US2005131116A1PendingUtilityA1
Process for dissolution of highly fluorinated ion-exchange polymers
Priority: Jul 12, 2002Filed: Feb 3, 2005Published: Jun 16, 2005
Est. expiryJul 12, 2022(expired)· nominal 20-yr term from priority
Inventors:Qun Sun
Y02E60/50Y02P70/50H01M 8/1023H01M 2300/0082C08J 3/095H01M 4/8668C08J 5/20H01M 8/1039H01M 8/1081
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Claims
Abstract
Highly fluorinated ion-exchange polymers achieve dissolution in aqueous tetrahydrofuran at lower pressures and temperatures than in other solvents, with few or no side products being formed.
Claims
exact text as granted — not AI-modified1 . A process for making a liquid composition of highly fluorinated ion-exchange polymer comprising
a) contacting the polymer with aqueous tetrahydrofuran, and b) heating said polymer in contact with aqueous tetrahydrofuran to form the liquid composition.
2 . The process of claim 1 wherein said aqueous tetrahydrofuran is comprised of water and tetrahydrofuran in a ratio of about 10:90 to about 90:10 weight %.
3 . The process of claim 1 wherein said aqueous tetrahydrofuran is comprised of water and tetrahydrofuran in a ratio of about 45:55 to about 55:45 weight %.
4 . The process of claim 1 wherein said aqueous tetrahydrofuran is comprised of less than about 50 weight % tetrahydrofuran.
5 . The process of claim 1 wherein the polymer comprises about 1 to about 15 weight % of the combined weight of polymer and water and tetrahydrofuran.
6 . The process of claim 1 wherein said polymer in contact with aqueous tetrahydrofuran is heated to a temperature of about 150° C. to about 300° C.
7 . The process of claim 1 wherein said polymer in contact with aqueous tetrahydrofuran is heated in a autoclave.
8 . The process of claim 1 wherein said highly fluorinated ion-exchange polymer is in the acid form, sodium ion form or potassium ion form, or a combination thereof.
9 . The process of claim 1 wherein said highly fluorinated ion-exchange polymer is in the acid form.
10 . The process of claim 1 wherein said ion-exchange polymer is perfluorinated.
11 . The process of claim 1 wherein said ion-exchange polymer has an ion-exchange ratio of about 3 to about 33.
12 . The process of claim 1 wherein said ion-exchange polymer has an ion-exchange ratio of about 8 to about 23.
13 . The process of claim 1 wherein said composition is substantially free of products from reactions of the solvent during preparation of said composition.
14 . A liquid composition consisting essentially of ion-exchange polymer in aqueous tetrahydrofuran, at least about 50% of the total number of halogen and hydrogen atoms in said ion-exchange polymer being fluorine atoms.
15 . The liquid composition of claim 14 wherein the aqueous tetrahydrofuran is from about 10:90 weight % water:tetrahydrofuran to about 90:10 weight % water:tetrahydrofuran.
16 . The liquid composition of claim 14 wherein the aqueous tetrahydrofuran is from about 45:55 weight % water:tetrahydrofuran to about 55:45 weight % water:tetrahydrofuran.
17 . The liquid composition of claim 14 wherein said ion-exchange polymer is in the acid form.
18 . The liquid composition of claim 14 wherein said ion-exchange polymer is about 1 to about 15 weight % of the combined weights of the polymer and aqueous tetrahydrofuran.
19 . The liquid composition of claim 14 wherein said ion-exchange polymer is perfluorinated.
20 . The liquid composition of claim 14 wherein said ion-exchange polymer has an ion-exchange ratio of about 3 to about 33.
21 . The liquid composition of claim 14 wherein said ion-exchange polymer has an ion-exchange ratio of about 8 to about 23.
22 . The liquid composition of claim 14 wherein said composition contains less than about 3 weight % organic materials other than said tetrahydrofuran and those associated with said ion exchange polymer.Join the waitlist — get patent alerts
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