Catalyst layer for gas diffusion electrode, method for manufacturing the same, membrane electrode assembly, and fuel cell
US-9799894-B2 · Oct 24, 2017 · US
US9692060B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9692060-B2 |
| Application number | US-201214119528-A |
| Country | US |
| Kind code | B2 |
| Filing date | May 21, 2012 |
| Priority date | May 23, 2011 |
| Publication date | Jun 27, 2017 |
| Grant date | Jun 27, 2017 |
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A particulate carbon catalyst in which particles having a particle diameter of 20 nm-1 μm account for a volume fraction of at least 45%, and the content of nitrogen atoms is 0.1-10 atomic % relative to the amount of carbon atoms.
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The invention claimed is: 1. A particulate carbon catalyst in which particles having a particle diameter of 20 nm or more and 1 μm or less account for a volume fraction of at least 55% and a content of nitrogen atoms relative to carbon atoms in the particulate carbon catalyst is 0.5 atomic % or more and 8 atomic % or less; wherein the particles contain metal atoms in amount of 0.0045 or more and 0.0430 or less in mass ratio relative to carbon atoms in the particulate carbon catalyst, wherein the metal atoms are at least one kind selected from the group consisting of iron, cobalt, nickel, copper, tin, manganese, and zinc atoms; wherein the particles are spherical; wherein the average value of the sphericity T defined by the following equation for randomly selected 10 or more particles is 0.80 or more and 0.95 or less: Sphericity T= 4 πS/L 2 wherein L is the circumferential length of the particle on a planar image of particles, S is the area of the particle on the image, and π is circumference ratio. 2. A method for producing the particulate carbon catalyst according to claim 1 , comprising carbonizing a particulate precursor composition containing nitrogen atoms and an organic polymer at 400 to 1500° C., wherein particles having a particle diameter of 20 nm or more and 1 μm or less account for a volume fraction of at least 55%, wherein the particulate precursor composition contains metal atoms, and wherein the metal atoms are at least one kind selected from the group consisting of iron, cobalt, nickel, copper, tin, manganese, and zinc atoms. 3. The method for producing the particulate carbon catalyst according to claim 2 , wherein the organic polymer contained in the particulate precursor composition is polyacrylonitrile and carbonization is performed after stabilizing the particulate precursor composition. 4. The method for producing the particulate carbon catalyst according to claim 2 , wherein the organic polymer contained in the particulate precursor composition is at least one kind selected from the group consisting of a polyamide, a polyamic acid, a polyimide, a polyamideimide, a polyimide ester, a polyamide ester, a polyazole, and a polybenzimidazopyrrolone. 5. The method for producing the particulate carbon catalyst according to claim 2 , wherein the particulate precursor composition comprises at least one kind of metal atom selected from the group consisting of iron, cobalt, nickel, and copper. 6. The method for producing the particulate carbon catalyst according to claim 2 , wherein the particulate precursor composition is spherical particles and the particulate carbon catalyst formed by carbonization is also spherical. 7. The method for producing the particulate carbon catalyst according to claim 6 , wherein the average value of the sphericity T defined by the following equation for randomly selected 10 or more particles from each of the particulate precursor composition and the particulate carbon catalyst is 0.80 or more and 0.95 or less: Sphericity T= 4 πS/L 2 wherein L is circumferential length of the particle on a planar image of particles, S is area of the particle on the image, and it is circumference ratio. 8. The method for producing the particulate carbon catalyst according to claim 2 , wherein the metal atoms are removed by further washing the particulate carbon catalyst after carbonization. 9. The method for producing the particulate carbon catalyst according to claim 8 , wherein the carbon catalyst is activated by further heating at 650 to 1500° C. under an atmosphere of at least one kind of gas selected from the group consisting of ammonia, hydrogen, water vapor and carbon dioxide, after removing the metal atoms by washing the particulate carbon catalyst. 10. A method of using a particulate carbon catalyst according to claim 1 , comprising conducting a reduction reaction of oxygen with the particulate carbon catalyst as an oxygen reduction reaction catalyst.
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