JP2006344428A - Solid polymer fuel cell - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a solid polymer fuel cell capable of maintaining high power generation property for a long period. <P>SOLUTION: The solid polymer fuel cell (150) composed of a catalyst layer (120a, 120c) formed by laminating a catalyst layer (1) (121a, 121c) free from cracks and a catalyst layer (2) (122a, 122c) having cracks (123a, 123c). Average diameter of catalyst particles contained in the catalyst layer (120a, 120c) becomes larger, and crystallinity of carbon carrier contained in the catalyst becomes higher as it is headed from inlet side to outlet side of a gas flow passage (141) of separators (140a, 140c). <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

  The present invention relates to a polymer electrolyte fuel cell, and more particularly to a technique for improving a catalyst layer of a polymer electrolyte fuel cell.

  In recent years, fuel cells have attracted attention as one of power sources. A fuel cell refers to a device that generates electricity by oxidizing a fuel such as hydrogen or methanol. The power generation efficiency of fuel cells is very high. Moreover, the discharge from the fuel cell using hydrogen as a fuel is water, which is a very useful power source from the viewpoint of protecting the global environment.

  Various fuel cells such as a polymer electrolyte fuel cell, a solid oxide fuel cell, a molten carbonate fuel cell, and a phosphoric acid fuel cell have been proposed as fuel cells. Among these, the polymer electrolyte fuel cell can be operated at a relatively low temperature, and is expected to be used as a power source for moving bodies such as automobiles, and is being developed.

  The polymer electrolyte fuel cell is also called a polymer electrolyte fuel cell or PEFC, and is a fuel cell using a proton conductive solid polymer electrolyte. The PEFC has a membrane electrode assembly in which a pair of catalyst layers including an electrode catalyst for promoting a power generation reaction, that is, an oxygen electrode catalyst layer and a fuel electrode catalyst layer, are formed on both sides of a proton conductive solid polymer electrolyte membrane. . Further, a gas diffusion layer and a separator are disposed outside the catalyst layer. A gas flow path through which gas flows is formed on the catalyst layer side surface of the separator, and the gas used for the power generation reaction diffuses through the gas flow path and the gas diffusion layer and is supplied to the catalyst layer. Moreover, the water produced | generated with the electric power generation reaction is discharged | emitted outside PEFC through a gas diffusion layer, a gas flow path, etc.

  The catalyst layer contains a proton conductive solid polymer electrolyte in addition to the electrode catalyst in which catalyst particles are supported on a carbon support. The conventional catalyst layer has a porous structure in which a solid polymer electrolyte serves as a binder and pores are formed by an aggregate of electrode catalysts.

In such a PEFC, the following power generation reaction proceeds. First, hydrogen contained in the fuel gas supplied to the fuel electrode side is oxidized by the catalyst particles to become protons and electrons (2H ₂ → 4H ⁺ + 4e ⁻ ). Next, the generated protons pass through the solid polymer electrolyte contained in the fuel electrode catalyst layer and the polymer electrolyte membrane in contact with the fuel electrode catalyst layer, and reach the oxygen electrode catalyst layer. In addition, the electrons generated in the fuel electrode catalyst layer are the carbon carrier constituting the fuel electrode catalyst layer, the gas diffusion layer in contact with the polymer electrolyte membrane of the fuel electrode catalyst layer, the separator, and the external circuit. To reach the oxygen electrode catalyst layer. The protons and electrons that have reached the oxygen electrode catalyst layer react with oxygen contained in the oxidant gas supplied to the oxygen electrode side to generate water (O ₂ + 4H ⁺ + 4e ⁻ → 2H ₂ O). In the fuel cell, electricity can be taken out through the power generation reaction described above.

  The power generation reaction occurs at a three-phase interface where the catalyst particles, the solid polymer electrolyte, and the supplied gas are in contact. Therefore, in order to obtain a fuel cell in which the amount of formation of the three-phase interface is high and a high output voltage can be obtained, it is common to produce a porous structure as dense as possible in the catalyst layer to sufficiently diffuse the reaction gas. It is. However, the catalyst layer having a dense porous structure has a problem that the gas diffusibility in the thickness direction is lowered.

As a technique for solving this problem, a technique has been proposed in which a crack for intentionally improving gas diffusibility is provided in the catalyst layer surface to secure a reaction gas flow path (see Patent Document 1). .
Japanese Patent Laid-Open No. 2002-270187

  In PEFC, the life of the battery is a problem as well as the cost. The battery life is said to be 5000 hours for automobiles and 40,000 hours for home use, and it is required to maintain high power generation performance over a long period of time.

  However, in the PEFC described in Patent Document 1, the contact between the carbon supports is cut off by the crack formed in the catalyst layer, the electron transfer path is reduced, and the electron transfer resistance of the catalyst layer is increased. Therefore, it has been difficult to sufficiently improve the output voltage of PEFC.

Further, the conventional PEFC such as Patent Document 1 has a problem that the porous structure of the catalyst layer is destroyed due to corrosion of the carbon support due to repeated start and stop. Corrosion of the carbon support is caused by an electrochemical oxidation reaction (C + 2H ₂ O → CO ₂ + 4H ⁺ + 4e ⁻ ) that generates carbon dioxide using water present in the catalyst layer as an oxidizing agent. When the porous structure is destroyed due to corrosion of the carbon support, the gas diffusibility and drainage of the catalyst layer are lowered, the concentration overvoltage is increased, and the battery characteristics tend to be lowered.

  Furthermore, when the cell voltage is exposed to a high potential environment during startup, shutdown, storage, etc., there is a problem that the catalyst particles contained in the catalyst layer are dissolved and eluted and the performance of the PEFC deteriorates. It was. In particular, in battery operation with a duty cycle, the cathode potential changes greatly, so that the catalyst particles contained in the oxygen electrode catalyst layer are significantly dissolved and eluted, and the catalyst activity decreases with time, resulting in the output voltage of the PEFC. Is a cause of deterioration.

  As described above, in the conventional PEFC, sufficient durability cannot be obtained due to corrosion of the carbon support, dissolution and elution of the catalyst particles, and it has been difficult to maintain high power generation performance over a long period of time.

  Accordingly, an object of the present invention is to provide a polymer electrolyte fuel cell capable of maintaining high power generation performance over a long period of time.

  The present invention solves the above problems by the following polymer electrolyte fuel cells (1) and (2).

(1) A membrane electrode assembly in which a pair of catalyst layers is disposed on both sides of a solid polymer electrolyte membrane is sandwiched by a separator having a gas flow path,
The catalyst layer is a solid polymer fuel cell including at least an electrode catalyst having catalyst particles supported on a carbon support and a solid polymer electrolyte,
At least one of the catalyst layers includes a catalyst layer (1) that is in contact with the solid polymer electrolyte membrane and does not have cracks, and a catalyst layer (2) that has cracks is the thickness of the membrane electrode assembly. Laminated in the direction,
At least one of the catalyst layer (1) and the catalyst layer (2) has an average particle diameter of the catalyst particles that increases from the inlet side to the outlet side of the gas flow path, and A polymer electrolyte fuel cell in which crystallinity increases from an inlet side to an outlet side of the gas flow path.

(2) A membrane / electrode assembly in which a pair of catalyst layers are disposed on both sides of a solid polymer electrolyte membrane is sandwiched by a separator having a gas flow path,
The catalyst layer includes at least an electrode catalyst in which catalyst particles are supported on a carbon support, and a solid polymer electrolyte,
The catalyst particles are solid polymer fuel cells containing platinum particles and platinum alloy particles,
At least one of the catalyst layers includes a catalyst layer (1) that is in contact with the solid polymer electrolyte membrane and does not have cracks, and a catalyst layer (2) that has cracks is the thickness of the membrane electrode assembly. Laminated in the direction,
At least one of the catalyst layer (1) and the catalyst layer (2) has a higher content of the platinum alloy particles from the inlet side to the outlet side of the gas flow path, and A polymer electrolyte fuel cell in which crystallinity increases from an inlet side to an outlet side of the gas flow path.

  In the polymer electrolyte fuel cell of the present invention, the reaction gas is efficiently supplied to the catalyst contained in the catalyst layer. Further, the increase in the electron transfer resistance of the catalyst layer due to the means for efficiently supplying the reaction gas is suppressed to the minimum. Furthermore, corrosion of the carbon support and elution of the catalyst particles in the catalyst layer are efficiently suppressed.

  First, a first polymer electrolyte fuel cell (also simply referred to as “PEFC”) of the present invention will be described with reference to FIG. FIG. 1 is a schematic cross-sectional view of a polymer electrolyte fuel cell 150 of the present invention.

  A polymer electrolyte membrane 110 is disposed in the center of the membrane electrode assembly 100. A catalyst layer 120a is disposed on the fuel electrode side of the solid polymer electrolyte membrane 110, and the catalyst layer 120a is disposed on the solid polymer electrolyte membrane 110 side and has a crack-free catalyst layer (1) 121a, a separator The catalyst layer (2) 122a in which the crack 123a was formed arrange | positioned at the 140a side. On the other hand, the catalyst layer 120c is also arranged on the oxygen electrode side of the polymer electrolyte membrane 110. Like the fuel electrode side, the catalyst layer 120c is arranged on the polymer electrolyte membrane 110 side, and no crack is formed. It consists of a catalyst layer (1) 121c and a catalyst layer (2) 122c disposed on the separator 140c side and having a crack 123c.

  The polymer electrolyte fuel cell 150 has a structure in which both sides of the membrane electrode assembly 100 are further sandwiched between two separators 140a and 140c. Separator 140a, 140c has gas channel 141 for supplying gas supplied from the outside, such as fuel gas containing hydrogen or oxidant gas containing oxygen, to catalyst layers 120a, 120c.

  In the present application, the “membrane electrode assembly” means a laminate having at least a solid polymer electrolyte membrane and a pair of catalyst layers sandwiching the solid polymer electrolyte membrane.

  In the polymer electrolyte fuel cell of the present invention, at least one catalyst layer is formed by laminating the catalyst layer (1) and the catalyst layer (2) in the direction in which the constituent elements of the membrane electrode assembly are laminated, that is, in the thickness direction. It consists of two or more layers.

  In the catalyst layer composed of the catalyst layer (1) and the catalyst layer (2), the layer disposed on the separator side is defined as the catalyst layer (2), and the catalyst layer (2) has cracks for promoting the gas supply. Have. On the other hand, a layer disposed on the polymer electrolyte membrane side is defined as a catalyst layer (1), and this catalyst layer (1) does not have a crack for promoting gas supply.

  Thus, at least one catalyst layer on the fuel electrode side or oxygen electrode side has a laminated structure including two or more layers including the catalyst layer (1) and the catalyst layer (2), and the catalyst layer disposed on the separator side. (2) is provided with a crack. Due to the crack, the diffusibility of the gas supplied through the gas flow path provided in the separator is improved, and the gas is efficiently supplied to the catalyst particles arranged in the catalyst layer. Moreover, the water produced | generated by the battery reaction in a catalyst layer can be efficiently excluded by the crack to the separator side.

  On the other hand, cracks for promoting gas supply are not formed in the catalyst layer (1) in contact with the polymer electrolyte membrane 110. Due to the presence of the catalyst layer having no crack, an electron transfer path is secured, and an increase in the electron transfer resistance of the catalyst layer is suppressed to a minimum.

  Thus, the catalyst layer has a laminated structure composed of two or more layers, and the catalyst layer (2) disposed on the separator side improves the gas diffusion and generated water discharge function, and is disposed on the polymer electrolyte membrane side. By ensuring the electronic electric function by the catalyst layer (1), the reaction gas is efficiently supplied to the catalyst particles contained in the catalyst layer, and the increase in the electron transfer resistance of the catalyst layer is minimized. .

  In the catalyst layer of the present invention, a laminated structure composed of two or more layers including the catalyst layer (1) and the catalyst layer (2) is used, and the average particle size of the catalyst particles for promoting the electrode reaction is set to the catalyst layer (1 And at least one of the catalyst layers (2) is configured to increase from the inlet side to the outlet side of the gas flow path of the separator.

  The moisture generated by the electrode reaction and the moisture contained in the gas supplied through the gas flow path provided in the separator are likely to stay in the catalyst layer, and in the catalyst layer from the inlet side to the outlet side of the gas flow path. The amount of water to be retained increases. The dissolution of the catalyst particles is likely to occur at a location with a lot of moisture, and hardly occurs at a location where it is dry. For this reason, the dissolution of the catalyst particles that causes a decrease in the durability of the fuel cell tends to occur remarkably as it goes from the inlet side to the outlet side of the gas flow path. Even if there is little dissolution of the catalyst particles on the inlet side of the gas flow path in the catalyst layer, the power generation performance of the entire battery tends to decrease due to the large dissolution of the catalyst particles on the outlet side.

  In addition, catalyst particles having a small particle size have a large specific surface area and high catalytic activity, whereas catalyst particles having a large particle size are excellent in dissolution resistance. In the catalyst layer, high catalyst activity is maintained by disposing catalyst particles with small particle diameters in areas where catalyst particles are unlikely to dissolve and disposing catalyst particles with large particle diameters in areas where catalyst particles are likely to dissolve. However, catalyst particles having a large particle diameter in the catalyst layer can be efficiently suppressed.

  The catalyst layer of the present invention has a laminated structure composed of two or more layers including the catalyst layer (1) and the catalyst layer (2), and in addition to the average particle diameter of the catalyst particles, carbon used as a carrier for the catalyst particles. The crystallinity of the carrier is increased from the inlet side to the outlet side of the gas flow path of the separator.

  As described above, the moisture generated by the electrode reaction and the moisture contained in the gas supplied through the gas flow path provided in the separator are the water that stays from the inlet side to the outlet side of the gas flow path in the catalyst layer. The amount increases. The corrosion of the carbon support proceeds using water as an oxidizing agent. For this reason, the corrosion of the carbon carrier, which causes a decrease in the durability of the fuel cell, tends to occur remarkably as it goes from the inlet side to the outlet side of the gas flow path. Even if there is little corrosion of the carbon support on the inlet side of the gas flow path in the electrode catalyst layer, there is a tendency for the power generation performance of the entire battery to decrease due to the large corrosion of the carbon support on the outlet side.

  In addition, a carbon support having low crystallinity has a large specific surface area and can carry catalyst particles in a highly dispersed manner, whereas a carbon support having high crystallinity is excellent in corrosion resistance. In the catalyst layer, high catalytic activity is maintained by disposing a carbon support with low crystallinity at a site where corrosion of the carbon support is unlikely to occur, and a carbon support with high crystallinity at a site where corrosion of the carbon support is likely to occur. However, corrosion of the carbon support in the catalyst layer can be efficiently suppressed.

  As described above, in the first polymer electrolyte fuel cell of the present invention, the catalyst layer has a laminated structure composed of two or more layers, and the catalyst particles (1) and / or (2) have a particle size of catalyst particles. While increasing in the catalyst layer in a predetermined direction and increasing the crystallinity of the carbon support in a predetermined direction, in the catalyst layer, as well as ensuring electron conductivity and catalytic activity and improving gas diffusivity, Corrosion of the carbon carrier that occurs due to repeated start and stop cycles of the fuel cell, and elution of catalyst particles that occur when the cell voltage reaches a noble potential (approximately 0.8 V or more) during the start and stop cycle of the fuel cell Can be suppressed. Therefore, according to the present invention, it is possible to provide a polymer electrolyte fuel cell capable of maintaining high power generation performance over a long period of time.

  Then, the structure which the catalyst layer in 1st PEFC of this invention has is demonstrated.

  A catalyst layer is a site | part by which the catalyst particle which mediates an electrode reaction is arrange | positioned. The catalyst layer generally includes an electrode catalyst in which catalyst particles are supported on a carbon support, and a proton conductive solid polymer electrolyte.

  In the present invention, the catalyst layer disposed on at least one of the fuel electrode side and the oxygen electrode side is formed by laminating at least two layers of the catalyst layer (1) and the catalyst layer (2). In the catalyst layer composed of at least two layers, the catalyst layer (2) having cracks is disposed on the separator side, and the catalyst layer (1) having no cracks is disposed on the polymer electrolyte membrane side.

  Three or more layers of the catalyst layer may be laminated. At this time, the catalyst layer (2) is disposed on the outermost layer on the separator side, and the catalyst layer (1) is disposed on the solid polymer electrolyte membrane side. Other layers such as the catalyst layer (3) may be further disposed between the catalyst layer (1) and the catalyst layer (2). Examples of the catalyst layer (3) include those having a configuration such as a catalyst layer having a porosity between the porosity of the catalyst layer (1) and the porosity of the catalyst layer (2).

  Conventionally, a general PEFC catalyst layer has pores which are formed by gaps between electrode catalysts and have a diameter of about several nanometers to several hundred nanometers. With respect to this hole, the “crack” in the present invention means a crack having a predetermined size as shown in FIG. Therefore, the catalyst layer (1) has pores formed between the electrode catalysts and the catalyst layer (2) has cracks in addition to the pores. Since cracks are present in the catalyst layer in this way, it is possible to promote efficient diffusion of the supplied gas both in the surface direction of the catalyst layer and in the stacking direction.

  The shape and size of the crack are not particularly limited as long as the supply of fuel gas or oxidant gas is promoted. The diameter of the crack is preferably several tens of nm to several tens of μm, more preferably several hundreds of nm to several tens of μm. In addition, the diameter of a crack means the diameter of the space | gap part which a crack has. The diameter of the crack can be measured by observation with a microscope or the like.

  The porosity of the catalyst layer (2) is preferably 1.5 to 3.0 times, more preferably 2.0 to 3.0 times the porosity of the catalyst layer (1). Good. Thereby, the gas diffusibility of a catalyst layer, drainage, and electric power generation performance can be improved more.

  The porosity of the catalyst layer (1) is not particularly limited, but is preferably 10 to 60%, more preferably 20 to 50% from the viewpoint of ensuring electronic conductivity.

  The porosity of the catalyst layer (2) is not particularly limited, but is preferably 30 to 80%, and more preferably 50 to 50% in order to effectively promote gas supply and not greatly reduce the utilization rate of the catalyst. It is preferable to have a porosity of about 80%.

  The porosity of the catalyst layers (1) and (2) can be measured by measuring from an SEM photograph and using a mercury porosimeter.

  In the present invention, the average particle diameter of the catalyst particles is further increased from the gas inlet side to the outlet side of the gas supply path of the separator in at least one of the catalyst layer (1) and the catalyst layer (2). However, it is preferable to further increase the average particle diameter of the catalyst particles contained in the catalyst layer from the separator side of the catalyst layer having the catalyst layers (1) and (2) toward the solid polymer electrolyte membrane side. As a result, catalyst particles having high dissolution resistance can be disposed in the catalyst layer where the catalyst particles are likely to be dissolved, and the durability of the PEFC can be further improved.

  In order to increase the average particle size of the catalyst particles contained in the catalyst layer from the separator side of the catalyst layer toward the solid polymer electrolyte membrane side, more preferably, the average particle size of the catalyst particles contained in the catalyst layer (1) Is preferably larger than the average particle diameter of the catalyst particles contained in the catalyst layer (2). Thereby, the average particle diameter of the catalyst particles in the catalyst layer can be easily adjusted. Further, when there are three or more catalyst layers due to the presence of another catalyst layer (3) between the catalyst layer (1) and the catalyst layer (2), the catalyst layer The average particle diameter of the catalyst particles contained in the catalyst layer (3) may be adjusted so that the average particle diameter of the catalyst particles increases from (2) toward the catalyst layer (1).

  The average particle diameter of the catalyst particles may increase stepwise from the inlet side to the outlet side of the gas flow path of the catalyst layer, more preferably from the separator side to the solid polymer electrolyte membrane side. You may increase gradually. Among these, since the production of the catalyst layer and the control of the average particle diameter of the catalyst particles in the catalyst layer are easy, the average particle diameter of the catalyst particles is preferably increased stepwise.

  The catalyst particles having a predetermined average particle diameter are respectively arranged so that the particle diameter increases in a predetermined direction in the catalyst layer (1) and / or the catalyst layer (2). In the catalyst layer (1) and / or the catalyst layer (2), the range in which the catalyst particles having the respective average particle diameters are included in the catalyst layer may be appropriately determined in consideration of the durability and power generation performance of the obtained PEFC. Good.

  As a preferred embodiment, for example, there is a configuration shown in FIG. 2 in which the catalyst layer is divided into two or more regions in the surface direction of the membrane electrode assembly. FIG. 2 is a schematic diagram of the catalyst layer 120, and the catalyst layer (1) is divided into two regions, that is, the inlet side catalyst layer (1-1) 121 i and toward the surface direction (arrow A) of the membrane electrode assembly. In the same manner, the catalyst layer (2) is also divided into the inlet catalyst layer (2-1) 122i and the outlet catalyst layer (2-2) 122e. Catalyst particles having a predetermined average particle diameter are divided into an inlet-side catalyst layer (1-1) 121i, an outlet-side catalyst layer (1-2) 121e, an inlet-side catalyst layer (2-1) 122i, and an outlet-side catalyst layer ( 2-2) It may be included in 122e. When the catalyst layer is incorporated into the polymer electrolyte fuel cell, the inlet side catalyst layers (1-1, 2-1) are arranged so as to be close to the gas flow path inlet side of the separator, and the outlet side catalyst layer What is necessary is just to arrange | position so that (1-2,2-2) may adjoin to the gas flow path exit side of a separator.

  When the catalyst layer (1) is composed of at least two layers of the inlet side catalyst layer (1-1) and the outlet side catalyst layer (1-2), the difference in the average particle diameter of the catalyst particles from the adjacent layer is preferably Is 0.1 to 3.0 nm, more preferably 0.1 to 2.0 nm.

  Further, when the catalyst layer (2) is composed of at least two layers of the inlet side catalyst layer (2-1) and the outlet side catalyst layer (2-2), the difference in the average particle diameter of the catalyst particles from the adjacent layers is The thickness is preferably 0.1 to 3.0 nm, more preferably 0.1 to 2.0 nm.

  As the average particle diameter of the catalyst particles in each layer, specifically, the average particle diameter of the catalyst particles contained in the inlet catalyst layer (2-1) is preferably 2 to 4 nm, more preferably 2 to 3 nm. The average particle diameter of the catalyst particles contained in the outlet side catalyst layer (2-2) is preferably 2.5 to 5 nm, more preferably 2.5 to 4 nm.

  The average particle diameter of the catalyst particles contained in the inlet side catalyst layer (1-1) is preferably 2.5 to 5 nm, more preferably 2.5 to 4 nm, and the outlet side catalyst layer (1- The average particle diameter of the catalyst particles contained in 2) is preferably 4 to 6 nm, more preferably 4 to 5 nm. At this time, the average particle diameter of the catalyst particles is larger in the outlet catalyst layer (1-2) than in the inlet catalyst layer (1-1), and is larger than that in the inlet catalyst layer (2-1). Also, the inlet side catalyst layer (1-1) is larger, the inlet side catalyst layer (2-2) is larger than the inlet side catalyst layer (2-1), and the outlet side catalyst layer (2) is larger. The outlet side catalyst layer (1-2) is preferably larger than -2).

  The average particle diameter of the catalyst particles in the catalyst layer can be measured by measurement from a TEM photograph of the catalyst-supporting carbon and XRD measurement.

  The range of the inlet side catalyst layer (1-1) and the outlet side catalyst layer (1-2) in the catalyst layer (1), the inlet side catalyst layer (2-1) and the outlet side catalyst layer ( The range 2-2) may be determined in consideration of the durability of the obtained polymer electrolyte fuel cell.

  The inlet catalyst layer (2-1) is preferably 30 to 60% by volume, more preferably 40 to 50% by volume, based on the entire catalyst layer (2).

  The inlet catalyst layer (1-1) is preferably 30 to 60% by volume, more preferably 40 to 50% by volume, based on the entire catalyst layer (1).

  In the above description, the catalyst layers (1) and (2) are divided into two regions in the flow direction of the gas flow path. Further, the catalyst layers (1) and / or Alternatively, (2) may be divided into three or more regions. In this case, another layer may be disposed between the inlet side catalyst layer (1-1, 2-1) and the outlet side catalyst layer (1-2, 2-2). The average particle diameter of the catalyst particles may be increased from 1, 2) toward the outlet catalyst layer (1-2, 2-2).

  In the present invention, the crystallinity of the carbon support is further increased from at least one of the catalyst layer (1) and the catalyst layer (2) from the gas inlet side to the outlet side of the gas supply path of the separator. .

  In the present invention, the crystallinity of the carbon support contained in the catalyst layer (1) and / or (2) is increased from the gas inlet side to the outlet side in the gas supply path of the separator of the catalyst layer. It is preferable to increase the crystallinity of the carbon carrier contained in the catalyst layer from the separator side of the catalyst layer having the catalyst layers (1) and (2) toward the solid polymer electrolyte membrane side. Thereby, a carbon support with high corrosion resistance can be arranged on the solid polymer electrolyte membrane side where the carbon support of the catalyst layer is likely to corrode, and the durability of PEFC can be further improved.

  In order to increase the crystallinity of the carbon carrier contained in the catalyst layer from the separator side to the solid polymer electrolyte membrane side of the catalyst layer, more preferably, the crystallinity of the carbon carrier contained in the catalyst layer (1) is increased as a catalyst. The crystallinity of the carbon support contained in the layer (2) is preferably higher. Thereby, the crystallinity of the carbon support in the catalyst layer can be easily adjusted. Further, when there are three or more catalyst layers due to the presence of another catalyst layer (3) between the catalyst layer (1) and the catalyst layer (2), the catalyst layer The crystallinity of the carbon support contained in the catalyst layer (3) may be adjusted so that the crystallinity of the carbon support increases from (2) toward the catalyst layer (1).

  The crystallinity of the carbon support can be easily adjusted by graphitization of the carbon support.

  The graphitization of the carbon carrier is not particularly limited as long as it is conventionally used, such as heat treatment. The heat treatment is preferably performed in an inert gas atmosphere such as nitrogen, argon, or helium. Moreover, although heat processing temperature and heat processing time change with materials of the carbon support | carrier to be used, what is necessary is just to carry out at 2,000-3,000 degreeC for about 5 to 20 hours.

  As described above, the graphitization and the like improve the crystallinity of the carbon support and reduce the specific surface area of the carbon support, and the specific surface area of the carbon support is an indicator of the crystallinity of the carbon support. That is, as a preferred form of the catalyst layer of the present invention, the specific surface area of the carbon support in the catalyst layer is from the inlet side to the outlet side of the gas flow path, and from the separator side to the solid polymer electrolyte membrane side. It becomes the form which becomes small toward.

  At this time, the specific surface area of the carbon support gradually decreases from the inlet side to the outlet side of the gas flow path of the catalyst layer, more preferably from the separator side to the solid polymer electrolyte membrane side. Or may be gradually reduced. In particular, the specific surface area of the carbon support should be reduced stepwise because the production of the catalyst layer and the control of the crystallinity of the carbon support in the catalyst layer are easy.

  The carbon carriers having a predetermined specific surface area are arranged so that the crystallinity increases in a predetermined direction in the catalyst layer (1) and / or the catalyst layer (2). In the catalyst layer (1) and / or the catalyst layer (2), the range in which each carbon carrier is included in the catalyst layer may be appropriately determined in consideration of the durability, power generation performance, etc. of the obtained PEFC.

  As a preferred embodiment, for example, the configuration shown in FIG. 2 described above in which the catalyst layer is divided into two or more regions in the surface direction of the membrane electrode assembly can be mentioned. FIG. 2 is a schematic diagram of the catalyst layer 120, and the catalyst layer (1) is divided into two regions, that is, the inlet side catalyst layer (1-1) 121 i and toward the surface direction (arrow A) of the membrane electrode assembly. In the same manner, the catalyst layer (2) is also divided into the inlet catalyst layer (2-1) 122i and the outlet catalyst layer (2-2) 122e. The carbon support having each specific surface area described above is divided into an inlet side catalyst layer (1-1) 121i, an outlet side catalyst layer (1-2) 121e, an inlet side catalyst layer (2-1) 122i, and an outlet side catalyst layer ( 2-2) It may be included in 122e.

When the catalyst layer (1) is composed of at least two layers of an inlet side catalyst layer (1-1) and an outlet side catalyst layer (1-2), the difference in specific surface area of the carbon support with the adjacent layer is preferably It is good to set it as 130-700 m < ² > / g, More preferably, it is 70-200 m < ² > / g.

Further, when the catalyst layer (2) is composed of at least two layers of an inlet side catalyst layer (2-1) and an outlet side catalyst layer (2-2), the difference in specific surface area of the carbon support with the adjacent layer is as follows: preferably 200~800m ² / g, more preferably from to the 300~500m ² / g.

As the specific surface area of the carbon support in each layer, specifically, the specific surface area of the carbon carrier contained in the inlet-side catalyst layer (2-1), preferably 400~1200m ² / g, more preferably 600~900m ² / The specific surface area of the carbon support contained in the outlet side catalyst layer (2-2) is preferably 200 to 900 m ² / g, more preferably 250 to 350 m ² / g. At this time, the crystallinity of the carbon support is preferably such that the outlet side catalyst layer (2-2) is smaller than the inlet side catalyst layer (2-1).

The specific surface area of the carbon support contained in the inlet catalyst layer (1-1) is preferably 200 to 900 m ² / g, more preferably 250 to 350 m ² / g, and the outlet catalyst layer (1-2). the specific surface area of the carbon carrier contained in, preferably 70 to 250 ² / g, more preferably from 100 to 200 m ² / g. At this time, the crystallinity of the carbon support is preferably such that the outlet side catalyst layer (2-2) is smaller than the inlet side catalyst layer (2-1). At this time, the specific surface area of the carbon support is smaller in the outlet side catalyst layer (1-2) than in the inlet side catalyst layer (1-1), and is smaller than that in the inlet side catalyst layer (2-1). The inlet side catalyst layer (1-1) is smaller, and the outlet side catalyst layer (1-2) is preferably smaller than the outlet side catalyst layer (2-2).

  In the present invention, the specific surface area of the carbon support is a value measured by the BET method measured by nitrogen adsorption.

  In the above description, the catalyst layers (1) and (2) are divided into two regions toward the surface direction of the membrane electrode assembly. However, the catalyst layer (1) is further directed toward the surface direction of the membrane electrode assembly. And / or (2) may be divided into three or more regions. In this case, another layer may be disposed between the inlet side catalyst layer (1-1, 2-1) and the outlet side catalyst layer (1-2, 2-2). The specific surface area of the carbon support may be reduced from (1, 2-1) to the outlet catalyst layer (1-2, 2-2).

  The average particle diameter of the catalyst particles and the crystallinity of the carbon carrier increase from the inlet side to the outlet side of the gas flow path in the separator if at least one of the catalyst layer (1) and the catalyst layer (2). More preferably, it is applied to the catalyst layer (1) which is susceptible to corrosion of the carbon support and elution of the catalyst particles, most preferably both the catalyst layer (1) and the catalyst layer (2). Thereby, durability of a polymer electrolyte fuel cell can be improved more.

  The catalyst layer of the present invention includes at least a solid polymer electrolyte in addition to the electrode catalyst in which catalyst particles are supported on the carbon support described above.

  In the catalyst layer, the content of the solid polymer electrolyte is preferably increased from the separator side toward the solid polymer electrolyte membrane side. At this time, the content of the solid polymer electrolyte in the catalyst layer may increase stepwise or may gradually increase. In terms of the ease of production of the catalyst layer and the control of the solid polymer electrolysis mass, the number should be increased in stages. Therefore, it is preferable that the content of the solid polymer electrolyte in the catalyst layer (1) is larger than the content of the solid polymer electrolyte in the catalyst layer (2).

  As the solid polymer electrolysis mass in the catalyst layer increases, the proton transfer resistance decreases. For this reason, sufficient proton conductivity is ensured by raising the concentration of the solid polymer electrolyte at a site close to the solid polymer electrolyte membrane. On the other hand, when there is much solid polymer electrolysis mass, there exists a possibility that gas diffusibility and drainage may fall. For this reason, it is advisable to reduce the concentration of the solid polymer electrolyte in a region close to the separator to ensure gas diffusibility and drainage.

  The difference in the content of the solid polymer electrolyte in the catalyst layer (1) and the catalyst layer (2) is preferably 0 to 7% by mass, more preferably 0 to 3% by mass.

  Specifically, the content of the solid polymer electrolyte in the catalyst layer (1) is preferably 27 to 32% by mass with respect to the total weight (catalyst metal + carbon support + polymer electrolyte) of the catalyst layer (1). More preferably, the content of the solid polymer electrolyte in the catalyst layer (2) is preferably 28 to 31% by mass with respect to the total weight of the catalyst layer (2) (catalyst metal + carbon support + polymer electrolyte). Is 26 to 31% by mass, more preferably 27 to 30% by mass.

  The thickness of the catalyst layer (2) is preferably equal to or greater than the thickness of the catalyst layer (1) from the viewpoint of improving the diffusibility of the gas supplied to the catalyst layer and the discharge of produced water.

  The thickness of the catalyst layer (2) is preferably equal to or greater than the thickness of the catalyst layer (1) from the viewpoint of improving the diffusibility of the gas supplied to the catalyst layer and the discharge of produced water.

  More preferably, the thickness of the catalyst layer (2) is 1.0 to 7.5, more preferably 1.0 to 5.0 times, particularly 1.5 to 3.times. The thickness of the catalyst layer (1). 0 times. If it is such composition, both gas diffusion and discharge of generated water will advance effectively. Since the electron transfer path is sufficiently secured even with a relatively thin layer, the thickness of the catalyst layer (1) may be relatively thin. The thickness of each of the catalyst layer (1) and the catalyst layer (2) is calculated as an average film thickness. For example, the film to be measured is divided into nine parts, and the film is obtained from each cross section of nine regions using SEM photographs. It is calculated as an average value when the thickness is measured.

  Specifically, the thickness of the catalyst layer (2) is preferably 4 to 15 μm, more preferably 6 to 10 μm. The thickness of the catalyst layer (1) is preferably 2 to 7 μm, more preferably 2 to 5 μm. By setting the total film thickness of the catalyst layer (1) within this range, the amount of catalyst necessary for the power generation reaction is ensured. Further, an increase in battery size and an increase in electron transfer resistance are suppressed.

  The total film thickness of the catalyst layer having the catalyst layer (2) and the catalyst layer (1) is preferably 50 μm or less. If the thickness of the entire catalyst layer is too thin, it may not be possible to secure a sufficient amount of catalyst necessary for the electrode reaction, and battery performance and life characteristics may be deteriorated. On the other hand, if the thickness of the catalyst layer is too thick, the power generation performance may be reduced. Therefore, the thickness of the catalyst layer should be determined in consideration of battery performance and life characteristics.

  In the PEFC of the present invention, a laminated structure composed of two or more layers including the catalyst layer (1) and the catalyst layer (2) is used, and the average particle diameter of the catalyst particles used as the catalyst particle carrier is determined by the gas flow of the separator. The above-described catalyst layer having a configuration in which the height is increased from the inlet side to the outlet side of the road may be used for at least one of the fuel electrode catalyst layer and the oxygen electrode catalyst layer. Among them, it is preferably used for an oxygen electrode catalyst layer in which moisture retention occurs and the carbon support is likely to corrode, and more preferably used for both a fuel electrode catalyst layer and an oxygen electrode catalyst layer as shown in FIG. It is good to be done.

  Next, the second polymer electrolyte fuel cell of the present invention will be described. In the second polymer electrolyte fuel cell of the present invention, the catalyst layer has a laminated structure composed of two or more layers including the catalyst layer (1) and the catalyst layer (2), and the catalyst layer In at least one of (1) and the catalyst layer (2), the crystallinity of the carbon support and the content of platinum alloy particles in the catalyst particles increase from the inlet side to the outlet side of the gas flow path of the separator. It is characterized by this.

  In the second polymer electrolyte fuel cell of the present invention, in the catalyst layer (1) and / or the catalyst layer (2), the average particle size of the catalyst particles from the inlet side to the outlet side of the gas flow path of the separator A catalyst comprising two or more layers used in the first polymer electrolyte fuel cell of the present invention, except that the content of platinum alloy particles in the catalyst particles is increased instead of the configuration having an increased diameter. The structure is the same as that of the layer. Therefore, below, only the points different from the first polymer electrolyte fuel cell of the present invention will be described. That is, only the configuration in which the content of platinum alloy particles in the catalyst particles increases from the inlet side to the outlet side of the gas flow path of the separator in the catalyst layer (1) and / or the catalyst layer (2) will be described. .

  In the catalyst layer (1) and / or the catalyst layer (2), platinum particles and platinum alloy particles are used as catalyst particles for promoting the electrode reaction. The platinum particles have high catalytic activity, whereas the platinum alloy particles have excellent resistance to dissolution. In the catalyst layer (1) and / or the catalyst layer (2), platinum particles are arranged at a site where the catalyst particles are hardly dissolved, and platinum alloy particles are arranged at a site where the catalyst particles are easily dissolved. Thus, catalyst particles having a large particle diameter in the catalyst layer can be efficiently suppressed while maintaining high catalyst activity.

  Thus, in the second polymer electrolyte fuel cell of the present invention, the catalyst layer has a laminated structure composed of two or more layers, and the content of platinum alloy particles is set to the catalyst layer (1) and / or ( In 2), by elevating in a predetermined direction, elution of catalyst particles generated during the start / stop cycle of the fuel cell is suppressed at the same time as ensuring the electron conductivity and catalytic activity and improving the gas diffusibility in the catalyst layer. It becomes possible. Therefore, according to the present invention, it is possible to provide a polymer electrolyte fuel cell capable of maintaining high power generation performance over a long period of time.

  The content rate of the platinum alloy particles contained in the catalyst layer (1) and / or (2) is increased from the gas inlet side to the outlet side of the gas supply path of the separator. Further, the catalyst layer (1) and It is preferable to increase the content of platinum alloy particles contained in the catalyst layer from the separator side of the catalyst layer having (2) to the solid polymer electrolyte membrane side. As a result, platinum alloy particles having high dissolution resistance can be disposed in the catalyst layer where the catalyst particles are likely to be dissolved, and the durability of the PEFC can be further improved.

  In order to increase the content of platinum alloy particles contained in the catalyst layer from the separator side of the catalyst layer toward the solid polymer electrolyte membrane side, more preferably, the content of platinum alloy particles contained in the catalyst layer (1) Is preferably larger than the content of platinum alloy particles contained in the catalyst layer (2). Thereby, the content rate of the platinum alloy particles in the catalyst layer can be easily adjusted. Further, when there are three or more catalyst layers due to the presence of another catalyst layer (3) between the catalyst layer (1) and the catalyst layer (2), the catalyst layer The crystallinity of the carbon support contained in the catalyst layer (3) may be adjusted so that the crystallinity of the carbon support increases from (2) toward the catalyst layer (1).

  The content rate of the platinum alloy particles may increase stepwise from the inlet side to the outlet side of the gas flow path of the catalyst layer, more preferably from the separator side to the solid polymer electrolyte membrane side. You may increase gradually. Among these, since the production of the catalyst layer and the control of the crystallinity of the carbon support in the catalyst layer are easy, the content of platinum alloy particles should be increased stepwise.

  In the catalyst layer (1) and / or the catalyst layer (2), the range in which the platinum alloy particles are contained at a predetermined content may be appropriately determined in consideration of the durability and power generation performance of the obtained PEFC.

  As a preferred embodiment, for example, the same configuration as described above shown in FIG. 2 in which the catalyst layer is divided into two or more regions in the surface direction of the membrane electrode assembly can be mentioned. FIG. 2 is a schematic diagram of the catalyst layer 120, and the catalyst layer (1) is divided into two regions, that is, the inlet side catalyst layer (1-1) 121 i and toward the surface direction (arrow A) of the membrane electrode assembly. In the same manner, the catalyst layer (2-1) is divided into the inlet catalyst layer (2-2) 122i and the outlet catalyst layer (1) 122e. The platinum alloy particles are mixed with the inlet catalyst layer (1-1) 121i, the outlet catalyst layer (1-2) 121e, the inlet catalyst layer (2-1) 122i, and the outlet catalyst so as to have a predetermined content. Each layer (2-1) 122e is preferably included. When the catalyst layer is incorporated into the polymer electrolyte fuel cell, the inlet side catalyst layers (1-1, 2-1) are arranged so as to be close to the gas flow path inlet side of the separator, and the outlet side catalyst layer What is necessary is just to arrange | position so that (1-2,2-2) may adjoin to the gas flow path exit side of a separator.

  As a content rate of the platinum alloy particles in the catalyst particles in each layer, specifically, the content rate of the platinum alloy particles in the catalyst particles contained in the inlet side catalyst layer (2-1) is preferably 20 masses. %, More preferably 0 to 10% by mass, and the content of the platinum alloy particles in the catalyst particles contained in the outlet catalyst layer (2-2) is preferably 10 to 50% by mass, more preferably Is preferably 20 to 40% by mass.

  At this time, the content rate of the platinum alloy particles in the catalyst particles is preferably higher in the outlet catalyst layer (2-2) than in the inlet catalyst layer (2-1).

  The content of the platinum alloy particles in the catalyst particles contained in the inlet catalyst layer (1-1) is preferably 10 to 50% by mass, more preferably 20 to 40% by mass, and the outlet side The content of the platinum alloy particles in the catalyst particles contained in the catalyst layer (1-2) is preferably 30 to 100% by mass, more preferably 60 to 100% by mass.

  At this time, the content rate of the platinum alloy particles in the catalyst particles is higher in the outlet catalyst layer (1-2) than in the inlet catalyst layer (1-1), and the inlet catalyst layer ( 2-1) is higher in the inlet side catalyst layer (1-1), and the outlet side catalyst layer (1-2) is higher than the outlet side catalyst layer (2-2). Good.

  The content of platinum alloy particles in the catalyst particles in the catalyst layer is calculated from the amount of Pt-supported carbon and Pt alloy-supported carbon added to the catalyst ink prepared when each catalyst layer is formed. And ask.

  The range of the inlet side catalyst layer (1-1) and the outlet side catalyst layer (1-2) in the catalyst layer (1), the inlet side catalyst layer (2-1) and the outlet side catalyst layer ( The range 2-2) may be determined in consideration of the durability of the obtained polymer electrolyte fuel cell.

  The inlet catalyst layer (2-1) is preferably 30 to 60% by volume, more preferably 40 to 50% by volume, based on the entire catalyst layer (2).

  The inlet catalyst layer (1-1) is preferably 30 to 60% by volume, more preferably 40 to 50% by volume, based on the entire catalyst layer (1).

  In the above description, the catalyst layers (1) and (2) are divided into two regions in the flow direction of the gas flow path, but the catalyst layers (1) and (2) are further divided in the flow direction of the gas flow path. 2) may be divided into three or more regions. In this case, another catalyst layer may be disposed between the inlet side catalyst layer (1-1, 2-1) and the outlet side catalyst layer (1-2, 2-2). The content rate of the platinum alloy particles may be increased from the (-1, 2-1) to the outlet side catalyst layer (1-2, 2-2).

  The content of platinum alloy particles and the crystallinity of the carbon support increase from the inlet side to the outlet side of the gas flow path in the separator as long as they are at least one of the catalyst layer (1) and the catalyst layer (2). Is more preferably applied at least to the catalyst layer (1) where the catalyst particles are likely to be eluted, and most preferably both the catalyst layer (1) and the catalyst layer (2). Thereby, durability of a polymer electrolyte fuel cell can be improved more.

  In the first and second PEFCs of the present invention, the catalyst layer has a catalyst layer (1) and a catalyst layer (2). In addition to the crystallinity of the carbon support, the average particle diameter of the catalyst particles or the platinum alloy particles The materials used in the conventional PEFC can be used similarly except that the content rate has the above-described configuration. The constituent materials such as the solid polymer electrolyte membrane and the catalyst layer used in the first and second PEFCs of the present invention will be briefly described below, but these materials are limited to the exemplified materials and shapes. However, a conventionally well-known thing is used suitably.

  The solid polymer electrolyte membrane is a polymer membrane having proton conductivity. Various materials have been proposed as the solid polymer electrolyte membrane. For example, various Nafion (registered trademark of DuPont) manufactured by DuPont and perfluorosulfonic acid membranes represented by Flemion, ion exchange resin membranes, ethylene-tetrafluoroethylene copolymer resin membranes manufactured by Dow Chemical Co., Ltd. Fluoropolymer electrolytes such as resin membranes based on fluorostyrene, and hydrocarbon polymer resin membranes having sulfonic acid groups, such as polymer electrolyte membranes and polymer microporous membranes that are generally commercially available Alternatively, a membrane impregnated with a liquid electrolyte or a membrane in which a porous body is filled with a polymer electrolyte may be used.

  The thickness of the solid polymer electrolyte membrane may be appropriately determined in consideration of the properties of the obtained MEA, but is preferably 5 to 300 μm, more preferably 10 to 200 μm, and particularly preferably 15 to 150 μm. From the viewpoint of strength during film formation and durability during MEA operation, it is preferably 5 μm or more, and from the viewpoint of output characteristics during MEA operation, it is preferably 300 μm or less.

  The catalyst layer includes at least an electrode catalyst in which catalyst particles are supported on a carbon support and a solid polymer electrolyte.

  As the carbon carrier, any carbon carrier may be used as long as it has a specific surface area for supporting the catalyst particles in a desired dispersed state, and has sufficient electronic conductivity as a current collector. The main component is carbon. Is preferred. Specifically, carbon particles such as carbon black such as ketjen black, channel black, furnace black and thermal black, activated carbon, coke, natural graphite, artificial graphite and the like can be mentioned. Carbon black is preferably used because of its high specific surface area and excellent conductivity.

  The shape of the carbon support is not particularly limited, but it is preferably in the form of particles in order to carry the catalyst particles in a highly dispersed manner. The average particle diameter of the carbon particles is 5 to 200 nm, preferably about 10 to 100 nm, from the viewpoint of controlling the thickness of the electrode catalyst layer produced using the electrode catalyst within an appropriate range.

  The catalyst particles used for the electrode catalyst are required to have a catalytic action in the oxidation reaction of hydrogen and / or the reduction reaction of oxygen, and at least platinum particles are preferably used. Further, the catalyst particles may be platinum alloy particles made of an alloy of platinum and other metals in order to improve dissolution resistance, catalytic activity, poisoning resistance to carbon monoxide, heat resistance, and the like. . Specifically, the alloy is at least selected from platinum, ruthenium, iridium, rhodium, palladium, osmium, tungsten, lead, iron, chromium, cobalt, nickel, manganese, vanadium, molybdenum, gallium, and aluminum. Examples thereof include alloys with one or more metals.

  Among these, from the viewpoint of dissolution resistance, the platinum alloy particles are preferably an alloy of platinum and at least one metal selected from cobalt, ruthenium, and iridium. The composition of the alloy is preferably 30 to 90 atomic% for platinum and 10 to 70 atomic% for the metal to be alloyed, depending on the type of metal to be alloyed.

  In general, an alloy is a generic term for a metal element having one or more metal elements or non-metal elements added and having metallic properties. The alloy structure includes a eutectic alloy, which is a mixture of the constituent elements as separate crystals, a solid solution in which the constituent elements are completely mixed, and the constituent element is an intermetallic compound or a compound of a metal and a nonmetal. In the present application, any of them may be used.

  In addition to the electrode catalyst, the catalyst layer contains a solid polymer electrolyte. The solid polymer electrolyte is not particularly limited and a known one can be used, but any member having at least high proton conductivity may be used. Specifically, perfluorocarbon polymers having sulfonic acid groups such as Nafion (registered trademark, manufactured by DuPont), Flemion (registered trademark, manufactured by Asahi Glass Co., Ltd.), Aciplex (registered trademark, manufactured by Asahi Kasei Co., Ltd.), phosphoric acid, and the like. Hydrocarbon polymer compound doped with inorganic acid such as organic / inorganic hybrid polymer partially substituted with proton conductive functional group, polymer matrix impregnated with phosphoric acid solution or sulfuric acid solution And proton conductors.

  The PEFC of the present invention has a membrane electrode assembly in which a pair of catalyst layers, that is, a fuel electrode catalyst layer and an air electrode catalyst layer, are disposed on both sides of a solid polymer electrolyte membrane. A gas diffusion layer (GDL) may be disposed outside the air electrode catalyst layer.

  As a material used for GDL, a sheet-like material made of carbon paper, carbon cloth, non-woven fabric, carbon woven fabric, paper-like paper body, felt or the like has been proposed. GDL is also required to have functions such as electron conductivity and water repellency. When GDL has excellent electron conductivity, efficient transport of electrons generated by a power generation reaction is achieved, and the performance of the fuel cell is improved. Moreover, if GDL has excellent water repellency, the generated water is efficiently discharged.

  In order to ensure high water repellency, a technique for water repellency treatment of a material constituting the GDL has also been proposed. For example, a solution containing a fluorine-based resin such as polytetrafluoroethylene (PTFE) is impregnated with a material constituting GDL such as carbon paper, and dried in the air or an inert gas such as nitrogen. Depending on the case, the hydrophilization treatment may be performed on the material constituting the GDL. After drying, a carbon layer formed of carbon black powder and PTFE may be disposed.

  Various improvements may be made to the GDL in order to improve performance. For example, GDL gas diffusibility and compressibility may be improved by forming a layer composed of a fluororesin and carbon black on the surface of a carbon fiber woven sheet-like material (for example, Japanese Patent Laid-Open No. Hei 10). -261421, JP-A-11-273688).

  The separator used in the polymer electrolyte fuel cell of the present invention can be used without limitation as long as it is conventionally known, such as those made of carbon such as dense carbon graphite and carbon plate, and those made of metal such as stainless steel. . The separator has a function of separating the oxidant gas and the fuel gas, and preferably has a gas flow path for securing the flow paths thereof. The thickness and size of the separator, the shape of the gas flow path, and the like are not particularly limited, and may be appropriately determined in consideration of the output characteristics of the obtained fuel cell. Examples of the shape of the gas flow path in the separator include a meandering shape and a linear shape from one end of the separator to the other end.

  In addition to the above-described ones, various members can be installed in the PEFC of the present invention as necessary. For example, a gasket that prevents leakage of gas supplied to the PEFC to the outside is disposed.

  In the polymer electrolyte fuel cell of the present invention, a stack in which a plurality of membrane electrode assemblies are stacked and connected in series via a separator is formed so that the desired voltage of the polymer electrolyte fuel cell can be obtained. Also good. The shape of the fuel cell is not particularly limited, and may be determined as appropriate so that desired battery characteristics such as voltage can be obtained.

  The use of the polymer electrolyte fuel cell of the present invention is not particularly limited. The polymer electrolyte fuel cell of the present invention is preferably used for a vehicle such as an automobile. Vehicles such as automobiles are not only prone to corrosion of the carbon support of the fuel cell due to frequent start and stop, but also have a high cell voltage (about 0.80 V or more) during traffic jams or in urban areas. Voltage fluctuations (load fluctuations) frequently occur and catalyst particles are likely to dissolve. As described above, the polymer electrolyte fuel cell of the present invention is excellent in the corrosion resistance of the carbon support and the elution resistance of the catalyst particles, and thus has higher performance when used as a driving power source in a vehicle such as an automobile. It becomes possible to demonstrate.

  Hereinafter, a preferred embodiment of the method for producing a catalyst layer comprising the catalyst layer (1) and the catalyst layer (2) used in the PEFC of the present invention will be described.

  First, a catalyst slurry for preparing a catalyst layer (1) having no cracks is prepared. The catalyst slurry is mixed with a material constituting the catalyst layer, such as an electrode catalyst and a solid polymer electrolyte. Examples of the solvent that can be used in the slurry include water and / or alcohol solvents such as methanol and ethanol.

  The catalyst slurry may be applied to a predetermined sheet such as a water-repellent substrate and dried, and then the obtained catalyst layer (1) may be transferred to the surface of the solid polymer electrolyte membrane. The slurry may be applied directly to the surface of the membrane. The coating film formed on the water repellent substrate is transferred onto the polymer electrolyte membrane by hot pressing. After hot pressing, the water repellent substrate is peeled off.

  In order to suppress the occurrence of cracks in the catalyst layer (1), it is better not to use a porous substrate as the base material on which the catalyst slurry is applied. Further, the catalyst slurry is applied on the water-repellent substrate or the solid polymer electrolyte membrane by reducing the thickness of the catalyst slurry once, and then dried, so that a catalyst layer having a desired thickness is produced. Is good.

  At this time, the application method is not particularly limited, and can be performed using a known method such as a die coater method, a screen printing method, a doctor blade method, a spray method, or the like. The applied slurry may be dried at 20 to 25 ° C. for about 0.5 to 2 hours.

  Next, as a method for producing the cracked catalyst layer (2), the catalyst slurry prepared in the same manner as described above was applied to a water repellent substrate, a substrate such as carbon paper used for a gas diffusion layer, and dried. Is used.

  In order to generate cracks in the catalyst layer (2), it is preferable to use a porous substrate for applying the catalyst slurry. Specifically, carbon paper used for the gas diffusion layer is preferably used. By using such a porous base material, it is considered that the dry state of the catalyst slurry can vary, and volume shrinkage occurs in a fast-drying part, so that the slow-drying part is pulled and a crack is generated. The drying temperature of the catalyst slurry may be about 20 to 25 ° C.

  Moreover, the crack in a catalyst layer (2) can be generated also by adjusting the drying temperature at the time of drying the apply | coated catalyst slurry. Specifically, the catalyst slurry applied on a substrate such as a water-repellent substrate or a gas diffusion layer is preferably heated and dried at about 70 to 100 ° C.

  Furthermore, cracks can be generated in the catalyst layer (2) obtained by adding a foaming agent such as camphor to the catalyst slurry.

  In the first polymer electrolyte fuel cell of the present invention, in the catalyst layer, the average particle diameter of the catalyst particles is increased in addition to the crystallinity of the carbon support from the inlet side to the outlet side of the gas flow path of the separator. . To prepare such a catalyst layer, when preparing the catalyst ink, a plurality of catalyst inks containing electrode catalysts having different carbon carrier crystallinity and average particle diameter of the catalyst particles are prepared, and each catalyst ink is applied. A method of adjusting the site may be used.

  In the second polymer electrolyte fuel cell of the present invention, in the catalyst layer, the content of platinum alloy particles increases in addition to the crystallinity of the carbon support from the inlet side to the outlet side of the gas flow path of the separator. . In order to prepare such a catalyst layer, when preparing a catalyst ink in the same manner as described above, a plurality of catalyst inks containing electrode catalysts having different carbon carrier crystallinity and platinum alloy particle content are prepared. What is necessary is just to use the method of adjusting the site | part which apply | coats each catalyst ink.

  Hereinafter, although the present invention is explained using an example, the technical scope of the present invention is not limited to the following example.

Example 1
1. Preparation of Ink for Catalyst Layer For electrode catalyst 1 in which platinum particles (average particle size 2.5 nm, supported amount about 47% by mass) are supported on a carbon support (Ketjen black, specific surface area about 800 m ² / g) 2.5 parts by weight of water, 9 parts by weight of 5 wt% Nafion ^TM solution and 1 part by weight of 1-propanol were mixed and dispersed and mixed with a homogenizer to prepare catalyst layer ink A.

Next, platinum particles (average particle diameter of about 3.2 nm, carbon dioxide (Ketjen black) on a carbon support (specific surface area of about 300 m ² / g) heat-treated in a nitrogen gas atmosphere at 1300 ° C. for about 8 hours. With respect to the electrode catalyst 2 supporting a supported amount of about 47% by mass), 2.5 parts by weight of pure water, 9 parts by weight of a 5 wt% Nafion ^TM solution, and 1 part by weight of 1-propanol are mixed and dispersed and mixed by a homogenizer. Catalyst layer ink B was prepared.

Next, platinum particles (average particle diameter of about 4.5 nm, on a carbon support (specific surface area of about 120 m ² / g) on a carbon support (specific surface area of about 120 m ² / g) heat treated in a nitrogen gas atmosphere at 2000 ° C. for about 10 hours. The electrode catalyst 3 supporting a supported amount of about 47% by mass) is mixed with 2.5 parts by weight of pure water, 9 parts by weight of a 5 wt% Nafion ^TM solution and 1 part by weight of 1-propanol, and dispersed and mixed with a homogenizer. Catalyst layer ink C was prepared.

2. Preparation of oxygen electrode catalyst layer An oxygen electrode catalyst layer was formed using catalyst layer ink A, catalyst layer ink B, and catalyst layer ink C prepared as described above. In this example, since the oxygen electrode catalyst layer has a two-layer structure, a catalyst layer (1) and a catalyst layer (2) were prepared below.

  First, the catalyst layer (1) was formed on a Teflon sheet having a thickness of 0.08 mm using a screen printer. The application area of the catalyst ink is 50 mm × 50 mm as a whole, and the catalyst layer ink B is applied to a portion of 50 mm × 25 mm, and the remaining 50 mm × 25 mm is applied to the catalyst layer ink C, and then about 1 at about 25 ° C. Let dry for hours. As a result, a catalyst layer (1) (thickness of about 4 μm, porosity of about 35% by volume) without cracks was obtained.

  Next, the catalyst layer (2) was formed on a carbon paper (thickness: about 300 μm, size: 52 mm × 63 mm) with a carbon layer (carbon black + PTFE particles) used as a gas diffusion layer, using a table coater. After the catalyst ink application area is 50 mm × 50 mm as in the catalyst layer 1 as a whole, the catalyst layer ink A is applied to the 50 mm × 25 mm portion, and the catalyst layer ink B is applied to the remaining 50 mm × 25 mm portion. And dried at about 25 ° C. for about 1 hour. As a result, a catalyst layer (2) (thickness: about 8 μm, porosity: about 70%) in which cracks were formed was obtained. In order to apply the catalyst layer ink only to a predetermined portion on the carbon layer, the catalyst ink was applied using a mask having an opening having a predetermined size.

3. Preparation of fuel electrode catalyst layer Next, the catalyst layer ink A prepared above was applied to a 50 mm × 50 mm portion on a Teflon sheet having a thickness of 0.08 mm using a screen printer, and about 25 C. for about 1 hour. As a result, the thickness of the fuel electrode catalyst layer (thickness: about 10 μm, porosity: about 35%) in which no crack was formed was obtained.

4). Fabrication of PEFC A solid polymer electrolyte membrane (Nafion ^TM 111, thickness 25 μm, size 72 mm × 72 mm) is sandwiched between a Teflon sheet having a catalyst layer (1) and a Teflon sheet having a fuel electrode catalyst layer. The catalyst layer (1) and the fuel electrode catalyst layer are integrated by hot pressing at 150 ° C. for 10 minutes, and the catalyst layer 2 is disposed on the catalyst layer 1 after peeling the Teflon sheet (at this time) The portion coated with the catalyst layer ink C in the catalyst layer (1) and the portion coated with the catalyst layer ink B in the catalyst layer (2) are in contact with each other), and the carbon layer on the fuel electrode catalyst layer. Arrange carbon paper (carbon black + PTFE particles) (thickness about 300μm, size 52mm x 63mm) and integrate them to make a membrane electrode assembly (MEA) It was.

  The membrane electrode assembly was sandwiched between a pair of separators to produce a PEFC single cell. The separator is provided with a serpentine type gas supply path, and a portion coated with the catalyst layer ink B in the catalyst layer (1) and a portion coated with the catalyst layer ink A in the catalyst layer (2). And a portion coated with the catalyst layer ink C in the catalyst layer (1) and a portion coated with the catalyst layer ink B in the catalyst layer (2), The membrane electrode assembly was taught by a pair of separators so as to be close to the outlet side of the gas supply path.

5. Evaluation Evaluation of initial power generation characteristics and durability of the PEFC produced above was performed according to the following procedure.

(1) Initial power generation characteristics Cell temperature: 70 ° C., fuel electrode: hydrogen (60% RH, utilization rate 67%), oxidizer electrode: air (50% RH, utilization rate 40%), supply gas is not pressurized Measured. A power generation test was performed under these conditions, and initial cell voltages at 0.2 A / cm ² and 1.0 A / cm ² were measured. The results are shown in Table 1.

(2) Durability 1
The cell temperature and supply gas humidification conditions were the same as the initial power generation characteristics. Power generation: A cycle of 3 minutes and a stop of 3 minutes was performed, the cell voltage after 1000 cycles was measured, and the durability was compared by the difference (Δ) between the cell voltage after 1000 cycles and the initial cell voltage.

The power generation conditions were such that 260 cc / min of pure hydrogen was supplied to the fuel electrode and 1050 cc / min of air was supplied to the oxidizer electrode. The load rise time from 0 A to 1 A / cm ² was 30 seconds.

  The gas conditions during the stop are shown below. After the power generation of the fuel cell is completed, the current load is turned off and at the same time, 100 cc / min non-humidified air is supplied to the fuel electrode, and the gas is not supplied to the oxidizer electrode, and this state is maintained for 2 minutes and 30 seconds. . Thereafter, with the current load turned off, 260 cc / min of hydrogen was supplied to the fuel electrode and 1050 cc / min of air was supplied to the oxidizer electrode. The results are shown in Table 2.

(3) Durability 2
Cell temperature: 70 ° C., fuel electrode: hydrogen (100% RH, 500 cc / min), oxidant electrode: nitrogen (100% RH, 500 cc / min), supply gas was measured without pressurization. Under this condition, using a potentiostat, a potential of 0.65 V was applied to the oxidizer electrode for 30 seconds and then a potential of 0.95 V was applied to the fuel electrode for 30 seconds, after 10,000 cycles. The cell voltage was measured, and the durability was compared with the difference (Δ) between the cell voltage after 10,000 cycles and the initial cell voltage. The results are shown in Table 3.

(Example 2)
0.8 parts by weight of an electrode catalyst 4 supporting platinum particles (average particle diameter of about 3.2 nm, supported amount of about 47% by mass) on a heat-treated carbon support, and platinum-cobalt alloy particles (average particles on the heat-treated carbon support 0.2 parts by weight of an electrode catalyst 5 having a diameter of about 4 nm, a supported amount of about 50% by weight, and a Pt: Co mass ratio of 3: 1), 2.5 parts by weight of pure water, and 9 parts by weight of a 5 wt% Nafion ^TM solution 1 part by weight of 1-propanol was mixed and dispersed and mixed with a homogenizer to prepare catalyst layer ink B ′. In the electrode catalyst 4 and the electrode catalyst 5, the heat-treated carbon carrier was a carbon carrier (Ketjen black) heat-treated in a nitrogen gas atmosphere at 1300 ° C. for about 8 hours and had a specific surface area of about 300 m ² / g. It was.

Next, 0.1 part by weight of an electrode catalyst 6 supporting platinum particles (average particle diameter of about 4.5 nm, supported amount of about 47% by mass) on the heat-treated carbon support, and platinum-cobalt alloy particles on the heat-treated carbon support 7 parts by weight of electrode catalyst 7 (average particle size: about 5.2 nm, supported amount: about 50% by mass, Pt: Co mass ratio: 3: 1), 2.5 parts by weight of pure water, 5 wt% Nafion ^TM solution 9 parts by weight and 1 part by weight of 1-propanol were mixed and dispersed and mixed with a homogenizer to prepare catalyst layer ink C ′. In the electrode catalyst 6 and the electrode catalyst 7, as the heat-treated carbon carrier, a carbon carrier (Ketjen black) heat-treated in a nitrogen gas atmosphere at 2000 ° C. for about 10 hours is used. The specific surface area is about 120 m ² / g.

  A PEFC was prepared and evaluated in the same manner as in Example 1 except that the catalyst ink B 'was used in place of the catalyst ink B and the catalyst ink C' was used in place of the catalyst ink C. The results are shown in Tables 1-3.

(Example 3)
1 part by weight of an electrode catalyst 8 having platinum particles (average particle diameter of about 3 nm, supported amount of about 47% by mass) supported on a carbon support (Vulcan XC-72, specific surface area of about 270 m ² / g), pure water 2.5 weights 9 parts by weight of a 5 wt% Nafion ^TM solution and 1 part by weight of 1-propanol were mixed and dispersed and mixed with a homogenizer to prepare catalyst layer ink B ″.

Next, 1 part by weight of an electrode catalyst 10 having platinum particles (average particle diameter of about 4.1 nm, supported amount of about 47% by mass) supported on a carbon support (acetylene black, specific surface area of about 100 m ² / g), pure water 2 5 parts by weight, 9 parts by weight of 5 wt% Nafion ^TM solution and 1 part by weight of 1-propanol were mixed and dispersed and mixed with a homogenizer to prepare catalyst layer ink C ″.

  A PEFC was prepared and evaluated in the same manner as in Example 1 except that the catalyst ink B ″ was used instead of the catalyst ink B and the catalyst ink C ″ was used instead of the catalyst ink C. The results are shown in Tables 1-3.

Example 4
0.8 parts by weight of an electrode catalyst 11 having platinum particles (average particle diameter of about 3 nm, supported amount of about 50% by mass) supported on a carbon support (Vulcan XC-72, specific surface area of about 270 m ² / g), carbon support (Vulcan XC-72, a specific surface area of about 270 m ² / g) and platinum-cobalt alloy particles (average particle diameter of about 4 nm, supported amount of about 50 mass%, Pt: Co mass ratio of 3: 1) 2 parts by weight, 2.5 parts by weight of pure water, 9 parts by weight of a 5 wt% Nafion ^TM solution and 1 part by weight of 1-propanol were mixed and dispersed and mixed with a homogenizer to prepare catalyst layer ink B ′ ″.

Next, 0.1 parts by weight of an electrode catalyst 13 having platinum particles (average particle diameter of about 4.1 nm, supported amount of about 50% by mass) supported on a carbon support (acetylene black, specific surface area of about 100 m ² / g), carbon Electrocatalyst 140 in which platinum-cobalt alloy particles (average particle diameter of about 5 nm, supported amount of about 50 mass%, Pt: Co mass ratio of 3: 1) are supported on a support (acetylene black, specific surface area of about 100 m ² / g) 9 parts by weight, 2.5 parts by weight of pure water, 9 parts by weight of 5 wt% Nafion ^TM solution and 1 part by weight of 1-propanol were mixed and dispersed and mixed with a homogenizer to prepare catalyst layer ink C ′ ″.

  A PEFC was prepared and evaluated in the same manner as in Example 1 except that the catalyst ink B "'was used in place of the catalyst ink B and the catalyst ink C"' was used in place of the catalyst ink C. The results are shown in Tables 1-3.

(Comparative Example 1)
The catalyst layer ink A prepared in the same manner as in Example 1 was applied to a 50 mm × 50 mm portion on a 0.08 mm thick Teflon sheet using a screen printer and dried at about 25 ° C. for about 1 hour. By repeating this coating and drying process 6 times, a catalyst layer (thickness 12 μm, porosity of about 35%) without cracks was obtained.

Using two Teflon sheets with a catalyst layer formed as described above, with the catalyst layer on the inside, sandwich the solid polymer electrolyte membrane (Nafion ^™ 111, thickness 25 μm, size 72 mm × 72 mm) The catalyst layer and the solid polymer electrolyte membrane were integrated by hot pressing at 150 ° C. for 10 minutes, and this was further combined with carbon paper (carbon black + PTFE particles) (thickness about 300 μm, size 52 mm × 63 mm), and sandwiched by using two sheets to prepare a membrane electrode assembly.

  A PEFC was produced in the same manner as in Example 1 using the membrane electrode assembly, and this was evaluated. The results are shown in Tables 1-3.

(Comparative Example 2)
A catalyst layer ink A prepared in the same manner as in Example 1 was applied to a 50 mm × 50 mm portion of carbon paper (thickness: about 300 μm, size: 52 mm × 63 mm) with a carbon layer (carbon black + PTFE particles). And then dried at 40 ° C. for 10 minutes and at 60 ° C. for 20 minutes. By repeating this coating and drying process 6 to 8 times, a catalyst layer having a crack (thickness 12 μm, porosity of about 35%) ) Was formed.

Using two pieces of carbon paper with the catalyst layer formed as described above, the catalyst layer is inside, and a solid polymer electrolyte membrane (Nafion ^™ 111, thickness 25 μm, size 72 mm × 72 mm) is sandwiched The membrane electrode assembly was manufactured by integrating the catalyst layer and the solid polymer electrolyte membrane by hot pressing at 150 ° C. for 10 minutes.

  A PEFC was produced in the same manner as in Example 1 using the membrane electrode assembly, and this was evaluated. The results are shown in Tables 1-3.

The cross-sectional schematic diagram of the 1st and 2nd polymer electrolyte fuel cell of this invention is shown. The schematic diagram of the catalyst layer used for the 1st and 2nd polymer electrolyte fuel cell of this invention is shown.

Explanation of symbols

100: Membrane electrode assembly,
110 ... polymer electrolyte membrane,
120, 120a and 120c ... catalyst layer,
121a and 121c ... catalyst layer (2),
122a and 122c ... catalyst layer (1),
121i ... Inlet side catalyst layer (1-1),
121e ... Outlet side catalyst layer (1-2),
122i ... Inlet side catalyst layer (2-1),
122e ... Outlet side catalyst layer (2-2),
123a and 123c ... cracks,
140a and 140c ... separators,
141: Gas supply path,
150: Solid polymer fuel cell.

Claims (18)

A membrane electrode assembly in which a pair of catalyst layers is disposed on both sides of a solid polymer electrolyte membrane is sandwiched by a separator having a gas flow path,
The catalyst layer is a solid polymer fuel cell including at least an electrode catalyst having catalyst particles supported on a carbon support and a solid polymer electrolyte,
At least one of the catalyst layers includes a catalyst layer (1) that is in contact with the solid polymer electrolyte membrane and does not have cracks, and a catalyst layer (2) that has cracks is the thickness of the membrane electrode assembly. Laminated in the direction,
At least one of the catalyst layer (1) and the catalyst layer (2) has an average particle diameter of the catalyst particles that increases from the inlet side to the outlet side of the gas flow path, and A polymer electrolyte fuel cell in which crystallinity increases from an inlet side to an outlet side of the gas flow path.   The polymer electrolyte fuel cell according to claim 1, wherein the porosity of the catalyst layer (2) is 1.5 to 3.0 times the porosity of the catalyst layer (1).   3. The solid polymer fuel cell according to claim 1, wherein an average particle diameter of the catalyst particles contained in the catalyst layer further increases from the separator side toward the solid polymer electrolyte membrane side. The catalyst layer (2) includes an inlet side catalyst layer (2-1) and an outlet side catalyst layer (2-2) arranged in the surface direction of the membrane electrode assembly,
The average particle diameter of the catalyst particles contained in the inlet catalyst layer (2-1) is 2 to 4 nm, and the average particle diameter of the catalyst particles contained in the outlet catalyst layer (2-2) is 2. The polymer electrolyte fuel cell according to any one of claims 1 to 3, which is 5 to 5 nm. The catalyst layer (1) includes an inlet-side catalyst layer (1-1) and an outlet-side catalyst layer (1-2) arranged in the surface direction of the membrane electrode assembly,
The average particle diameter of the catalyst particles contained in the inlet side catalyst layer (1-1) is 2.5 to 5 nm, and the average particle diameter of the catalyst particles contained in the outlet side catalyst layer (1-2) is 4-6 nm,
The average particle diameter of the catalyst particles is larger in the outlet side catalyst layer (1-2) than in the inlet side catalyst layer (1-1), and in the inlet than in the inlet side catalyst layer (2-1). The side catalyst layer (1-1) is larger, the inlet side catalyst layer (2-2) is larger than the inlet side catalyst layer (2-1), and the outlet side catalyst layer (2-2). The polymer electrolyte fuel cell according to any one of claims 1 to 4, wherein the outlet side catalyst layer (1-2) is larger than the outlet side catalyst layer (1-2). A membrane electrode assembly in which a pair of catalyst layers is disposed on both sides of a solid polymer electrolyte membrane is sandwiched by a separator having a gas flow path,
The catalyst layer includes at least an electrode catalyst in which catalyst particles are supported on a carbon support, and a solid polymer electrolyte,
The catalyst particles are solid polymer fuel cells containing platinum particles and platinum alloy particles,
At least one of the catalyst layers includes a catalyst layer (1) that is in contact with the solid polymer electrolyte membrane and does not have cracks, and a catalyst layer (2) that has cracks is the thickness of the membrane electrode assembly. Laminated in the direction,
At least one of the catalyst layer (1) and the catalyst layer (2) has a higher content of the platinum alloy particles from the inlet side to the outlet side of the gas flow path, and A polymer electrolyte fuel cell in which crystallinity increases from an inlet side to an outlet side of the gas flow path.   The polymer electrolyte fuel cell according to claim 6, wherein the porosity of the catalyst layer (2) is 1.5 to 3.0 times the porosity of the catalyst layer (1).   The solid polymer fuel cell according to claim 6 or 7, wherein an average particle diameter of the platinum alloy particles contained in the catalyst layer further increases from the separator side toward the solid polymer electrolyte membrane side. The catalyst layer (2) includes an inlet side catalyst layer (2-1) and an outlet side catalyst layer (2-2) arranged in the surface direction of the membrane electrode assembly,
The content of the platinum alloy particles in the catalyst particles contained in the inlet catalyst layer (2-1) is less than 20% by mass, and the catalyst particles contained in the outlet catalyst layer (2-2) The platinum alloy particle content is 10-50% by mass,
The content rate of the platinum alloy particles in the catalyst particles is higher in the outlet side catalyst layer (2-2) than in the inlet side catalyst layer (2-1). Solid polymer fuel cell. The catalyst layer (1) includes an inlet-side catalyst layer (1-1) and an outlet-side catalyst layer (1-2) arranged in the surface direction of the membrane electrode assembly,
The catalyst particles contained in the outlet side catalyst layer (1-2) having a content of 10 to 50% by mass of the platinum alloy particles in the catalyst particles contained in the inlet side catalyst layer (1-1). The content of the platinum alloy particles is 30 to 100% by mass,
The content rate of the platinum alloy particles in the catalyst particles is higher in the outlet side catalyst layer (1-2) than in the inlet side catalyst layer (1-1), and the inlet side catalyst layer (2-1). The inlet side catalyst layer (1-1) is higher than the outlet side catalyst layer (2-2), and the outlet side catalyst layer (1-2) is higher than the outlet side catalyst layer (2-2). The solid polymer fuel cell according to any one of the above.   The polymer electrolyte fuel cell according to any one of claims 1 to 10, wherein the crystallinity of the carbon support contained in the catalyst layer further increases from the separator side toward the solid polymer electrolyte membrane side.   12. The polymer electrolyte fuel cell according to claim 1, wherein the crystallinity of the carbon support is adjusted by graphitization of the carbon support. The catalyst layer (2) includes an inlet side catalyst layer (2-1) and an outlet side catalyst layer (2-2) arranged in the surface direction of the membrane electrode assembly,
The carbon carrier contained in the inlet catalyst layer (2-1) has a specific surface area of 400 to 1200 m ² / g, and the carbon carrier contained in the outlet catalyst layer (2-2) has a specific surface area of 200. ~900m is a ² / g,
13. The polymer electrolyte fuel cell according to claim 1, wherein a specific surface area of the carbon support is smaller in the outlet side catalyst layer (2-2) than in the inlet side catalyst layer (2-1). . The catalyst layer (1) includes an inlet-side catalyst layer (1-1) and an outlet-side catalyst layer (1-2) arranged in the surface direction of the membrane electrode assembly,
The carbon carrier contained in the inlet catalyst layer (1-1) has a specific surface area of 200 to 900 m ² / g, and the carbon carrier contained in the outlet catalyst layer (1-2) has a specific surface area of 70. ~250m is a ² / g,
The specific surface area of the carbon carrier is smaller in the outlet side catalyst layer (1-2) than in the inlet side catalyst layer (1-1), and more in the inlet side than in the inlet side catalyst layer (2-1). The solid according to any one of claims 1 to 13, wherein the catalyst layer (1-1) is smaller and the outlet catalyst layer (1-2) is smaller than the outlet catalyst layer (2-2). Polymer fuel cell.   The solid polymer fuel cell according to any one of claims 1 to 14, wherein the content of the solid polymer electrolyte contained in the catalyst layer increases from the separator side toward the solid polymer electrolyte membrane side.   The solid polymer fuel cell according to any one of claims 1 to 15, wherein a thickness of the catalyst layer (2) is equal to or greater than a thickness of the catalyst layer (1).   The polymer electrolyte fuel cell according to any one of claims 1 to 16, wherein the thickness of the catalyst layer (2) is 1.5 to 3.0 times the thickness of the catalyst layer (1). .   An automobile equipped with the polymer electrolyte fuel cell according to claim 1.

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