JP3579885B2 - Electrode structure for fuel cell and manufacturing method thereof - Google Patents

Description

【００３３】
表１および図５に示す通り、電極触媒層１と電解膜Ｍとを一体成形した電極構造体ＭＥＡは、良好な冷熱剥離率およびクロスリーク量（ガス透過性ｃｃ／ｃｍ^２・分）を示し、特に触媒粒子の侵入深さ５〜２０μｍ（密度傾斜係数８５９．００〜３４３６．００）の範囲のものが特に好ましいことが分かる。一方、電極触媒層と電解膜が一体成形されていない比較例１では冷熱剥離率が著しく劣っているのが分かる。
ちなみに、侵入深さが浅いと、密度傾斜係数が大きくなり、冷熱剥離率も大きくなる傾向にあることが分かる。逆に侵入深さが深いと、密度傾斜係数が小さくなり冷熱剥離率も小さくなる傾向にあることが分かる。また、触媒の侵入深さを深くするには、スラリーの粘度が小さい方がよいことが分かる。同時に、触媒の侵入深さを深くするには、残存溶媒が多い方がよいことが分かる。
また、図６に示す通り、本発明の電極構造体ＭＥＡは比較例１の電極構造体と比較して測定した全ての電流密度範囲で端子電圧が高いことが分かる。従って、本発明の電極構造体ＭＥＡは、従来の電極構造体と比較して耐久性が優れているだけでなく、より高い電力を供給することができる。
【００３４】
【発明の効果】
以上説明した通り、本発明の電極構造体は、触媒粒子の電解膜への侵入深さが５μｍ〜２０μｍの範囲内とすることができ、電極触媒層が形成される際に、電極触媒層と電解膜とが両者の境界面で組成が連続的に変化して一体形成される。したがって、電解膜と電極触媒層との界面における剥離が発生せず、また所定の温度サイクルにおいても電極構造体の耐久性が増加することが可能となる（請求項１）。なお、電解膜と電極触媒層を一体形成した電極構造体を含む燃料電池単セルは、電極構造体において電解膜と電極触媒層の界面における剥離が発生せず、燃料電池全体の耐久性を向上させることが可能となる。しかも、この燃料電池は、従来技術のものと比較して高い出力を得ることができる。また、電極触媒層と電解膜との界面におけるイオン交換密度傾斜係数が３．５×１０³ｍｅｑ／ｇ／ｃｍ以下とすると、より高い耐久性が得られる（請求項２）。
このように優れた電極構造体は、電極触媒層を構成する触媒粒子を極性溶媒に溶解した後、イオン導伝性高分子溶液に分散させて粘度５，０００〜２５，０００ｍＰａ・秒のスラリーを調製し、このようにして調製したスラリーを電解膜に直接塗布し、１．５〜２．５ＭＰａの圧力条件、１２０〜１８０℃の温度条件及び３０〜６０秒の時間条件でホットプレスして触媒を電解膜へ侵入させて電極触媒層を電解膜と一体形成することにより容易に製造することができる（請求項３）。また、電解膜に直接塗布した触媒粒子分散イオン導伝性高分子の有機溶媒を２０ｍｇ／ｃｍ²〜１００ｍｇ／ｃｍ²の量で残存した状態でホットプレスして触媒粒子を電解膜へ侵入させるとさらに優れた耐久性を有する電極構造体を容易・かつ確実に製造することが可能となる（請求項４）。
【図面の簡単な説明】
【図１】本発明が適用される燃料電池単セルの概略を示す概略図である。
【図２】本発明の電極構造体（燃料電池用電極構造体）の断面図である
【図３】触媒粒子の構成を示す模式図である。
【図４】本発明の電極構造体の製造の様子を示す模式図である。
【図５】本発明および比較例における電極触媒層の侵入深さとガス透過性および冷熱剥離率の関係を示すグラフである。
【図６】本発明および比較例における電流密度と端子電圧の関係を示すグラフである。
【符号の説明】
ＦＣ 燃料電池
ＭＥＡ 電極構造体（燃料電池用電極構造体）
Ｍ 電解膜
１ 電極触媒層
２ 拡散層
３ セパレータ
４ 流路[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to a fuel cell electrode structure used for a fuel cell and a method for manufacturing the same. More specifically, the present invention relates to a fuel cell electrode structure in which an electrode catalyst layer and an electrolyte membrane are integrally formed, and a method for manufacturing the same.
[0002]
[Prior art]
The fuel cell system is a fuel cell system that supplies hydrogen as a fuel gas to the hydrogen electrode side of the fuel cell and supplies an oxidizing gas containing oxygen to the oxygen electrode side of the fuel cell to generate electric power. . Fuel cells, which form the core of this fuel cell system, convert chemical energy directly into electric energy, and have recently been receiving attention because of their high power generation efficiency and extremely low emission of harmful substances.
[0003]
First, a single fuel cell constituting a fuel cell will be described with reference to FIG.
As shown in FIG. 1, the fuel cell unit cell CE has a fuel cell electrode composed of electrode catalyst layers 1 ( _1H , _1O ) provided on both sides of the electrolyte membrane M on the hydrogen electrode side and the oxygen electrode side. Diffusion layers 2 _H , 2 _O and separators 3 _H , 3 _O are laminated on both sides of the structure MEA, respectively. The member on the hydrogen electrode side has a suffix H after the numeral, and the member on the oxygen electrode side has a suffix O after the numeral. Is not followed by a subscript.
[0004]
As the electrolyte membrane M, a solid polymer membrane, for example, a perfluorocarbon sulfonic acid membrane which is a proton (ion) exchange membrane is generally used. The electrolyte membrane M has a large number of proton exchange groups in the solid polymer, shows a low specific resistance of 20 Ω / cm proton or less at room temperature by containing saturated water, and functions as a proton conductive electrolyte. Since a solid polymer membrane is used for the fuel cell unit CE as described above, a fuel cell configured by stacking the unit cells CE is called a solid polymer fuel cell.
[0005]
The electrode catalyst layer 1 is configured by dispersing catalyst particles each having a catalyst metal having an oxidation / reduction catalytic function such as platinum supported on a carrier such as carbon in an ionic (proton) conductive resin.
[0006]
Further, the diffusion layer 2 is provided in contact with the flow path 4 on the surface of the separator 3 to transfer electrons between the electrode catalyst layer 1 and the separator 3, as well as a fuel gas (hydrogen gas) and an oxidizing gas. It has a function of diffusing (air) and supplying it to the electrode catalyst layer 1, and is generally formed of a carbon-based material such as carbon paper, carbon cloth, and carbon felt.
The separator 3 is made of a material having excellent airtightness and thermal conductivity, has a function of separating a fuel gas, an oxidizing gas and a refrigerant, has a flow path 4, and has an electron transfer function.
[0007]
In this single fuel cell CE, when supply air flows through the oxygen electrode side gas flow path 4 _O of the separator 3 _O and supply hydrogen H ₂ is supplied to the hydrogen electrode side gas flow path 4 _H of the separator 3 _H. On the hydrogen electrode side, hydrogen is ionized by the catalytic action of the catalyst in the electrode catalyst layer _1H to generate protons, and the generated protons move through the electrolytic film M and reach the oxygen electrode side. Then, protons reach the oxygen electrode side, the presence of a catalyst of the electrode catalyst layer 1 in _O, immediately react to form water and generate oxygen ions from oxygen in the feed air. The supply air containing the generated water and unused oxygen is discharged from the outlet on the oxygen electrode side of the fuel cell FC as exhaust air (the exhaust air contains a large amount of moisture). On the hydrogen electrode side, electrons e ⁻ are generated when hydrogen is ionized, and the generated electrons e ⁻ reach the oxygen electrode side via an external load such as a motor (FIG. 1). Arrow)).
Hundreds of such fuel cell single cells CE are stacked and used as a fuel cell, for example, mounted on a vehicle or the like.
[0008]
[Problems to be solved by the invention]
Conventionally, in the fuel cell unit CE having such a configuration, the electrode catalyst layer 1 is formed by attaching the electrode catalyst layer 1 to the electrolytic film M and then performing thermocompression bonding using a hot press or the like. However, the electrode catalyst layer 1 formed by such a method has a bite due to the unevenness of the electrode catalyst layer C1 at the interface between the electrode catalyst layer 1 and the electrolytic film M, but the bonding interface is almost flat.
Therefore, for example, when a fuel cell is used by being mounted on a vehicle or the like, the fuel cell has a temperature cycle of about 85 ° C. or more from the outside temperature (the temperature below the freezing point in winter) to the time when the vehicle is running. In a high-temperature environment such as operating at a high temperature, the adhesive strength may not be sufficient, and a peeling phenomenon may occur. There was room for improvement in terms of gender.
[0009]
Accordingly, an object of the present invention is to provide a fuel cell electrode structure which prevents separation at the interface between the electrolyte membrane M and the electrode catalyst layer 1 and has high durability even at a temperature cycle of about 85 ° C. or more from below freezing. It is to be.
Another object of the present invention is to provide a method for manufacturing a fuel cell electrode structure that efficiently manufactures such a highly durable fuel cell electrode structure.
[0010]
[Means for Solving the Problems]
The present inventors have conducted intensive studies in view of the state of the prior art, and as a result, have been formed of a pair of electrode catalyst layers and an electrolytic membrane sandwiched between those electrode catalyst layers, at least one surface of the electrode catalyst layer The inventors have found that the above problem can be solved by a catalyst penetrating into the electrolytic membrane to integrally form the electrode catalyst layer and the electrolytic membrane, and have completed the present invention.
[0011]
That is, the present invention comprises a pair of electrode catalyst layers and an electrolytic film sandwiched between the electrode catalyst layers, and the catalyst of the electrode catalyst layer on at least one surface has a penetration depth of 5 μm to 20 μm into the electrolytic film. An electrode structure for a fuel cell in which the electrode catalyst layer and the electrolyte membrane are integrally formed by penetrating inside ,
After dissolving the catalyst in a polar solvent, it is dispersed in an ion-conducting polymer solution to prepare a slurry having a viscosity of 5,000 to 25,000 mPa · S,
After directly applying the slurry prepared in this manner to at least one surface of the electrolytic membrane, with the solvent remaining in the slurry, a pressure condition of 1.5 to 2.5 MPa, a temperature of 120 to 180 ° C. and pressed at the time the conditions of temperature and 30 to 60 seconds, which pre Symbol electrode catalyst layer by entering the pre-Symbol electrolyte membrane a part of the catalyst is characterized in that it has the electrolyte membrane and integrally formed (Claim 1). With this configuration, when the electrode catalyst layer is formed, the composition of the electrode catalyst layer and the electrolytic film is continuously changed at the boundary between the two, and the electrode catalyst layer and the electrolytic film are integrally formed. No separation occurs at the interface of the electrode structure, and the durability of the electrode structure can be increased even at a predetermined temperature cycle. Incidentally, the polar solvent has a property of dissolving the electrolytic membrane. In this configuration, in addition to the catalyst entering the electrolyte membrane, the electrode conductive layer is formed by depositing the ion-conductive polymer and the catalyst on the electrolyte membrane.
[0012]
Further, according to the present invention, in the fuel cell electrode structure, the ion exchange capacity of the electrolytic membrane is A, the ion exchange capacity of the formed electrode catalyst layer is B, and the electrolytic membrane before hot pressing is formed. The thickness is C (μm), and the thickness of a portion of the electrolyte membrane after the hot pressing where the catalyst has not penetrated is D (μm), and the following formula (1):
(AB) / (CD) (1)
It is preferable that the ion exchange density gradient coefficient at the interface between the electrode catalyst layer and the electrolytic membrane calculated in (1) is 3.5 × 10 ³ meq / g / cm or less (claim 2).
By thus defining the integral part of the electrode catalyst layer and the electrolytic membrane, the durability can be further ensured.
[0014]
Method for producing a conductive electrode structure of the present invention is composed of an electrolyte membrane sandwiched between a pair of electrode catalyst layers and their electrode catalyst layer, the catalyst of the electrode catalyst layer of at least one surface of deep penetration into the electrolyte membrane A method for producing an electrode structure for a fuel cell, wherein the electrode catalyst layer and the electrolyte membrane are integrally formed by penetrating within a range of 5 μm to 20 μm ,
After dissolving the catalyst constituting the electrode catalyst layer in a polar solvent, the slurry is dispersed in an ion-conducting polymer solution to prepare a slurry having a viscosity of 5,000 to 25,000 mPa · S,
After directly applying the slurry prepared in this way to at least one surface of the electrolytic membrane, with the solvent remaining in the slurry, a pressure condition of 1.5 to 2.5 MPa, a temperature of 120 to 180 ° C. Hot pressing under conditions and a time period of 30 to 60 seconds to cause a part of the catalyst to penetrate into the electrolyte membrane to form an electrode catalyst layer integrally with the electrolyte membrane (claim 3 ). ).
With this configuration, it is possible to easily and reliably manufacture an electrode structure having excellent durability.
[0015]
Further, it is preferable that the catalyst particles enter the electrolyte membrane by hot pressing while the polar solvent in the slurry directly applied to the electrolyte membrane in an amount of 20 mg / cm ^{2 to} 100 mg / cm ² remains ( Claim 4 ).
With this configuration, it is possible to easily and surely manufacture an electrode structure having more excellent durability.
[0016]
BEST MODE FOR CARRYING OUT THE INVENTION
Hereinafter, embodiments of the present invention will be described in detail with reference to the accompanying drawings, but the present invention is not limited to these embodiments.
FIG. 1 is a schematic view schematically showing a fuel cell unit cell to which the present invention is applied, and FIG. 2 is a cross-sectional view of a fuel cell electrode structure (hereinafter, referred to as “electrode structure”) of the present invention. , FIG. 3 is a schematic diagram showing the configuration of the catalyst particles, and FIG. 4 is a schematic diagram showing the manner of manufacturing the electrode structure of the present invention.
[0017]
[Configuration of electrode structure (single cell of fuel cell)]
As shown in FIG. 1, the electrode structure MEA of one embodiment mainly includes an electrolytic film M and an electrode catalyst layer 1 stacked on both sides of the electrolytic film M, and the electrode structure MEA thus configured. The diffusion layer 2 and the separator 3 are stacked on both sides of the fuel cell unit to constitute a fuel cell single cell CE. A large number of such fuel cell single cells CE are stacked to form a fuel cell.
[0018]
As the electrolyte membrane M of the electrode structure MEA, for example, a perfluorocarbon sulfonic acid membrane which is a proton (ion) exchange membrane is generally used. As described above, the electrolyte membrane M has a large number of proton exchange groups in the solid polymer, exhibits a low specific resistance of 20 Ω / cm proton or less at room temperature by being saturated with water, and functions as a proton conductive electrolyte. is there. The electrolyte membrane M that can be used in the present invention is not limited to this, as long as it is used in the fuel cell unit cell CE.
[0019]
In addition, the electrode catalyst layer 1 in the electrode structure MEA according to the embodiment is configured by dispersing catalyst particles (see FIG. 3) composed of a carrier in which a catalyst metal is supported on an ionic (proton) conductive resin. ing.
At this time, a platinum group metal, generally platinum, is usually supported on carbon as a carrier and formed as a catalyst metal. However, the present invention is not limited to these as long as it can be used as a catalyst for a fuel cell.
In addition, a base layer (not shown) may be provided between the diffusion layer 2 and the separator 3 for the purpose of enhancing the water repellency and the water storage effect, or for preventing the electrode catalyst layer 2 from biting into the diffusion layer 3. The underlayer is composed of a carbon black powder and a Teflon powder or a carbon black powder and an electrolyte solution.
[0020]
The electrode structure MEA is characterized in that, as shown in FIG. 2, a part of the catalyst particles in the electrode catalyst layer 1 has a configuration in which the catalyst particles penetrate a predetermined distance on both sides of the electrolytic film M. That is, instead of having a clear interface between the electrolytic membrane and the electrode catalyst layer as in a conventional electrode structure, a catalyst (a material constituting the electrode catalyst layer 1) is applied to a part of the electrolytic membrane M by a predetermined amount. The electrolyte membrane M and the electrode catalyst layer 1 are integrally formed.
At this time, the degree of penetration of the catalyst (catalyst particles) into the electrolytic membrane M is determined by setting the ion exchange capacity of the electrolytic membrane M to A and the ion exchange capacity of the electrode catalyst layer 1 to B (the ion exchange capacity is the electrolytic membrane M). M), the thickness of the electrolyte membrane before heating under pressure is defined as C (μm), and the distance between the permeated catalyst particles from both sides is defined as Dw (μm). The following equation (1):
(AB) / (C-Dw) / 2 (1)
Can be expressed as an ion exchange density gradient coefficient at the interface between the electrode catalyst layer 1 and the electrolytic membrane M calculated by Note that the distance Dw is the thickness of a portion of the electrolyte membrane M where the catalyst particles have not penetrated.
[0021]
That is, when the electrode catalyst layer 1 penetrates into the electrolytic membrane M by the length (C−Dw) / 2, it is shown as an increment of the ion exchange capacity per unit length.
In the present invention, it has been experimentally found that such an ion exchange density gradient coefficient is preferably 3.5 × 10 ³ meq / g / cm or less. That is, when the ion exchange density gradient coefficient exceeds 3.5 × 10 ³ meq / g / cm, the integral formation of the electrode catalyst layer 1 and the electrolytic membrane M is insufficient (that is, both 1 and M are completely mixed). The portion (gradation portion) formed integrally is small), which is not preferable from the viewpoint of preventing separation of the electrode catalyst layer 1 and the electrolytic film M.
[0022]
Another measure for determining the degree of penetration of the electrode catalyst layer 1 into the electrolyte membrane M is the depth of penetration of catalyst particles into the electrolyte membrane (that is, (C−Dw) / 2 itself). It is preferable that the depth of penetration into the electrolytic film M is in the range of 5 μm to 20 μm. If the penetration of the catalyst particles into the electrolyte membrane M is too shallow, it is not preferable from the viewpoint of preventing the electrode catalyst layer 1 and the electrolyte membrane M from peeling off. On the other hand, if the penetration is too deep, the performance of the electrolytic film M is reduced.
[0023]
In the present invention, in order to achieve such a structure, the electrode catalyst layer 1 is formed by directly applying an electrode catalyst layer slurry composed of catalyst particles and an ion-conductive polymer electrolyte membrane to the electrolyte membrane. Thereafter, heating is performed under pressure to cause a part of the catalyst particles to penetrate into the electrolyte membrane to form an integral part with the electrolyte membrane.
That is, in the present invention, the electrode catalyst layer 1 is prepared by dissolving the catalyst particles in a polar solvent, and then preparing a slurry in which the slurry is dispersed in an ion-conductive polymer solution. Apply directly at a predetermined thickness. Next, heating is performed under pressure to cause a part of the catalyst particles to penetrate into the electrolyte membrane to form the electrode catalyst layer 1 and the electrolyte membrane M integrally.
[0024]
The solvent used at this time is used to allow the catalyst particles in the slurry to enter the electrolytic membrane M, and a polar solvent soluble in the electrolytic membrane M is used. The polar solvent that can be used in the present invention is not particularly limited as long as the electrolyte membrane M and the electrode catalyst layer 1 can be integrally formed. For example, dimethylacetamide (boiling point: 165.5 ° C.), dimethylformamide (boiling point: 153 ° C.) Dimethyl sulfoxide (boiling point: 189 ° C.), triethyl phosphate (boiling point: 115 ° C.), N-methylpyrrolidone (boiling point: 202 ° C.), and the like, and these can be used alone or as a mixture of two or more.
The polymer ion exchange component is not particularly limited as long as it is conventionally used in fuel cells.For example, polyether ether ketone, polyether sulfone, polysulfone, polyetherimide, polyphenylene sulfide, Examples thereof include polyphenylene oxide, which can be used alone or as a mixture of two or more.
[0025]
In the present invention, when the slurry is applied, the slurry may be applied to one surface of the electrolytic film M, heated under pressure (hot pressing), and integrally laminated one by one. Since the structure MEA may be bent due to thermal strain or the like, it is preferable to apply slurry to both surfaces of the electrolytic film M and integrally mold the electrolytic film M and the electrode catalyst layer 1.
The pressurizing pressure, the heating temperature, and the hot pressing time at this time are appropriately selected depending on the solvent to be used, the viscosity of the slurry, and the like. Typically, the pressure is 1.5 to 2.5 MPa (15 to 25 kgf / cm ² ). And hot pressing at a temperature of 120 to 180 ° C. for 30 to 60 seconds.
At this time, when the solvent is allowed to remain in an amount of 20 mg / cm ² or more, it becomes possible to dissolve the surface of the electrolytic film M with the remaining solvent in the slurry at the time of hot pressing in combination with the above conditions, Of the catalyst into the electrolytic membrane M, and the catalyst can be pushed into a certain depth.
[0026]
The viscosity of the slurry at this time is not particularly limited as long as the operation of directly applying the slurry to the electrolytic membrane M can be performed and the predetermined electrode catalyst layer 1 defined in the present invention can be formed. , Preferably in the range of 5,000 to 25,000 mPa · s. That is, if the slurry viscosity is less than 5,000 mPa · sec, there is a possibility that the slurry will leak when hot-pressed, and if the slurry viscosity exceeds 25,000 mPa · sec, the slurry may be difficult to handle. is there.
[0027]
As described above, in the present invention, the pressure-bonding strength at the interface between the electrolytic film M and the electrode catalyst layer 1 is increased by integrally molding with the electrolytic layer M in the electrode structure MEA. It becomes possible to prevent peeling and cold peeling due to temperature cycling.
[0028]
(Manufacture of electrode structure)
Hereinafter, a method for manufacturing the electrode structure MEA in which the electrolytic membrane M and the electrode catalyst layer 1 of one embodiment are integrally formed will be described with reference to FIG.
In producing the electrode structure MEA, first, the catalyst particles are dissolved in a polar solvent in which the electrolyte membrane M is soluble, and then dispersed in an ion-conductive polymer solution to have a viscosity of 5,000 to 25,000 mPa · sec. A slurry is formed so that
Next, a predetermined amount of the slurry thus prepared is directly applied to the electrolytic film M as shown in FIG.
If necessary, a slurry for forming an underlayer composed of a carbon black powder and a Teflon powder or a carbon black powder and an electrolyte solution (an ion-conductive polymer solution) is overlaid on the slurry for forming an electrode catalyst layer. To form an underlayer.
[0029]
FIGS. 4B to 4E are cross-sectional views in which a part of FIG. 4A is enlarged, and show how the catalyst layer 1 is integrally formed with the electrolytic membrane M according to the present invention. .
As shown in FIG. 4 (b), first, a polar solvent that is soluble in the applied electrolyte catalyst slurry in the electrode catalyst forming slurry starts to dissolve the electrolyte membrane M.
Next, as shown in FIG. 4C, the polar solvent dissolves a part of the electrolyte membrane.
Then, as shown in FIG. 4D, when hot pressing is performed from above the slurry for forming the electrode catalyst, the catalyst particles Cat enter the portion where the polar solvent is dissolved in the electrolytic membrane. At this time, it is preferable to perform hot pressing in a state where the polar solvent (organic solvent) is left in an amount of 20 mg / cm ² or more.
When the temperature and the pressure are released after performing the hot pressing in this way, an electrode structure MEA in which the electrolytic film M and the electrode catalyst layer 1 are integrally formed is formed as shown in FIG.
Thus, it becomes possible to manufacture the desired highly durable electrode structure MEA by a simple process. In the present invention, the electrode catalyst layer 1 is formed so as to be overlaid on the electrolytic film M, but the boundary between the two (the electrolytic film M and the electrode catalyst layer 1) is completely integrated.
[0030]
【Example】
Hereinafter, the present invention will be described in detail based on examples, but the present invention is not limited to the following examples.
[Example 1]
A polar solvent-soluble electrolyte component (PE; ion conductive polymer material) is mixed with the catalyst particles (Cat) at a ratio of PE / Cat = 0.4 with respect to the catalyst particles (Cat), and the solvent (N-methylpyrrolidone) ) Was added so as to have a viscosity of 5,000 mPa · s to prepare a slurry. The slurry thus prepared is dried until the remaining amount of the polar solvent (remaining solvent amount) becomes 100 mg / cm ^2, and then hot pressed to integrally form the electrode catalyst layer 1 and the electrolytic film M. Thus, an electrode structure MEA of the present invention was obtained. Table 1, FIG. 5 and FIG. 6 show the physical properties of the obtained electrode structure MEA.
In Table 1, the penetration depth of the catalyst was determined by actual measurement with a scanning electron microscope (SEM), and the gradient density was similarly determined by calculating the average distance between the catalysts (catalyst particles) penetrating from both sides. ) Expression.
The thermal peeling rate was determined by repeating a cold environment and a hot environment at −40 ° C. for 30 minutes and 90 ° C. for 30 minutes for 100 cycles, and image-processed the surface peeling state. Numerical values are obtained by converting the peeled area in the unit observation area. The cross leak amount (gas permeability cc / cm ² · min) is determined by assembling the sample into a single cell of the fuel cell, and then submerging the sample gas. The amount of sample gas supplied from the supply port and discharged from the gas discharge port through the membrane sample was measured and obtained.
[0031]
[Examples 2 to 9 and Comparative Example 1]
Example 1 was repeated except that the viscosity of the slurry and the amount of the remaining solvent were changed as shown in Table 1. The results are shown in Table 1, FIG. 5 and FIG.
[0032]
[Table 1]

[0033]
As shown in Table 1 and FIG. 5, the electrode structure MEA in which the electrode catalyst layer 1 and the electrolytic film M were integrally formed exhibited a good thermal exfoliation rate and a good cross leak rate (gas permeability cc / cm ² · min). In particular, it is found that the catalyst particles having a penetration depth of 5 to 20 μm (density gradient coefficient 859.0 to 3436.00) are particularly preferable. On the other hand, in Comparative Example 1 in which the electrode catalyst layer and the electrolyte membrane were not integrally formed, it can be seen that the thermal delamination rate was extremely poor.
By the way, it can be seen that when the penetration depth is small, the density gradient coefficient tends to increase, and the thermal delamination rate tends to increase. Conversely, it can be seen that when the penetration depth is large, the density gradient coefficient tends to decrease, and the thermal delamination rate tends to decrease. In addition, it can be seen that the lower the viscosity of the slurry, the better the depth of penetration of the catalyst. At the same time, it can be seen that in order to increase the depth of penetration of the catalyst, it is better to have more residual solvent.
In addition, as shown in FIG. 6, it can be seen that the electrode structure MEA of the present invention has a high terminal voltage in all the current density ranges measured as compared with the electrode structure of Comparative Example 1. Therefore, the electrode structure MEA of the present invention not only has excellent durability compared with the conventional electrode structure, but also can supply higher power.
[0034]
【The invention's effect】
As described above, in the electrode structure of the present invention , the penetration depth of the catalyst particles into the electrolyte membrane can be in the range of 5 μm to 20 μm, and when the electrode catalyst layer is formed, The composition of the electrolyte membrane and the electrolyte film is continuously changed at the interface between them, and the electrolyte membrane is integrally formed. Therefore, separation does not occur at the interface between the electrolytic membrane and the electrode catalyst layer, and the durability of the electrode structure can be increased even in a predetermined temperature cycle (claim 1). The fuel cell unit cell including the electrode structure in which the electrolyte membrane and the electrode catalyst layer are integrally formed does not cause separation at the interface between the electrolyte membrane and the electrode catalyst layer in the electrode structure, thereby improving the durability of the entire fuel cell. It is possible to do. In addition, this fuel cell can obtain a higher output than that of the prior art. Further, when the ion exchange density gradient coefficient at the interface between the electrode catalyst layer and the electrolytic membrane is 3.5 × 10 ³ meq / g / cm or less, higher durability can be obtained (Claim 2) .
Excellent electrode structure as this is, after dissolving the catalyst particles constituting the electrode catalyst layer in a polar solvent, is dispersed in ion-conducting polymer solution viscosity 5,000～25,000MPa · sec slurry Is prepared, and the slurry thus prepared is directly applied to the electrolyte membrane, and hot-pressed under a pressure condition of 1.5 to 2.5 MPa, a temperature condition of 120 to 180 ° C., and a time condition of 30 to 60 seconds. The electrode catalyst layer can be easily manufactured by forming the electrode catalyst layer integrally with the electrolyte membrane by infiltrating the catalyst into the electrolyte membrane (claim 3 ). Further, when the hot-pressed catalyst particles to penetrate into the electrolyte membrane in a state in which the organic solvent of the catalyst particle dispersed ion conducting polymer that is applied directly to the electrolyte membrane remained in an amount of 20mg / cm ² ~100mg / cm ² Furthermore, it is possible to easily and reliably manufacture an electrode structure having excellent durability (claim 4 ).
[Brief description of the drawings]
FIG. 1 is a schematic diagram showing an outline of a single fuel cell to which the present invention is applied.
FIG. 2 is a cross-sectional view of an electrode structure (electrode structure for a fuel cell) of the present invention. FIG. 3 is a schematic view showing a configuration of catalyst particles.
FIG. 4 is a schematic view showing a state of manufacturing the electrode structure of the present invention.
FIG. 5 is a graph showing the relationship between the penetration depth of an electrode catalyst layer, gas permeability, and the thermal delamination rate in the present invention and a comparative example.
FIG. 6 is a graph showing a relationship between a current density and a terminal voltage in the present invention and a comparative example.
[Explanation of symbols]
FC fuel cell MEA electrode structure (electrode structure for fuel cell)
M electrolyte membrane 1 electrode catalyst layer 2 diffusion layer 3 separator 4 flow path

Claims (4)

It is composed of a pair of electrode catalyst layers and an electrolytic film sandwiched between the electrode catalyst layers, and the catalyst of the electrode catalyst layer on at least one surface penetrates into the electrolytic film at a depth of 5 μm to 20 μm in the range of 5 μm to 20 μm. An electrode structure for a fuel cell in which an electrode catalyst layer and the electrolyte membrane are integrally formed,
After dissolving the catalyst in a polar solvent, it is dispersed in an ion-conducting polymer solution to prepare a slurry having a viscosity of 5,000 to 25,000 mPa · S,
After directly applying the slurry prepared in this manner to at least one surface of the electrolytic membrane, with the solvent remaining in the slurry, a pressure condition of 1.5 to 2.5 MPa, a temperature of 120 to 180 ° C. and pressed at the time the conditions of temperature and 30 to 60 seconds, a fuel cell, characterized in that the by entering the pre-Symbol electrolyte membrane part electrode catalyst layer of the catalyst was the electrolyte membrane and integrally formed Electrode structure. The ion exchange capacity of the electrolytic membrane is A, the ion exchange capacity of the formed electrode catalyst layer is B, the thickness of the electrolytic membrane before the hot pressing is C (μm), and the thickness after the hot pressing is The thickness of a portion of the electrolyte membrane where the catalyst has not penetrated is represented by the following formula (1) as D (μm):
(AB) / (CD) (1)
2. The fuel cell according to claim 1, wherein the ion exchange density gradient coefficient at the interface between the electrode catalyst layer and the electrolyte membrane, calculated by the following, is 3.5 × 10 ³ meq / g / cm or less. Electrode structure. It is composed of a pair of electrode catalyst layers and an electrolytic film sandwiched between the electrode catalyst layers, and the catalyst of the electrode catalyst layer on at least one surface penetrates into the electrolytic film at a depth of 5 μm to 20 μm in the range of 5 μm to 20 μm. A method for producing a fuel cell electrode structure in which an electrode catalyst layer and the electrolyte membrane are integrally formed,
After dissolving the catalyst constituting the electrode catalyst layer in a polar solvent, the slurry is dispersed in an ion-conducting polymer solution to prepare a slurry having a viscosity of 5,000 to 25,000 mPa · S,
After directly applying the slurry prepared in this way to at least one surface of the electrolytic membrane, with the solvent remaining in the slurry, a pressure condition of 1.5 to 2.5 MPa, a temperature of 120 to 180 ° C. Hot pressing under conditions and a time condition of 30 to 60 seconds to allow a part of the catalyst to penetrate into the electrolytic membrane to form an electrode catalyst layer integrally with the electrolytic membrane. The method of manufacturing the structure. To claim 3, characterized in that to penetrate the polar solvent of the slurry was applied directly to the electrolyte membrane by hot pressing while remaining in an amount of ^{20mg / cm 2 ~100 mg / cm} 2 to the electrolyte membrane The manufacturing method of the fuel cell electrode structure according to the above.

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