Solid polymer type fuel cell catalyst, solid polymer type fuel cell electrode, and fuel cell

1. A catalyst for a solid polymer membrane fuel cell which is comprised of a carbon material which carries a catalyst ingredient which has an oxygen reducing activity, said catalyst characterized in that said carbon material has an amount of adsorption of water vapor (V 10 ) at 25° C. and a relative humidity of 10% of 2 ml/g or less and in that said carbon material has an amount of adsorption of water vapor (V 90 ) at 25° C. and a relative humidity of 90% of 400 ml/g or more to 2000 mL/g or less.

2. A catalyst for a solid polymer membrane fuel cell as set forth in claim 1 , characterized in that said carbon material has a ratio V 10 /V 90 of an amount of adsorption of water vapor (V 10 ) at 25° C. and a relative humidity of 10% and an amount of adsorption of water vapor (V 90 ) at 25° C. and a relative humidity of 90% of 0.002 or less.

3. An electrode for a solid polymer membrane fuel cell characterized by including the catalyst as set forth in claim 1 .

4. A fuel cell which includes a pair of catalyst layers sandwiching a solid polymer proton conductive electrolytic membrane, said cell characterized in that at least the catalyst layer of the cathode includes a catalyst ingredient, electrolytic material, and carbon material

said carbon material includes at least two types of carbon materials, wherein one is a catalyst-carrying carbon material which carries said catalyst ingredient and the other one is a gas-diffusing carbon material which does not carry said catalyst ingredient,

and said catalyst-carrying carbon material includes at least two types of catalyst-carrying carbon materials which are catalyst-carrying carbon material A and catalyst-carrying carbon material B,

said catalyst-carrying carbon material A is a solid polymer type fuel cell catalyst as set forth in claim 1 , and

said catalyst-carrying carbon material B has a ratio X/S BET of 0.2 to 3.0, wherein X is a dibutyl phthalate oil absorption in ml/100 g and S BET is a specific surface area evaluated by the BET method.

5. A fuel cell including a pair of catalyst layers sandwiching a solid polymer proton conductive electrolytic membrane, in which fuel cell at least the catalyst layer of the cathode includes a catalyst ingredient, electrolytic material, and carbon material,

said carbon material includes at least two types of carbon materials, wherein one is a catalyst-carrying carbon material which carries said catalyst ingredient and the other one is a gas-diffusing carbon material which does not carry said catalyst ingredient,

said catalyst-carrying carbon material includes at least two types of catalyst-carrying carbon material which are catalyst-carrying carbon material A and catalyst-carrying carbon material B,

said catalyst-carrying carbon material A is a solid polymer type fuel cell catalyst as described in claim 1 ,

said catalyst-carrying carbon material B has a ratio X/S BET of 0.2 to 3.0, wherein X is a dibutyl phthalate oil absorption ml/100 g and S BET is a specific surface area evaluated by the BET method, and

said catalyst layer of the cathode is comprised of a two-phase mixed structure comprised of

a catalyst aggregation phase comprised of ingredients comprised of said catalyst-carrying carbon material and said electrolytic material aggregated together and

a gas-diffusing carbon material aggregation phase comprised of said gas-diffusing carbon material aggregated together.

6. A fuel cell including a pair of catalyst layers sandwiching a solid polymer proton conductive electrolytic membrane, in which fuel cell at least the catalyst layer of the cathode includes a catalyst ingredient, electrolytic material, and carbon material,

said carbon material includes at least three types of carbon materials which are a catalyst-carrying carbon material which carries said catalyst ingredient, a conductivity aid carbon material which does not carry said catalyst ingredient, and a gas-diffusing carbon material which does not carry said catalyst ingredient,

said catalyst-carrying carbon material includes at least two types of catalyst-carrying carbon material which are a catalyst-carrying carbon material A and catalyst-carrying carbon material B,

said catalyst-carrying carbon material A is a solid polymer type fuel cell catalyst as set forth in claim 1 ,

said catalyst-carrying carbon material B has a ratio X/S BET of 0.2 to 3.0, wherein X is a dibutyl phthalate oil absorption in ml/100 g and S BET is a specific surface area evaluated by BET of 0.2 to 3.0, and

said catalyst layer of the cathode has a structure which contains at least two layers of an inner layer on a side contiguous with said proton conductive electrolytic membrane and an outer layer on a side not contiguous with said proton conductive electrolytic membrane,

said inner layer is comprised of

an at least two-phase mixed structure of a catalyst aggregation phase A comprised of ingredients comprised of said catalyst-carrying carbon material A, said conductivity aid carbon material, and said electrolytic material agglomerated together and a gas-diffusing carbon material aggregation phase comprised of at least ingredients comprised of said gas-diffusing carbon material agglomerated together, and

said outer layer is comprised of

an at least two-phase mixed structure of a catalyst aggregation phase B comprised of at least ingredients comprised of said catalyst-carrying carbon material B and said electrolytic material and a gas-diffusing carbon material aggregation phase comprised of at least ingredients comprised of said gas-diffusing carbon material agglomerated together, and

said inner layer and said outer layer are structures wherein, in their layers, said catalyst aggregation phase A and said catalyst aggregation phase B are continuous and said gas-diffusing carbon material aggregation phase is dispersed in said catalyst aggregation phase A or B.

7. A fuel cell as set forth in claim 5 characterized in that said catalyst-carrying carbon material A further has a specific surface area S BET evaluated by BET of 1000 m 2 /g to 4000 m 2 /g and has a ratio S micro /S total of 0.5 or more, wherein S micro is the micropore surface area of diameter 2 nm or less by t-plot analysis and S total is the total surface area.

8. A fuel cell as set forth in claim 4 characterized in that a mass ratio A/(A+B) of said catalyst-carrying carbon material A and said catalyst-carrying carbon material B in said catalyst layer is 0.2 to 0.95.

9. A fuel cell as set forth in claim 6 characterized in that a mass ratio Y/(A+Y) of said conductivity aid carbon material Y and said catalyst-carrying carbon material A in said inner layer is 0.05 to 0.4.

10. A fuel cell as set forth in claim 6 characterized in that said conductivity aid carbon material in said inner layer has a ratio X/S BET of 0.2 to 3.0, wherein X is dibutyl phthalate oil absorption in ml/100 g and S BET is a specific surface area evaluated by BET.

11. A fuel cell as set forth in claim 6 characterized in that a content of said gas-diffusing carbon material in said inner layer is 3 mass % to 30 mass %.

12. A fuel cell as set forth in claim 6 , characterized in that a content of said gas-diffusing carbon material in said outer layer is 3 mass % to 30 mass %.