly 10. Thus, the cathode side gas diffusion layer 20a according to the present embodiment has a function of cutting the fluff 50 inside.

  The cathode-side gas diffusion layer 20a according to the present embodiment maintains a state in which a temperature difference is provided in the firing process, so that the exposure rate in the conductive porous layer 21a is different between the diffusion layer base material 22a side and the opposite side. It is different. The method for varying the exposure rate along the thickness direction is not limited to the above method, and various methods can be employed.

For example , the cathode-side gas diffusion layer 20a is prepared by preparing a plurality of baked conductive porous layers 21a having different exposure rates and hot-pressing them in a state where they are arranged on top of the diffusion layer substrate 22. May be formed.

  The embodiments of the present invention have been described above with reference to specific examples. However, the present invention is not limited to these specific examples. In other words, those specific examples that have been appropriately modified by those skilled in the art are also included in the scope of the present invention as long as they have the characteristics of the present invention. For example, the elements included in each of the specific examples described above and their arrangement, materials, conditions, shapes, sizes, and the like are not limited to those illustrated, but can be changed as appropriate. Moreover, each element with which each embodiment mentioned above is provided can be combined as long as technically possible, and the combination of these is also included in the scope of the present invention as long as it includes the features of the present invention.

1: Fuel cell 10: Membrane electrode assembly 11: Electrolyte membrane 12a: Cathode electrode 12b: Anode electrode 20: Gas diffusion layer 20a: Cathode side gas diffusion layer 20b: Anode side gas diffusion layer 21a, 21b: Conductive porous Layer 22, 22a, 22b: Diffusion layer base material 30: Separator 30a: Cathode side separator 30b: Anode side separator 31a, 31b: Groove 50: Fluff

Claims (2)

A state in which a single-layer conductive porous layer is formed on one surface of a diffusion layer substrate formed in a sheet shape, and the conductive porous layer is in contact with the catalyst layer of the membrane electrode assembly A fuel cell gas diffusion layer laminated on the membrane electrode assembly,
The conductive porous layer is
A porous conductive member formed so that the porosity distribution along the stacking direction with the membrane electrode assembly is uniform, and the density along the stacking direction with the membrane electrode assembly is uniform; ,
A water repellent member dispersed and disposed throughout the interior of the conductive member,
When the ratio of the surface of the conductive member that is exposed without being covered with the water repellent member is defined as the exposure rate,
The fuel cell gas diffusion layer characterized in that the exposure rate on the catalyst layer side of the conductive porous layer is higher than the exposure rate on the diffusion layer base material side of the conductive porous layer. . Young's modulus at the diffusion layer base material side of the conductive porous layer, the fuel cell according to claim 1, wherein the higher than the Young's modulus in the catalyst layer side of the conductive porous layer Gas diffusion layer.

Images