Granted Patent B2

US 8,222,346 · App. 11/988,818 · Granted Jul 17, 2012

Abstract

Claims (50)

1. A hydrogenated sulfonated block copolymer having the general configuration A-B, A-B-A, (A-B) n , (A-B-A) n , (A-B-A) n X, (A-B) n X or mixtures thereof, where n is an integer from 2 to about 30, and X is coupling agent residue and wherein:

prior to hydrogenation each A block is a mono alkenyl arene polymer block and each B block is a controlled distribution copolymer block of at least one conjugated diene and at least one mono alkenyl arene;

subsequent to hydrogenation about 0-10% of the arene double bonds have been reduced, and at least about 90% of the conjugated diene double bonds have been reduced;

each A block having a number average molecular weight between about 3,000 and about 60,000 and each B block having a number average molecular weight between about 30,000 and about 300,000;

each B block comprises terminal regions adjacent to the A blocks that are rich in conjugated diene units and one or more regions not adjacent to the A blocks that are rich in mono alkenyl arene units;

the total amount of mono alkenyl arene in the hydrogenated block copolymer is about 20 percent by weight to about 80 percent by weight;

the weight percent of mono alkenyl arene in each B block is between about 10 percent and about 75 percent;

at least 25% of the aromatic rings of the alkenyl arene are sulfonated; and

the hydrogenated sulfonated block copolymer has an ionic conductivity greater than 0.08 siemens/cm.

2. The sulfonated block copolymer of claim 1 wherein the polymer has from about one sulfonic acid or sulfonate group per molecule to about one sulfonic acid or sulfonate group per aromatic ring.

3. The sulfonated block copolymer of claim 2 wherein the polymer has from about three sulfonic acid or sulfonate groups per molecule to about 50 percent of the aromatic rings having sulfonic acid or sulfonate groups.

4. The sulfonated block copolymer of claim 2 wherein the mono alkenyl arene is styrene and the conjugated diene is selected from the group consisting of isoprene and butadiene.

5. The sulfonated block copolymer of claim 4 wherein the conjugated diene is butadiene, and wherein about 20 to about 80 mol percent of the condensed butadiene units in block B have 1, 2-configuration prior to hydrogenation.

6. The sulfonated block copolymer of claim 5 wherein the styrene blockiness index of the block B is less than about 40 percent, the styrene blockiness index being the proportion of styrene units in the block B having two styrene neighbors on the polymer chain.

7. The sulfonated block copolymer of claim 6 wherein each block B has a center region with a minimum ratio of butadiene units to styrene units.

8. The sulfonated block copolymer of claim 7 wherein the weight percentage of styrene in the B block is between about 20 percent and about 70 percent, and the styrene blockiness index of the block B is less than about 10 percent, the styrene blockiness index being the proportion of styrene units in the block B having two styrene neighbors on the polymer chain.

9. The sulfonated block copolymer of claim 4 wherein the weight percentage of styrene in the block copolymer is between about 60 and 80 weight percent and the molecular weight of the A blocks are between about 10,000 and about 35,000.

10. The sulfonated block copolymer of claim 9 wherein between about 30 and about 50 percent of the styrene rings have a sulfonic acid or sulfonate group.

11. The sulfonated block copolymer of claim 10 having a water uptake of between about 200 volume percent and 300 volume percent.

12. The sulfonated block polymer of claim 1 wherein from about 25 percent to about 70 percent of the aromatic rings have a sulfonic acid or sulfonate group.

13. The sulfonated block polymer of claim 12 wherein from about 25 percent to about 50 percent of the aromatic rings have a sulfonic acid or sulfonate group.

14. A process for preparing a sulfonated block copolymer comprising:

hydrogenating a block copolymer having the general configuration A-B, A-B-A, (A-B) n , (A-B-A) n , (A-B-A) n X, (A-B) n X or mixtures thereof, where n is an integer from 2 to about 30, and X is coupling agent residue and wherein:

prior to hydrogenation each A block is a mono alkenyl arene polymer block and each B block is a controlled distribution copolymer block of at least one conjugated diene and at least one mono alkenyl arene;

subsequent to hydrogenation about 0-10% of the arene double bonds have been reduced, and at least about 90% of the conjugated diene double bonds have been reduced;

each A block having a number average molecular weight between about 3,000 and about 60,000 and each B block having a number average molecular weight between about 30,000 and about 300,000;

each B block comprises terminal regions adjacent to the A blocks that are rich in conjugated diene units and one or more regions not adjacent to the A blocks that are rich in mono alkenyl arene units;

the total amount of mono alkenyl arene in the hydrogenated block copolymer is about 20 percent by weight to about 80 percent by weight; and

the weight percent of mono alkenyl arene in each B block is between about 10 percent and about 75 percent;

dissolving the hydrogenated block copolymer in a solvent; and

admixing the polymer solution with a sulfonating agent under reaction conditions sufficient to prepare a sulfonated block copolymer having an ionic conductivity greater than 0.08 siemens/cm, wherein at least 25% of the aromatic rings of the alkenyl arene are sulfonated.

15. The process of claim 14 wherein the sulfonating agent is acetyl sulfate.

16. A process for preparing a sulfonated block copolymer comprising:

hydrogenating a block copolymer having the general configuration A-B, A-B-A, (A-B) n , (A-B-A) n , (A-B-A) n X, (A-B) n X or mixtures thereof, where n is an integer from 2 to about 30, and X is coupling agent residue and wherein:

prior to hydrogenation each A block is a mono alkenyl arene polymer block and each B block is a controlled distribution copolymer block of at least one conjugated diene and at least one mono alkenyl arene;

subsequent to hydrogenation about 0-10% of the arene double bonds have been reduced, and at least about 90% of the conjugated diene double bonds have been reduced;

each A block having a number average molecular weight between about 3,000 and about 60,000 and each B block having a number average molecular weight between about 30,000 and about 300,000;

each B block comprises terminal regions adjacent to the A blocks that are rich in conjugated diene units and one or more regions not adjacent to the A blocks that are rich in mono alkenyl arene units;

the total amount of mono alkenyl arene in the hydrogenated block copolymer is about 20 percent by weight to about 80 percent by weight; and

the weight percent of mono alkenyl arene in each B block is between about 10 percent and about 75 percent;

dissolving the hydrogenated block copolymer in a solvent; and

admixing the polymer solution with a sulfonating agent under reaction conditions sufficient to prepare a sulfonated block copolymer having an ionic conductivity greater than 0.08 siemens/cm, wherein at least 25% of the aromatic rings of the alkenyl arene are sulfonated;

wherein the temperature of the reaction is maintained at from about 30° C. to about 50° C.

17. The process of claim 16 wherein the sulfonating agent is acetyl sulfate.

18. The process of claim 17 wherein the process is a batch process and the polymer concentration in the solvent is from about 1 to about 5 percent by weight.

19. The process of claim 18 wherein the polymer concentration in the solvent is from about 2 to about 4 percent by weight.

20. The process of claim 19 wherein the polymer concentration in the solvent is about 3 percent by weight.

21. The process of claim 17 wherein the process is a continuous process and the polymer concentration in the solvent is from about 0.1 to about 3 percent by weight.

22. The process of claim 21 wherein the process is a continuous process and the polymer concentration in the solvent is from about 0.5 to about 2.5 percent by weight.

23. The process of claim 22 wherein the process is a continuous process and the polymer concentration in the solvent is about 2 percent by weight.

Assignments (9)