Carbon black, electrode catalyst and fuel cell using same, and method for producing carbon black
US-2019030514-A1 · Jan 31, 2019 · US
US11394034B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11394034-B2 |
| Application number | US-201816626724-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 29, 2018 |
| Priority date | Jun 29, 2017 |
| Publication date | Jul 19, 2022 |
| Grant date | Jul 19, 2022 |
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A support for a polymer electrolyte fuel cell catalyst satisfying the following requirements (A), (B), (C), and (D), and a producing method thereof, as well as a catalyst layer for a polymer electrolyte fuel cell and a fuel cell: (A) a specific surface area according to a BET analysis of a nitrogen adsorption isotherm is from 450 to 1500 m 2 /g. (B) a nitrogen adsorption and desorption isotherm forms a hysteresis loop in a range of relative pressure P/P 0 of more than 0.47 but not more than 0.90, and a hysteresis loop area ΔS 0.47-0.9 is from 1 to 35 mL/g; (C) a relative pressure P close /P 0 at which the hysteresis loop closes is more than 0.47 but not more than 0.70; and (D) a half-width of a G band detected by Raman spectrometry in a range of from 1500 to 1700 cm −1 is from 45 to 75 cm −1 .
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The invention claimed is: 1. A support for a polymer electrolyte fuel cell catalyst, comprising a carbon material, and satisfying the following requirements (A), (B), (C), and (D): (A) a specific surface area according to a BET analysis of a nitrogen adsorption isotherm is from 450 to 1500 m 2 /g; (B) a nitrogen adsorption and desorption isotherm forms a hysteresis loop in a range of relative pressure P/P 0 of more than 0.47 but not more than 0.90, and a hysteresis loop area ΔS 0.47-0.9 is from 5 to 35 mL/g; (C) a relative pressure P close /P 0 at which the hysteresis loop closes is more than 0.47 but not more than 0.70; and (D) a half-width of a G band detected by Raman spectrometry in a range of from 1500 to 1700 cm −1 is from 45 to 75 cm −1 . 2. The support for a polymer electrolyte fuel cell catalyst according to claim 1 , further satisfying the following requirement (E): (E) an adsorption volume V 0.2-0.9 measured from the nitrogen adsorption isotherm in a relative pressure range of from 0.20 to 0.90 is from 150 to 700 mL/g. 3. The support for a polymer electrolyte fuel cell catalyst according to claim 1 , wherein the hysteresis loop area ΔS 0.47-0.9 is from 15 to 35 mL/g. 4. The support for a polymer electrolyte fuel cell catalyst according to claim 1 , wherein the relative pressure P close /P 0 at which the hysteresis loop closes is from 0.50 to 0.70. 5. A method of producing a support for a polymer electrolyte fuel cell catalyst according to claim 1 , the method comprising: a support step of supporting an activation catalyst, which promotes an activation reaction on a porous carbon material, in pores in the porous carbon material, to produce a carbon material supporting the activation catalyst; and a first heat treatment step of heat-treating the carbon material supporting the activation catalyst in an oxygen-containing atmosphere in a range of from 300° C. to 700° C. 6. The method of producing a support for a polymer electrolyte fuel cell catalyst according to claim 5 , further comprising a second heat treatment step of heating the carbon material supporting the activation catalyst in a vacuum or in an inert gas atmosphere in a range of from 1600 to 2100° C., the second heat treatment step being performed at least one of before or after the first heat treatment step. 7. The method of producing a support for a polymer electrolyte fuel cell catalyst according to claim 5 , wherein: in the supporting step, in a case in which a particle diameter of the activation catalyst is from 2 to 7 nm, and the activation catalyst is a noble metal element, a support rate of the activation catalyst is from 3 to 20% by mass, and in a case in which the activation catalyst is a 3d element, a support rate of the activation catalyst is from 3 to 9% by mass; and in the first heat treatment step, an oxygen concentration of the oxygen-containing atmosphere is from 5 to 100% by volume with respect to a total volume of atmosphere gas, and a heat treatment time is from 20 min to 20 hours. 8. The method of producing a support for a polymer electrolyte fuel cell catalyst according to claim 5 , further comprising an activation catalyst removal step of removing the activation catalyst that is performed after the first heat treatment step. 9. A catalyst layer for a polymer electrolyte fuel cell comprising the support for a polymer electrolyte fuel cell catalyst according to claim 1 . 10. A fuel cell, comprising the catalyst layer for a polymer electrolyte fuel cell according to claim 9 . 11. The fuel cell according to claim 10 , wherein the catalyst layer for a polymer electrolyte fuel cell is a catalyst layer on a cathode side. 12. A support for a polymer electrolyte fuel cell catalyst, comprising a carbon material, and satisfying the following requirements (A), (B), (C), and (D): (A) a specific surface area according to a BET analysis of a nitrogen adsorption isotherm is from 450 to 1500 m 2 /g; (B) a nitrogen adsorption and desorption isotherm forms a hysteresis loop in a range of relative pressure P/P 0 of more than 0.47 but not more than 0.90, and a hysteresis loop area ΔS 0.47-0.9 is from 1 to 35 mL/g; (C) a relative pressure P close /P 0 at which the hysteresis loop closes is from 0.50 to 0.70; and (D) a half-width of a G band detected by Raman spectrometry in a range of from 1500 to 1700 cm −1 is from 45 to 75 cm −1 .
characterised by gaseous activating agents · CPC title
Fuel cells with solid electrolytes · CPC title
Positive electrodes · CPC title
Inert electrodes with catalytic activity, e.g. for fuel cells · CPC title
on carbon or graphite · CPC title
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