Electrolyte solution and method for producing same, continuously dissolving facility, electrolyte membrane, electrode catalyst layer, membrane electrode assembly and fuel cell
US-2016141696-A1 · May 19, 2016 · US
US2018248198A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2018248198-A1 |
| Application number | US-201715445194-A |
| Country | US |
| Kind code | A1 |
| Filing date | Feb 28, 2017 |
| Priority date | Feb 28, 2017 |
| Publication date | Aug 30, 2018 |
| Grant date | — |
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A membrane electrode assembly is provided that includes a polymer electrolyte membrane and a catalyst layer provided on a surface of the polymer electrolyte membrane. The catalyst layer comprises catalyst particles and an ionomer film surrounding each of the catalyst particles. The ionomer film has an oxygen permeability of approximately 6.0×1012 mol/cm/s to 15.0×1012 mol/cm/s at 80° C. and a relative humidity of approximately 30% to 100%.
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What is claimed is: 1 . A membrane electrode assembly comprising: a polymer electrolyte membrane; and a catalyst layer provided on a surface of the polymer electrolyte membrane, the catalyst layer comprising catalyst particles and an ionomer film surrounding each of the catalyst particles, and the ionomer film having an oxygen permeability of approximately 6.0×10 12 mol/cm/s to 15.0×10 12 mol/cm/s at 80° C. and a relative humidity of approximately 30% to 100%. 2 . The membrane electrode assembly according to claim 1 , wherein the catalyst particles comprise at least one selected from the group consisting of: ruthenium, rhodium, palladium, silver, osmium, iridium, platinum, gold and alloys thereof. 3 . The membrane electrode assembly according to claim 2 , wherein the catalyst particles comprise carbon supported platinum particles. 4 . The membrane electrode assembly according to claim 1 , wherein the ionomer comprises a fluoropolymer. 5 . The membrane electrode assembly according to claim 4 , wherein the fluoropolymer is perfluorosulfonic acid. 6 . The membrane electrode assembly according to claim 1 , wherein the catalyst layer has a porosity of 30 volume % to 40 volume % with respect to a total volume of the catalyst layer. 7 . The membrane electrode assembly according to claim 1 , further comprising a gas diffusion layer provided on a surface of the catalyst layer that is opposite the polymer electrolyte membrane. 8 . The membrane electrode assembly according to claim 1 , wherein the catalyst layer is a cathode side catalyst layer. 9 . A fuel cell comprising: the membrane electrode assembly according to claim 1 , an anode on a first side of the membrane electrode assembly; a cathode on a second side of the membrane electrode assembly; an anode gas diffusion layer on a side of the anode that is opposite the membrane electrode assembly; and a cathode gas diffusion layer on a side of the cathode that is opposite the membrane electrode assembly. 10 . The fuel cell according to claim 8 , wherein the catalyst layer is a cathode side catalyst layer. 11 . A method for producing a porous catalyst layer in a fuel cell, the method comprising: providing a catalyst composition on a substrate to form a catalyst layer on the substrate, the catalyst composition comprising catalyst particles and an ionomer film surrounding each of the catalyst particles; stretching the substrate together with the catalyst layer formed thereon to form a stretched substrate and a stretched catalyst layer; and transferring the stretched catalyst layer on the stretched substrate to one of a membrane and a gas diffusion layer. 12 . The method according to claim 11 , wherein transferring the stretched catalyst layer on the stretched substrate to the one of the membrane and the gas diffusion layer comprises attaching a second substrate to the stretched catalyst layer, removing the stretched substrate, attaching one of the membrane and the gas diffusion layer to the stretched catalyst layer and removing the second substrate. 13 . The method according to claim 11 , wherein the second substrate is a decal. 14 . The method according to claim 11 , wherein transferring the stretched catalyst layer on the stretched substrate to the one of the membrane and the gas diffusion layer comprises attaching the one of the membrane and the gas diffusion layer to the stretched catalyst layer and removing the stretched substrate. 15 . The method according to claim 11 , wherein the substrate with the catalyst layer formed thereon is stretched until the ionomer film has an oxygen permeability of approximately 6.0×10 12 mol/cm/s to 15.0×10 12 mol/cm/s at 80° C. and a relative humidity of approximately 30% to 100%. 16 . The method according to claim 11 , wherein the substrate is a hydrophobic substrate. 17 . The method according to claim 11 , wherein the substrate comprises polytetrafluoroethylene. 18 . A method for producing a porous catalyst layer in a fuel cell, the method comprising: providing a catalyst composition on one of a gas diffusion layer and a membrane layer to form a catalyst layer on the one of the gas diffusion layer and the membrane layer, the catalyst composition comprising catalyst particles and an ionomer film surrounding each of the catalyst particles; and stretching the one of the gas diffusion layer and the membrane layer together with the catalyst layer formed thereon. 19 . The method according to claim 18 , wherein the catalyst layer is formed on the membrane layer and the catalyst layer is stretched together with the membrane layer. 20 . The method according to claim 18 , further comprising, combining the membrane layer with a second membrane layer having a thickness greater than that of the membrane layer. 21 . The method according to claim 20 , wherein the membrane layer and the second membrane layer form a membrane, and the second membrane layer is closer than the membrane layer to an anode side of the membrane. 22 . The method according to claim 18 , wherein the one of the gas diffusion layer and the membrane layer with the catalyst layer formed thereon is stretched until the ionomer film has an oxygen permeability of approximately 6.0×10 12 mol/cm/s to 15.0×10 12 mol/cm/s at 80° C. and a relative humidity of approximately 30% to 100%.
comprising polyimides · CPC title
comprising halogenated polyolefins, e.g. PTFE · CPC title
Electrolytic membranes · CPC title
having nitrogen, e.g. sulfonated polybenzimidazoles [S-PBI], polybenzimidazoles with phosphoric acid, sulfonated polyamides [S-PA] or sulfonated polyphosphazenes [S-PPh] · CPC title
characterised by features of a layer formed of particles, e.g. chips, powder {or granules (layer formed of natural mineral particles B32B19/00; layer being formed of wood fibres, chips or particles B32B21/02)} · CPC title
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