Method for producing carrier for electrode catalyst, precursor of carrier for electrode catalyst, and carrier for electrode catalyst, comprising same
US-12057587-B2 · Aug 6, 2024 · US
US2018233758A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2018233758-A1 |
| Application number | US-201615751373-A |
| Country | US |
| Kind code | A1 |
| Filing date | Aug 10, 2016 |
| Priority date | Aug 12, 2015 |
| Publication date | Aug 16, 2018 |
| Grant date | — |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
The invention relates to a membrane electrode assembly ( 15 ) for a fuel cell ( 10 ), comprising a membrane ( 11 ) on each side of which is disposed a catalytic layer ( 12, 13 ), and on this a gas diffusion layer ( 30 ). It is provided that the gas diffusion layer ( 30 ) comprises a layer with electrically conductive particles ( 35 ), and a portion of the particles ( 35 ) is arranged directly adjacent to the catalytic layer ( 12, 13 ).
Opening claim text (preview).
1 . A membrane electrode assembly for a fuel cell, comprising: a membrane; a first catalytic layer positioned on a first surface of the membrane and a second catalytic layer positioned on a second surface of the membrane opposite to the first surface of the membrane; and a first gas diffusion layer positioned on the first catalytic layer and a second gas diffusion layer positioned on the second catalytic layer, wherein each of the first and second gas diffusion layers include electrically conductive particles, a portion of the particles of each of the first and second gas diffusion layers positioned immediately adjacent to the respective catalytic layer. 2 . The membrane electrode assembly according to claim 1 , wherein the electrically conductive particles have an average particle size in the range of 10 to 1000 μm. 3 . The membrane electrode assembly according to claim 1 , wherein the particles have different particle sizes, in particular with a variance in the range of 100 to 500 μm over the entire particle range. 4 . The membrane electrode assembly according to claim 1 , wherein the particles comprise at least two batches of particles, each batch of particles having a respective average particle size, and the at least two average particle sizes differ from one another by at least one error width. 5 . The membrane electrode assembly according to claim 3 , wherein the particles are arranged to have a gradient of the particle sizes which runs perpendicular to the first and second surfaces of the membrane. 6 . The membrane electrode assembly according to claim 3 , wherein the average particle size changes incrementally in a direction towards the catalytic layer. 7 . The membrane electrode assembly according to claim 3 , wherein the average particle size of the particles decreases in the direction towards the catalytic layer. 8 . The membrane electrode assembly according to claim 1 , wherein the particles include a graphite powder. 9 . The membrane electrode assembly according to claim 1 , wherein the gas diffusion layer has a cover layer on a surface facing away from the membrane. 10 . A fuel cell comprising a membrane electrode assembly including: a membrane; a first catalytic layer positioned on a first surface of the membrane and a second catalytic layer positioned on a second surface of the membrane opposite to the first surface of the membrane; and a first gas diffusion layer positioned on the first catalytic layer and a second gas diffusion layer positioned on the second catalytic layer, wherein each of the first and second gas diffusion layers include electrically conductive particles, a portion of the particles of each of the first and second gas diffusion layers positioned immediately adjacent to the respective catalytic layer. 11 . The fuel cell according to claim 10 , wherein the particles comprise at least two batches of particles, each batch of particles having a respective average particle size, and the at least two average particle sizes differ from one another by at least one error width. 12 . The fuel cell according to claim 10 , wherein the average particle size changes incrementally in a direction towards the catalytic layer. 13 . The fuel cell according to claim 10 , wherein the average particle size of the particles decreases in the direction towards the catalytic layer. 14 . The fuel cell according to claim 10 , wherein the particles include a graphite powder. 15 . The fuel cell according to claim 10 , wherein the gas diffusion layer has a cover layer on a surface facing away from the membrane. 16 . A method of fabricating a membrane electrode assembly for a fuel cell, comprising: positioning a first catalytic layer on a first surface of a membrane and a second catalytic layer on a second surface of the membrane opposite to the first surface of the membrane; and positioning a first gas diffusion layer on the first catalytic layer and a second gas diffusion layer on the second catalytic layer, wherein each of the first and second gas diffusion layers include electrically conductive particles, a portion of the particles of each of the first and second gas diffusion layers positioned immediately adjacent to the respective catalytic layer. 17 . The method according to claim 16 wherein the particles have an average particle size between 10 and 1000 μm. 18 . The method according to claim 16 wherein the particles have particle sizes that differ from one another by up to between 100 and 500 μm. 19 . The method according to claim 16 wherein the particles of the first gas diffusion layer are positioned so that a gradient exists in the size of the particles in a direction extending perpendicular to the first surface of the membrane.
Gas diffusion layers · CPC title
characterised by membrane-electrode assemblies [MEA] (H01M8/12 takes precedence) · CPC title
Carbonaceous material · CPC title
with solid or matrix-supported electrolytes · CPC title
Fuel cells with polymeric electrolytes · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.