Method and system for manufacturing membrane-electrode-gas diffusion layer assembly for fuel cell
US-2024136539-A1 · Apr 25, 2024 · US
US2017062836A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2017062836-A1 |
| Application number | US-201615350345-A |
| Country | US |
| Kind code | A1 |
| Filing date | Nov 14, 2016 |
| Priority date | Feb 12, 2009 |
| Publication date | Mar 2, 2017 |
| Grant date | — |
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A process for preparing gas diffusion substrate including a non-woven fibre web, thermally conductive materials and a carbonaceous residue, wherein the thermally conductive materials and carbonaceous residue are embedded within the non-woven fibre web and wherein the thermally conductive materials have a maximum dimension of between 1 and 100 μm and the gas diffusion substrate has a porosity of less than 80% is disclosed. The substrate has particular use in phosphoric acid fuel cells.
Opening claim text (preview).
1 . A process for preparing a gas diffusion substrate, said process comprising the steps of: (i) impregnating a non-woven fibre web with a mixture of a phenolic resin binder and thermally conductive materials selected from the group consisting of nanofibers, nanotubes and nanographene platelets, to give an impregnated web; (ii) curing the phenolic resin binder within the non-woven fibre web at a temperature of 100-250° C.; (iii) a first heat-treatment step of the impregnated web at 600-1000° C. to carbonize the phenolic resin binder to leave a carbonaceous residue; and (iv) a second heat-treatment step at 1800-3000° C. to provide the gas diffusion substrate. 2 . The process according to claim 1 , wherein the second heat-treatment step is at 2000-2300° C. 3 . The process according to claim 1 , wherein the first heat-treatment step is carried out in a non-oxidising gas atmosphere. 4 . The process according to claim 3 , wherein the non-oxidising gas atmosphere comprises nitrogen or carbon dioxide. 5 . The process according to claim 1 , wherein the gas diffusion substrate prepared by said process has a through-plane thermal conductivity of at least 3 W/m.K at a pressure of 1000 kPa. 6 . The process according to claim 1 , wherein before step (iii), two or more impregnated non-woven fiber webs are laminated. 7 . The process according to claim 6 , wherein the two or more impregnated non-woven fiber webs are laminated cross-plied. 8 . The process according to claim 6 , wherein the two or more impregnated non-woven fiber webs are laminated non-cross-plied. 9 . The process according to claim 6 , wherein the lamination is carried out at a temperature of between 150° C. and 160° C. 10 . The process according to claim 6 , wherein the laminated non-woven fiber webs have a thickness of 0.05 mm to 10 mm
Gas diffusion layers · CPC title
Inert electrodes with catalytic activity, e.g. for fuel cells · CPC title
Porous electrodes · CPC title
Phosphoric acid fuel cells [PAFC] · CPC title
Coated or impregnated woven, knit, or nonwoven fabric which is not [a] associated with another preformed layer or fiber layer or, [b] with respect to woven and knit, characterized, respectively, by a particular or differential weave or knit, wherein the coating or impregnation is neither a foamed material nor a free metal or alloy layer · CPC title
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