Gas separations utilizing glassy polymer membranes at sub-ambient temperatures

• US 5,679,133 A
• Filed: 08/18/1994
• Issued: 10/21/1997
• Est. Priority Date: 01/30/1991
• Status: Expired due to Term

• Current Assignee: Cynara Co. (Schlumberger NV)
• Original Assignee: The Dow Chemical Company (Dow, Inc.)
• Inventors: Wessling, Ritchie A., Beck, Henry Nelson, Moll, David J., Clark, James E., Young, Thomas C., Hotz, Charles Z., McReynolds, Kent B., Jeanes, Thomas O., Bales, Stephen E., Quarderer, George J., Smith, Bethanne L., Lacher, Ronald M., Burmester, Alan F.
• Primary Examiner(s): SPITZER, ROBERT H
• Application Number:
  US08/292,771
• Time in Patent Office: 1,160 Days
• Field of Search: 55/267-269, 96/4, 96/7-14, 95/45, 95/47-55
• US Class Current: 95/45
• CPC Class Codes: B01D 53/22 by diffusion manufacturing semi-permeable membranes B01D67/00; form, structure or properties of semi-permeable membranes B01D69/00; material for semi-permeable membranes B01D71/00
• CPC Class Codes: B01D 53/228 characterised by specific membranes
• CPC Class Codes: B01D 53/268 by diffusion
• CPC Class Codes: B01D 69/02 characterised by their properties
• CPC Class Codes: B01D 71/48 Polyesters
• CPC Class Codes: B01D 71/481 Polyarylates
• CPC Class Codes: B01D 71/50 Polycarbonates
• CPC Class Codes: B01D 71/52 Polyethers
• CPC Class Codes: B01D 71/5222 Polyetherketone, polyetheretherketone, or polyaryletherketone
• CPC Class Codes: B01D 71/5223 Polyphenylene oxide, phenyl ether polymers or polyphenylethers
• CPC Class Codes: B01D 71/62 Polycondensates having nitrogen-containing heterocyclic rings in the main chain
• CPC Class Codes: B01D 71/64 Polyimides; Polyamide-imides; Polyester-imides; Polyamide acids or similar polyimide precursors
• CPC Class Codes: B01D 71/641 Polyamide-imides
• CPC Class Codes: B01D 71/66 Polymers having sulfur in the main chain, with or without nitrogen, oxygen or carbon only
• CPC Class Codes: B01D 71/72 Macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds, not provided for in a single one of the groups B01D71/46 - B01D71/70 and B01D71/701 - B01D71/702
• CPC Class Codes: C01B 13/0251 by making use of membranes
• CPC Class Codes: C01B 21/0444 characterised by the membrane
• CPC Class Codes: C01B 2210/0046 Nitrogen
• CPC Class Codes: C01B 2210/0062 Water
• CPC Class Codes: C08G 64/10 containing halogens
• CPC Class Codes: C08G 75/06 : from cyclic thioethers
• CPC Class Codes: C08G 75/26 : Polythioesters
• CPC Class Codes: C08L 71/12 : Polyphenylene oxides
• CPC Class Codes: Y02P 20/129 : Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines

Abstract

This invention relates to a method of and apparatus for separating component gases in a gas mixture employing a glassy polymer membrane at temperatures of 5° C. or less so as to achieve superior separation of gas components.

Claims

1. A method of separating component gases in a gas mixture comprising:

A. contacting a first side of a gas separation membrane, the membrane comprising a discriminating layer or region of a glassy polymer, wherein for said polymer cellulose triacetate is excluded, with the gas mixture while maintaining a difference in chemical potential from the first side of the membrane to a second side of the membrane, such that at least one first component gas of the gas mixture selectively permeates relative to at least one second component gas in the gas mixture from the first side of the membrane through the membrane to the second side of the membrane, said contacting occurring at a temperature of -5°

C. or lower, wherein the membrane having a glassy region is selected so that, when using a mixture of 80 mole percent nitrogen and 20 mole percent oxygen as a feed at 30°

C. with a pressure of 30 psia on the first side of the membrane and a vacuum of less than 1 mm Hg on the second side of the membrane, the permeability of oxygen in barriers is less than 2000 and has the following relationship to oxygen/nitrogen selectivity;

##EQU6## B. recovering at least one of the permeate gas or rejected non-permeate gas.

2. The method as described in claim 1 wherein at least one of the first component gas or the second component gas is selected from the group consisting of hydrogen, helium, oxygen, nitrogen, argon, carbon monoxide, carbon dioxide, hydrogen sulfide, nitrogen oxides, sulfur oxides, ammonia, water vapor, and light hydrocarbons.

3. The method as described in claim 2 wherein the first component gas is oxygen and the second component gas is nitrogen.

4. The method as described in claim 3 wherein the membrane has a Figure of Merit for oxygen/nitrogen separation of at least about 1.0.

5. The method as described in claim 4 wherein the glassy polymer comprises a polyimide, a polyphenylene oxide, a polyamide, a polycarbonate, a polyester, a polyestercarbonate, a polyarylate, a polytriazole, a polyoxadiazole, a polyether, a polyolefin, a polysulfone, a polyethersulfone, a polybenzoxazole, or a copolymer or physical blend thereof.

6. The method as described in claim 5 wherein the membrane is an asymmetric, anisotropic, composite, or surface treated membrane.

7. The method as described in claim 6 wherein the glassy polymer comprises an indan-containing polybenzoxazole or indan-containing polyimide.

8. The method as described in claim 6 wherein the glassy polymer comprises a polymer having the recurring units:

##STR10## wherein Z is oxygen.

9. The method as described in claim 6 wherein the glassy polymer comprises a polymer containing 9,9-bis(dibromo-4-hydroxyphenyl)fluorene, 9,9-bis(dichloro-4-hydroxyphenyl)fluorene, hexafluoro bisphenol A, tetrahalo hexafluoro bisphenol A, or tetraalkyl hexafluoro bisphenol A moieties selected from the group consisting of polycarbonate, polyimide, polyether, polysulfone, polyethersulfone, polyarylate, polyester, polyestercarbonate, or a copolymer or physical blend thereof.

10. The method as described in claim 9 wherein the glassy polymer comprises tetrabromohexafluoro bisphenol A polycarbonate or tetrachlorohexafluoro bisphenol A polycarbonate.

11. The method as described in claim 9 wherein the glassy polymer comprises 9,9-bis(dibromo-4-hydroxyphenyl)fluorene polycarbonate or 9,9-bis(3,5-dichloro-4-hydroxyphenyl)fluorene polycarbonate.

12. The method as described in claim 3 wherein the membrane exhibits at a temperature of 5°

C. or less a selectivity for oxygen/nitrogen of at least about 10 and an oxygen permeability of at least about 1 barrer, as measured using a mixture of 80 mole percent nitrogen and 20 mole percent oxygen as a feed with a pressure of 30 psia on the first side of the membrane and a vacuum of less than 1 mm Hg on the second side of the membrane.

13. The method as described in claim 2 wherein the first component gas is carbon dioxide and the second component gas is a light hydrocarbon.

14. The method as described in claim 13 wherein the temperature for separation is in the range from about -40°

C. to about -5°

C.

15. The method as described in claim 13 wherein the membrane has a Figure of Merit for carbon dioxide/methane separation of at least about 20.

16. The method as described in claim 15 wherein the glassy polymer comprises a polybenzoazole, a polycarbonate, a polyester, a polyestercarbonate, a polysulfone, a polyethersulfone, a polyimide, a polyether, a polyarylate, or a copolymer or physical blend thereof.

17. The method as described in claim 16 wherein the membrane is an asymmetric, anisotropic, or composite, or surface treated membrane.

18. The method as described in claim 17 wherein the glassy polymer comprises a polymer having the recurring units:

##STR11## wherein Z is oxygen.

19. The method as described in claim 17 wherein the glassy polymer comprises a polymer containing 9,9-bis(dibromo-4-hydroxyphenyl)fluorene, 9,9-bis(dichloro-4-hydroxyphenyl)fluorene, hexafluoro bisphenol A, tetrahalo hexafluoro bisphenol A, or tetraalkyl hexafluoro bisphenol A moieties selected from the group consisting or polycarbonate, polyimide, polyether, polysulfone, polyethersulfone, polyarylate, polyester, polyestercarbonate, or a copolymer or physical blend thereof.

20. The method as described in claim 13 wherein the membrane exhibits at a temperature of 5°

C. or less a selectivity for carbon dioxide/methane of at least about 40 and a carbon dioxide permeability of at least about 10 barrers, as measured using a mixture or 5 mole percent carbon dioxide and 95 mole percent methane as a feed with a pressure of 30 psia on the first side of the membrane and a vacuum or less than 1 mm Hg on the second side of the membrane.

21. The method as described in claim 2 wherein the first component gas is hydrogen or helium and the second component gas is a light hydrocarbon.

22. The method as described in claim 21 wherein the membrane has a Figure of Merit for helium/methane separation of at least about 5.

23. The method as described in claim 2 wherein the first component gas is ethylene and the second component gas is ethane.

24. The method as described in claim 2 wherein the temperature for separation is in the range from about -30°

C. to about -5°

C.

25. The method as described in claim 2 wherein the membrane is in the form of a plurality of hollow fibers.

26. The method as described in claim 25 wherein the gas mixture is introduced into the bores of the hollow fibers and the gas which has permeated through the fibers generally flows countercurrent to the gas in the bores of the hollow fibers.

27. The method as described in claim 25 wherein the hollow fibers comprise a discriminating layer or region at or near the internal surface of the hollow fibers and a generally porous region extending from the discriminating layer or region to the external surface of the hollow fibers.

28. The method as described in claim 25 wherein the hollow fibers comprise a generally porous region at or near the external surface of the hollow fibers, a generally porous region at or near the internal surface the of the hollow fibers, and a discriminating layer or region generally situated between the two porous surface regions.

29. The method as described in claim 2 wherein the membrane is an asymmetric, anisotropic, composite, or surface treated membrane.

30. The method as described in claim 29 wherein the membrane has a Permselectivity Index of at least about 0.25 for oxygen/nitrogen separation.

31. The method as described in claim 29 wherein the membrane exhibits a Figure of Merit for oxygen/nitrogen of at least about 3.0.

32. The method as described in claim 29 wherein the membrane exhibits a Figure of Merit for carbon dioxide/methane separation of at least about 25.

33. The method as described in claim 29 wherein the membrane exhibits a Figure of Merit for helium/methane separation of at least about 15.

34. The method as described in claim 29 wherein the membrane exhibits at a temperature of 5°

C. or less a selectivity for oxygen/nitrogen of at least about 12 and an oxygen permeability of at least about 1 barrer, as measured using a mixture of 80 mole percent nitrogen and 20 mole percent oxygen as a feed with a pressure of 30 psia on the first side of the membrane and a vacuum of less than 1 mm Hg on the second side or the membrane.

35. The method as described in claim 2 wherein said glassy polymer exhibits a glass transition temperature of at least about 100°

C.

36. The method as described in claim 2 wherein the membrane is in the form of a flat sheet or film.

37. A method of separating component gases in a gas mixture comprising:

A. contacting a first side of a gas separation membrane, the membrane comprising a discriminating layer or region of a glassy polymer, wherein for said polymer celulose triacetate is excluded, with the gas mixture while maintaining a difference in chemical potential from the first side of the membrane to a second side of the membrane, such that at least one first component gas of the gas mixture selectively permeates relative to at least one second component gas in the gas mixture from the first side of the membrane through the membrane to the second side of the membrane, said contact and separation occurring in the temperature range from about -150°

C. to about -5°

C., wherein the membrane having a glassy region is selected so that, when using a mixture of 80 mole percent nitrogen and 20 mole percent oxygen as a feed at 30°

C. with a pressure of 30 psia on the first side of the membrane and a vacuum of less than 1 mm Hg on the second side of the membrane, the permeability of oxygen in barriers is less than 2000 and has the following relationship to oxygen/nitrogen selectivity;

##EQU7## B. recovering at least one of the permeate gas or rejected non-permeate gas, wherein at least one of the first component gas or the second component gas is selected from the group consisting of hydrogen, helium, oxygen, nitrogen, argon, carbon monoxide, carbon dioxide, hydrogen sulfide, nitrogen oxides, sulfur oxides, ammonia, water vapor, and light hydrocarbons.

38. The method as described in claim 37 wherein the temperature for separation is in the range from about -125°

C. to about -25°

C.

39. A process for separating component gases in a gas mixture comprising:

A. contacting a first side of a gas separation membrane comprising a discriminating layer or region of a glassy polymer with the gas mixture under pressure and at a temperature of -5°

C. or less;

B. maintaining a difference in pressure from the first side of the membrane to a second side of the membrane, under conditions such that at least one first component gas of the gas mixture selectively permeates relative to at least one second component gas through the membrane from the higher pressure first side of the membrane to the lower pressure second side of the membrane; and

C. recovering at least one of the rejected non-permeate gas from the first side or the membrane or the permeate gas from the second side of the membrane;

wherein the membrane is selected so that, when using a mixture of 80 mole percent nitrogen and 20 mole percent oxygen as a feed at 30°

C. with a pressure of 30 psia on the first side of the membrane and a vacuum of less than 1 mm Hg on the second side of the membrane, the permeability of oxygen in barrers is less than 2000 and has the following relationship to oxygen/nitrogen selectivity;

##EQU8##

40. The process as described in claim 39 wherein the glassy polymer comprises a polyphenylene oxide, a polyimide, a polycarbonate, a polyamide, a polyether, a polyestercarbonate, a polyarylate, a polyester, a polyacetylene, a polytriazole, a polyoxadiazole, a polyolefin, a polysulfone, a polyethersulfone, polyamideimide, a polyvinylsilane, a polybenzoazole, or a copolymer or physical blend thereof.

41. The process as described in claim 40 comprising the additional step of altering the temperature of the gas mixture to a temperature of -5°

C. or less.

42. The process as described in claim 41 wherein the temperature of the gas mixture is altered by cooling the gas mixture using at least one of an external refrigeration system, an adsorptive refrigeration system, an expansion device, or the self-refrigerating capacity of the permeate gas.

43. The process or claim 41 comprising the additional step of passing the cooled gas through a means for exchanging heat with the gas mixture to be introduced into the membrane so as to cool the gas mixture.

44. The process as described in claim 41 comprising the additional step of recycling at least a portion of either the non-permeate gas or the permeate gas.

45. The process as described in claim 44 wherein the temperature of one device at about -5°

C. or less is different from the temperature of at least one other device also at which is about -5°

C. or less.

46. The process as described in claim 41 operated with two or more membrane devices arranged in series or cascade configuration, or a combination thereof.

47. The process as described in claim 46 comprising the additional step of compression of gas between devices.

48. The process as described in claim 46 wherein the composition of the membrane used in at least one device is different than the composition of the membrane used in at least one other device.

49. The process as described in claim 41 comprising the additional separation step of at least one of pressure-swing adsorption, temperature-swing adsorption, vacuum-swing adsorption, fractionation, distillation, rectification, chemical absorption, chemical reaction, or extraction.

50. The process as described in claim 40 comprising the additional step of expanding at least a portion of either the feed gas mixture, the non-permeate gas, or the permeate gas to cool the gas.

51. The process as described in claim 50 wherein the gas is expanded and cooled using a turbine expander.

52. The process as described in claim 40 comprising the additional step of pretreating the gas mixture to substantially remove one or more contaminants having a deleterious impact on the performance or physical integrity of the membrane or system components.

53. The process as described in claim 52 wherein the contaminants comprise solid particulates or liquid droplets larger than 1 micron, hydrocarbons, glycols, oil field additives, surfactants, mercury, oils, hydrogen sulfide, water vapor, nitrogen oxides, sulfur oxides, hydrogen chloride, chlorine, mercaptans, carbonyl sulfide, or a combination thereof.

54. The process as described in claim 52 comprising the additional step of using at least a portion of either the non-permeate gas or the permeate gas to purge or regenerate pretreatment equipment.