IP Library Granted Patent US 11,239,485
Granted Patent B2
US 11,239,485 · App. 16/810,282 · Granted Feb 1, 2022

Process

Inventors: Robert Jeffrey Coleman (Swindon, GB); Thomas Robertson Ralph (Swindon, GB); Sam Haig (Bramhall, GB); Natalia V. Plechkova (Belfast, GB)
Assignee: Johnson Matthey Fuel Cells Limited
H01M8/24C08J3/095C08J5/2237H01M8/008H01M8/1039H01M8/1069H01M8/1081C08J2300/30C08J2327/12Y02P70/50Y02W30/84
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Quick Facts
Patent No.
US 11,239,485
App. No.
16/810,282
Granted
Feb 1, 2022
Kind
B2
Abstract

A process for the recovery of a perfluorosulphonic acid ionomer from a component comprising a perfluorosulphonic acid ionomer is disclosed, the process comprising immersing the component comprising the perfluorosulphonic acid ionomer in a solvent comprising an aliphatic diol and heating. Also disclosed is the use of the recovered perfluorosulphonic acid ionomer, for example in to prepared a proton conducting membrane or a catalyst ink.

Claims (13)

1. A process for separating a membrane electrode assembly into components, said process comprising:

(i) immersing the membrane electrode assembly in a solvent comprising a C1-8 aliphatic diol compound, wherein said diol compound comprises at least one —CH 2 OH group; and

(ii) heating the membrane electrode assembly/solvent mix to a temperature of 90° C. to 150° C. to effect separation of the membrane electrode assembly components.

2. The process according to claim 1 , wherein the membrane electrode assembly is chopped or shredded prior to being immersed in the solvent.

3. The process according to claim 1 , said process comprising heating the membrane electrode assembly/solvent mix to a temperature of 90° C. to 120° C.

4. The process according to claim 1 , wherein the solvent further comprises a co-solvent.

5. A process for the recovery of one or more catalyst components from an original component selected from the group consisting of a perfluorosulphonic acid membrane, a catalyst coated membrane, an electrode and a membrane electrode assembly, said process comprising:

(i) immersing the original component in a solvent comprising a C1-8 aliphatic diol compound, wherein said diol compound comprises at least one —CH 2 OH group;

(ii) heating the component/solvent mix to a temperature of 90° C. to 150° C. to obtain a dispersion comprising solvent, one or more PFSA ionomers and the one or more catalyst components; and

(iii) filtering the dispersion to separate the solvent and the one or more PFSA ionomers from the one of more catalyst components.

6. The process according to claim 5 , wherein the original component is chopped or shredded prior to being immersed in the solvent.

7. The process according to claim 5 , said process comprising heating the component/solvent mix to a temperature of 90° C. to 120° C.

8. The process according to claim 5 , wherein the solvent further comprises a co-solvent.

Assignments (2)
CHANGE OF ADDRESS Recorded Jan 14, 2026
From: JOHNSON MATTHEY HYDROGEN TECHNOLOGIES LIMITED
To: JOHNSON MATTHEY HYDROGEN TECHNOLOGIES LIMITED
Reel/Frame 074818/0894 →
CHANGE OF NAME Recorded Jul 28, 2022
From: JOHNSON MATTHEY FUEL CELLS LIMITED
To: JOHNSON MATTHEY HYDROGEN TECHNOLOGIES LIMITED
Reel/Frame 060991/0106 →
Priority Claims (1)
GB 1505311 · Mar 27, 2015 · national
Continuity (2)
Continuation 15561728
Related Publication 20200203751A1 · Jun 25, 2020