Support for polymer electrolyte fuel cell catalyst, method of producing support for polymer electrolyte fuel cell catalyst, catalyst layer for polymer electrolyte fuel cell, and fuel cell

US11394034B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-11394034-B2
Application numberUS-201816626724-A
CountryUS
Kind codeB2
Filing dateJun 29, 2018
Priority dateJun 29, 2017
Publication dateJul 19, 2022
Grant dateJul 19, 2022

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  1. Title

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  2. Abstract

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  5. First independent claim

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Abstract

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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 .

First claim

Opening claim text (preview).

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 .

Assignees

Inventors

Classifications

  • 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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What does patent US11394034B2 cover?
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 desorpt…
Who is the assignee on this patent?
Nippon Steel Chemical & Mat Co Ltd
What technology area does this patent fall under?
Primary CPC classification H01M4/9083. Mapped technology areas include Electricity.
When was this patent published?
Publication date Tue Jul 19 2022 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 5 related publications on this page (citations in our corpus or others sharing the same primary CPC).