Method of forming a fuel cell stack
US-9225027-B2 · Dec 29, 2015 · US
US9490488B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9490488-B2 |
| Application number | US-201214008238-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 29, 2012 |
| Priority date | Mar 29, 2011 |
| Publication date | Nov 8, 2016 |
| Grant date | Nov 8, 2016 |
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PBI-based MEAs for high temperature Polymer Electrolyte Membrane Fuel Cell (PEMFC) were prepared by direct hot pressing of catalyst layer on Teflon sheets on to both sides of phosphoric acid doped PBI membrane (decal transfer). These MEAs show two times higher performance compared to the MEAs prepared by normal brush coating method on GDL at an operating temperature of 160° C.
Opening claim text (preview).
We claim: 1. A process for the preparation of a membrane electrode assembly (MEA) comprising: a. hot pressing a poly benzimidazole membrane (PBI) doped with phosphoric acid at a temperature of 130° C., at a pressure of about 1.6 tons per square inch for 30 minutes; b. hot pressing the membrane as obtained in step (a) again with electrodes at a temperature of 130° C. at about 1.6 tons per square inch for a period of 15 minutes to obtain an electrolyte membrane; c. directly transferring a catalyst layer comprising Pt/carbon in the range of 0.15-0.3 mg/cm 2 from a nonporous support on to the electrolyte membrane as obtained in step (b) during hot pressing to obtain a membrane electrode assembly (MEA). 2. The process as claimed in claim 1 , wherein the non-porous support used in step (c) is selected from the group consisting of Teflon, a polyimide, a polystyrene, and nylon. 3. A process for the preparation of a membrane electrode assembly (MBA) comprising: a. hot pressing a poly benzimidazole membrane (PBI) doped with phosphoric acid at a temperature of 160° C., at a pressure of about 3.2 tons per square inch for 30 minutes; b. hot pressing the membrane as obtained in step (a) again with electrodes at a temperature of 160° C. at a pressure of about 3.2 tons per square inch for a period of 20 minutes to obtain an electrolyte membrane; c. directly transferring a catalyst layer comprising Pt/carbon in the range of 0.15-0.3 mg/cm 2 from a non-porous support on to the electrolyte membrane as obtained in step (b) during hot pressing to obtain a membrane electrode assembly (MEA). 4. The process as claimed in claim 3 , wherein the non-porous support used in step (c) is selected from the group consisting of Teflon, a polyimide, a polystyrene and nylon.
Means for holding the electrolyte (solid polymer electrolytes H01M8/1018) · CPC title
characterised by membrane-electrode assemblies [MEA] (H01M8/12 takes precedence) · CPC title
Temporary supports, e.g. decal · CPC title
Fuel cells with polymeric electrolytes · CPC title
on carbon or graphite · CPC title
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