Asymmetric modified carbon molecular sieve hollow fiber membranes having improved permeance

Patent metadata

Field	Value
Publication number	US-9815030-B2
Application number	US-201414501884-A
Country	US
Kind code	B2
Filing date	Sep 30, 2014
Priority date	Sep 30, 2013
Publication date	Nov 14, 2017
Grant date	Nov 14, 2017

Abstract

The present invention provides an asymmetric modified CMS hollow fiber membrane having improved gas separation performance properties and a process for preparing an asymmetric modified CMS hollow fiber membrane having improved gas separation performance properties. The process comprises treating a polymeric precursor fiber with a solution containing a modifying agent prior to pyrolysis. The concentration of the modifying agent in the solution may be selected in order to obtain an asymmetric modified CMS hollow fiber membrane having a desired combination of gas permeance and selectivity properties. The treated precursor fiber is then pyrolyzed to form an asymmetric modified CMS hollow fiber membrane having improved gas permeance.

First claim

What is claimed:

1. A process for preparing an asymmetric modified carbon molecular sieve hollow fiber membrane having improved gas separation performance properties comprising
a. providing an asymmetric polymer hollow fiber,
b. contacting the polymer fiber with a solution comprising a modifying agent,
c. contacting the polymer fiber of step b. with a moisture-containing atmosphere to form a treated polymer fiber, and
d. pyrolyzing the treated polymer fiber to form an asymmetric modified carbon molecular sieve hollow fiber membrane having an improved gas permeance,

wherein the concentration of the modifying agent in the solution is selected to obtain an asymmetric modified carbon molecular sieve hollow fiber membrane having an improved gas permeance.

2. The process of claim 1 , wherein the modifying agent comprises between about 1 wt % and about 95 wt % of the solution.

3. The process of claim 2 , wherein the modifying agent comprises between about 1 wt % and about 50 wt % of the solution.

4. The process of claim 3 , wherein the modifying agent comprises between about 5 wt % and about 25 wt % of the solution.

5. The process of claim 1 , wherein the modifying agent is a compound having the formula R 1 R 2 R 3 R 4 Si, where each of R 1 , R 2 , R 3 , and R 4 are independently C 1 -C 6 alkyl or alkenyl, alkoxy, or halogen; with the proviso that the compound contains at least one C 1 -C 6 alkyl or alkenyl substituent and at least one alkoxy or halogen substituent.

6. The process of claim 5 , wherein the modifying agent is vinyl trimethoxy silane.

7. The process of claim 1 , wherein the modifying agent is a compound having the formula R 1 R 2 R 3 R 4 M, where M is a metal and where each of R 1 , R 2 , R 3 , and R 4 are independently C 1 -C 6 alkyl or alkenyl, alkoxy, or halogen, with the proviso that the compound contains at least one C 1 -C 6 alkyl or alkenyl substituent and at least one alkoxy or halogen substituent.

8. The process of claim 7 , where M is selected from the group consisting of Ge, B, Al, Ti, V, Fe, and combinations thereof.

9. The process of claim 1 , wherein the solution further comprises a C 5 or greater, linear or branched-chain aliphatic hydrocarbon.

10. The process of claim 9 , wherein the C 5 or greater linear or branched-chain aliphatic hydrocarbon is n-hexane.

11. The process of claim 1 , wherein the solution comprises a vinyl trimethoxy silane modifying agent and n-hexane.

12. The process of claim 1 , wherein the asymmetric polymer hollow fiber comprises a polyimide.

13. The process of claim 12 , wherein the polyimide is
(i) a polyimide made up of 2,4,6-Trimethyl-l,3-phenylene diamine; 3,3,4,4-biphenyl tetracarboxylic dianhydride; and 5,5-[2,2,2-trifluoro-l-(trifluoromethyl)ethylidene]bis-l,3-isobenzofurandione; or
(ii) a polyimide having the following structure:

14. The process of claim 1 , wherein the concentration of the modifying agent in the solution is selected to obtain an asymmetric modified carbon molecular sieve hollow fiber membrane having a gas permeance property that is at least a 300% increase over an equivalent asymmetric carbon molecular sieve hollow fiber membrane that is not subjected to the treatment of step b.

15. The process of claim 14 , wherein the concentration of the modifying agent in the solution is selected to obtain an asymmetric modified carbon molecular sieve hollow fiber membrane having a selectivity that is at least 85% of the selectivity of an equivalent asymmetric carbon molecular sieve hollow fiber membrane that is not subjected to the treatment of step b.

16. The process of claim 1 , wherein the concentration of the modifying agent in the solution is selected to obtain an asymmetric modified carbon molecular sieve hollow fiber membrane that is useful for the separation of gases selected from the group consisting of CO 2 and CH 4 , H 2 S and CH 4 , CO 2 /H 2 S and CH 4 , CO 2 and N 2 , O 2 and N 2 , N 2 and CH 4 , He and CH 4 , H 2 and CH 4 , H 2 and C 2 H 4 , ethylene and ethane, propylene and propane, and ethane/propane and ethylene/propylene.

17. The process of claim 1 , wherein the concentration of the modifying agent in the solution is selected to obtain an asymmetric modified carbon molecular sieve hollow fiber membrane that is useful for the separation of acid gases from a natural gas stream.

18. The process of claim 1 , wherein the concentration of the modifying agent in the solution is selected to obtain an asymmetric modified carbon molecular sieve hollow fiber membrane that is useful for the separation of CO 2 from a hydrocarbon-containing gas stream.

19. The process of claim 1 , wherein the concentration of the modifying agent in the solution is selected to obtain an asymmetric modified carbon molecular sieve hollow fiber membrane having CO 2 permeance of at least 50 GPU and a CO 2 /CH 4 selectivity of at least 60 when subjected to a mixed feed containing 50 mol % CO 2 and 50 mol % CH 4 at 150 psi and 35° C.

20. The process of claim 1 , wherein a plurality of the treated polymer fibers are bundled prior to pyrolysis to form a bundle of asymmetric modified carbon molecular sieve hollow fibers, wherein the asymmetric modified carbon molecular sieve hollow fibers are substantially free from sticking to one another.

21. A process for forming an asymmetric modified carbon molecular sieve hollow fiber membrane comprising
a. forming an asymmetric hollow polymer fiber,
b. contacting the hollow polymer fiber with one or more solvent exchange materials, and
c. pyrolyzing the hollow polymer fiber to form an asymmetric carbon molecular sieve hollow fiber membrane,

wherein at least one of the solvent exchange materials comprises a modifying agent in an amount effective to improve the gas permeance of the asymmetric carbon molecular sieve hollow fiber membrane.

22. The process of claim 21 , further comprising, between step b and step c, contacting the hollow polymer fiber with a moisture-containing atmosphere.

23. The process of claim 21 , wherein at least one of the solvent exchange materials is a solution comprising an organic compound in addition to the modifying agent.

24. The process of claim 23 , wherein the organic compound is a C 5 or greater linear or branched-chain aliphatic hydrocarbon.

25. The process of claim 24 , wherein the organic compound is n-hexane.

26. The process of claim 21 , wherein the modifying agent is a compound having the formula R 1 R 2 R 3 R 4 Si, where each of R 1 , R 2 , R 3 , and R 4 are independently C 1 -C 6 alkyl or alkenyl, alkoxy, or halogen; with the proviso that the compound contains at least one C 1 -C 6 alkyl or alkenyl substituent and at least one alkoxy or halogen substituent.

27. The process of claim 26 , wherein the modifying agent is vinyl trimethoxy silane.

28. The process of claim 21 , wherein the modifying agent is a compound having the formula R 1 R 2 R 3 R 4 M, where M is a metal and where each of R 1 , R 2 , R 3 , and R 4 are independently C 1 -C 6 alkyl or alkenyl, alkoxy, or halogen, with the proviso that the compound contains at least one C 1 -C 6 alkyl or alkenyl substituent and at least one alkoxy or halogen substituent.

29. The process of claim 28 , where M is selected from the group

Assignees

• Georgia Tech Res Inst
• Shell Oil Co

Inventors

• Bhuwania Nitesh
• Koros William John
• Williams Paul Jason

Classifications

• B01D2325/022

  Asymmetric membranes · CPC title

• B01D53/228

  characterised by specific membranes · CPC title

• B01D2325/20

  Specific permeability or cut-off range · CPC title

• B01D2323/12

  Specific ratios of components used · CPC title

• B01D67/0067

  by carbonisation or pyrolysis · CPC title