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This abstract discusses membranes needed to separate fluids for the production of oxygen-enriched air, nitrogen-enriched-air, for the separation of carbon dioxide from hydrocarbons, and the separation of hydrogen from various petrochemical and oil refining streams. Membranes are needed that provide

This abstract discusses membranes needed to separate fluids for the production of oxygen-enriched air, nitrogen-enriched-air, for the separation of carbon dioxide from hydrocarbons, and the separation of hydrogen from various petrochemical and oil refining streams. Membranes are needed that provide a resistance to interaction with process components or contaminants, provide the mechanical strength required to withstand high membrane differential pressures and high process temperatures, and exhibit sufficient maximum strain such that membranes are not brittle and can easily be formed into desirable membrane forms. Membranes of polyimide polymers, particularly polyimide polymers sold under the trade name P-84, are annealed in a controlled annealing step to improve the mechanical properties of the polymers used to make separation membranes. The resulting annealed polyimide polymer is used to produce various forms of high strength, chemically resistant membranes, including hollow-fiber membranes that are suitable for high pressure, high temperature applications.

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1. A membrane for fluid separation formed from a polymeric composition comprising an annealed polyimide which is the annealing product of a virgin polymer comprising a plurality of first repeating units of a formula (I) and a plurality of second repeating units, wherein: said formula (I) is: in whic

1. A membrane for fluid separation formed from a polymeric composition comprising an annealed polyimide which is the annealing product of a virgin polymer comprising a plurality of first repeating units of a formula (I) and a plurality of second repeating units, wherein: said formula (I) is: in which R1 of said formula (I) is a moiety having a composition selected from the group consisting of a formula (A), a formula (B), a formula (C), and mixtures thereof;said formula (A), said formula (B), and said formula (C) are: R2 of said formula (I) is a moiety having a composition selected from the group consisting of a formula (Q), a formula (S), a formula (T), and mixtures thereof, wherein said formula (Q), said formula (S), and said formula (T) are: in which Z of said formula (T) is a moiety having a composition selected from the group consisting of a formula (L), a formula (M), a formula (N), and mixtures thereof;said formula (L), said formula (M), and said formula (N) are: andsaid second repeating units are represented by formula (II): 2. The membrane of claim 1, wherein a membrane of said annealed polyimide polymer has a maximum strain of greater than about 50%. 3. The membrane of claim 1, wherein said maximum strain is greater than about 100%. 4. The membrane of claim 2, wherein said membrane is a hollow fiber. 5. The membrane of claim 1, wherein an inherent viscosity of said annealed polyimide polymer is greater than about 0.58 dl/gm. 6. The membrane of claim 1, wherein said first repeating units comprise moieties of a formula (Ia), wherein said formula (Ia) is: wherein R1 of formula (Ia) is a moiety selected from the group consisting of said formula (A), said formula (B), said formula (C), and mixtures thereof. 7. The membrane of claim 6, wherein said moiety R1 has a composition of: a) said formula (A) in about 10-25% of said first repeating units;b) said formula (B) in about 55-75% of said first repeating units; andc) said formula (C) in about 20-40% of said first repeating units. 8. The membrane of claim 7, wherein said moiety R1 has a composition of: a) said formula (A) in about 16% of said first repeating units;b) said formula (B) in about 64% of said first repeating units; andc) said formula (C) in about 20% of said first repeating units. 9. The membrane of claim 1, wherein said first repeating units comprise moieties of a formula (Ib), wherein formula (Ib) is: wherein said R1 of formula (Ib) is a moiety wherein said R1 of formula (Ib) is a moiety selected from the group consisting of said formula (A) and said formula (B), and mixtures thereof. 10. The membrane of claim 1, wherein said first repeating units comprise moieties of: a) a formula (Ia); andb) a formula (Ib), wherein said formula (Ia) and said formula (Ib) are: and wherein R1 is a moiety selected from the group consisting of said formula (Q) and said formula (S), and mixtures thereof. 11. The membrane of claim 1, wherein R1 is a moiety having a composition of: a) said formula (A) in about 10-30% of said first repeating units; andb) said formula (B) in about 70-90% of said first repeating units, wherein said first repeating units of said formula (Ib) are about 30-50% of the total of said first repeating units. 12. The membrane of claim 11, wherein R1 is a moiety having a composition of: a) said formula (A) in about 20% of said first repeating units; andb) said formula (B) in about 80% of said first repeating units; andc) wherein said first repeating units of said formula (Ib) are about 40% of the total of said first repeating units. 13. The membrane of claim 1, wherein said second repeating units comprises less than about 3 mole % of a total of said first and second repeating units. 14. The membrane of claim 13, wherein said second repeating units comprises less than about 1 mole % of a total of said first and second repeating units. 15. The membrane of claim 13, wherein said membrane is a hollow fiber. 16. The membrane of claim 1, wherein said annealed polyimide polymer has been annealed by a process selected from the group consisting of mechanical annealing, thermal annealing, or combinations thereof. 17. The membrane of claim 1, wherein the polymeric composition further comprises an additional polymer blended with a polyethersulfone before membrane formation, the polyethersulfone having repeating units represented by formula III: 18. The membrane of claim 1, wherein the polymeric composition further comprises an additional polymer blended with the annealed polyimide polymer before membrane formation, the additional polymer comprising repeating units represented by formula (IV) and repeating units represented by formula (V): 19. A method of producing a fluid separation membrane, said method comprising the steps of: providing a virgin polymer comprising a plurality of first repeating units of a formula (I) and a plurality of second repeating units of a formula (II);annealing said virgin polymer to form an annealed polymer;preparing a concentrated solution of said annealed polyimide polymer in a solvent; andforming a membrane from said concentrated solution, wherein:a) said formula (I) is: in which R1 of said formula (I) is a moiety having a composition selected from the group consisting of a formula (A), a formula (B), a formula (C), and mixtures thereof;b) formula (A), said formula (B), and said formula (C) are: and in which R2 of said formula (I) is a moiety having a composition selected from the group consisting of a formula (Q), a formula (S), a formula (T), and mixtures thereof; c) said formula (Q), said formula (S), and said formula (T) are: in which Z of said formula (T) is a moiety having a composition selected from the group consisting of a formula (L), a formula (M), a formula (N), and mixtures thereof; d) said formula (L), said formula (M), and said formula (N) are: e) said formula (II) is: 20. The method of claim 19, wherein said annealed polyimide polymer comprises less than about 3 mole % said second repeating units. 21. The method of claim 20, wherein said annealed polyimide polymer comprises less than about 1 mole % said second repeating units after said annealing step. 22. The membrane of claim 19, wherein said first repeating units comprise moieties selected from the group consisting of a formula (Ia), a formula (Ib), and mixtures thereof, wherein said formula (Ia) and said formula (Ib) are: and wherein R1 is a moiety selected from the group consisting of said formula (Q) and said formula (S), and mixtures thereof. 23. The membrane of claim 19, wherein: R1 is a moiety having a composition of said formula (A) in about 10-30% of said first repeating units and said formula (B) in about 70-90% of said first repeating units; andsaid first repeating units of said formula (Ib) are about 30-50% of the total of said first repeating units. 24. The method of claim 19, wherein said annealing step is conducted by a process selected from the group consisting of mechanical annealing, thermal annealing, or combinations thereof. 25. The method of claim 24, wherein said annealing step is conducted for a period of time of about 6-30 hours at a temperature of about 100-250° C. 26. The method of claim 25, wherein said period of time is about 10-16 hours and said temperature is about 140-180° C. 27. The method of claim 24, wherein said annealing step is conducted under a vacuum of greater than about 15 inches of mercury. 28. The method of claim 19, wherein said concentrated solution comprises about 30 weight % said annealed polyimide polymer, wherein said solvent is NMP, and wherein said concentrated solution has a zero-shear complex viscosity of greater than about 90 Pa·s at 40° C. 29. The method of claim 28, wherein said concentrated solution has a zero-shear complex viscosity of greater than about 150 Pa·s at 40° C. 30. The method of claim 28, wherein said concentrated solution has a zero-shear complex viscosity in a range of about 150 Pa·s to about 500 Pa·s at 40° C. 31. The method of claim 19, wherein said membrane is a hollow fiber membrane. 32. The method of claim 19, wherein the inherent viscosity of said annealed polyimide polymer is at least about 5% greater than the inherent viscosity of said polyimide polymer. 33. The method of claim 19, wherein the concentrated solution further includes a polyethersulfone having repeating units represented by formula (III): 34. The method of claim 19, wherein the concentrated solution further includes an additional polymer comprising repeating units represented by formula (IV) and repeating units represented by formula (V): 35. A membrane for fluid separation formed from a polymeric composition comprising a polyimide and a polyethersulfone, the polymide comprising a plurality of first repeating units of a formula (I) and a plurality of second repeating units, wherein: said formula (I) is: in which R1 of said formula (I) is a moiety having a composition selected from the group consisting of a formula (A), a formula (B), a formula (C), and mixtures thereof;said formula (A), said formula (B), and said formula (C) are: R2 of said formula (I) is a moiety having a composition selected from the group consisting of a formula (Q), a formula (S), a formula (T), and mixtures thereof, wherein said formula (Q), said formula (S), and said formula (T) are: in which Z of said formula (T) is a moiety having a composition selected from the group consisting of a formula (L), a formula (M), a formula (N), and mixtures thereof;said formula (L), said formula (M), and said formula (N) are: said second repeating units are represented by formula (II): andsaid polyethersulfone comprises repeating units represented by formula (III): 36. A membrane for fluid separation formed from a polymeric composition comprising a polyimide and a polyamide-imide, the polymide comprising a plurality of first repeating units of a formula (I) and a plurality of second repeating units, wherein: said formula (I) is: in which R1 of said formula (I) is a moiety having a composition selected from the group consisting of a formula (A), a formula (B), a formula (C), and mixtures thereof;said formula (A), said formula (B), and said formula (C) are: R2 of said formula (I) is a moiety having a composition selected from the group consisting of a formula (Q), a formula (S), a formula (T), and mixtures thereof, wherein said formula (Q), said formula (S), and said formula (T) are: in which Z of said formula (T) is a moiety having a composition selected from the group consisting of a formula (L), a formula (M), a formula (N), and mixtures thereof;said formula (L), said formula (M), and said formula (N) are: said second repeating units are represented by formula (II): andsaid polyamide-imide comprises repeating units represented by formula (IV) and repeating units represented by formula (V):