CA2500346A1 - Polyimide blends for gas separation membranes - Google Patents
Polyimide blends for gas separation membranes Download PDFInfo
- Publication number
- CA2500346A1 CA2500346A1 CA002500346A CA2500346A CA2500346A1 CA 2500346 A1 CA2500346 A1 CA 2500346A1 CA 002500346 A CA002500346 A CA 002500346A CA 2500346 A CA2500346 A CA 2500346A CA 2500346 A1 CA2500346 A1 CA 2500346A1
- Authority
- CA
- Canada
- Prior art keywords
- formula
- membrane
- repeating units
- mixture
- copolyimide
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 239000000203 mixture Substances 0.000 title claims abstract 45
- 239000012528 membrane Substances 0.000 title claims abstract 27
- 238000000926 separation method Methods 0.000 title claims 4
- 239000004642 Polyimide Substances 0.000 title 1
- 229920001721 polyimide Polymers 0.000 title 1
- 229920000642 polymer Polymers 0.000 claims abstract 5
- 238000000034 method Methods 0.000 claims abstract 4
- 239000007789 gas Substances 0.000 claims 15
- 125000000217 alkyl group Chemical group 0.000 claims 4
- 239000012466 permeate Substances 0.000 claims 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims 2
- GTDPSWPPOUPBNX-UHFFFAOYSA-N ac1mqpva Chemical compound CC12C(=O)OC(=O)C1(C)C1(C)C2(C)C(=O)OC1=O GTDPSWPPOUPBNX-UHFFFAOYSA-N 0.000 claims 2
- 125000003118 aryl group Chemical group 0.000 claims 2
- 125000004432 carbon atom Chemical group C* 0.000 claims 2
- 230000000295 complement effect Effects 0.000 claims 2
- 229910052739 hydrogen Inorganic materials 0.000 claims 2
- 239000001257 hydrogen Substances 0.000 claims 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims 2
- XNGIFLGASWRNHJ-UHFFFAOYSA-N phthalic acid Chemical compound OC(=O)C1=CC=CC=C1C(O)=O XNGIFLGASWRNHJ-UHFFFAOYSA-N 0.000 claims 2
- 239000012465 retentate Substances 0.000 claims 2
- VLDPXPPHXDGHEW-UHFFFAOYSA-N 1-chloro-2-dichlorophosphoryloxybenzene Chemical compound ClC1=CC=CC=C1OP(Cl)(Cl)=O VLDPXPPHXDGHEW-UHFFFAOYSA-N 0.000 claims 1
- ZVDSMYGTJDFNHN-UHFFFAOYSA-N 2,4,6-trimethylbenzene-1,3-diamine Chemical group CC1=CC(C)=C(N)C(C)=C1N ZVDSMYGTJDFNHN-UHFFFAOYSA-N 0.000 claims 1
- ZHBXLZQQVCDGPA-UHFFFAOYSA-N 5-[(1,3-dioxo-2-benzofuran-5-yl)sulfonyl]-2-benzofuran-1,3-dione Chemical compound C1=C2C(=O)OC(=O)C2=CC(S(=O)(=O)C=2C=C3C(=O)OC(C3=CC=2)=O)=C1 ZHBXLZQQVCDGPA-UHFFFAOYSA-N 0.000 claims 1
- 150000004982 aromatic amines Chemical class 0.000 claims 1
- WKDNYTOXBCRNPV-UHFFFAOYSA-N bpda Chemical compound C1=C2C(=O)OC(=O)C2=CC(C=2C=C3C(=O)OC(C3=CC=2)=O)=C1 WKDNYTOXBCRNPV-UHFFFAOYSA-N 0.000 claims 1
- 239000001569 carbon dioxide Substances 0.000 claims 1
- 229910002092 carbon dioxide Inorganic materials 0.000 claims 1
- 239000012510 hollow fiber Substances 0.000 claims 1
- 238000006068 polycondensation reaction Methods 0.000 claims 1
- 230000035699 permeability Effects 0.000 abstract 1
- 239000000126 substance Substances 0.000 abstract 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
- B01D71/06—Organic material
- B01D71/58—Other polymers having nitrogen in the main chain, with or without oxygen or carbon only
- B01D71/62—Polycondensates having nitrogen-containing heterocyclic rings in the main chain
- B01D71/64—Polyimides; Polyamide-imides; Polyester-imides; Polyamide acids or similar polyimide precursors
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/22—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by diffusion
- B01D53/228—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by diffusion characterised by specific membranes
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L79/00—Compositions of macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing nitrogen with or without oxygen or carbon only, not provided for in groups C08L61/00 - C08L77/00
- C08L79/04—Polycondensates having nitrogen-containing heterocyclic rings in the main chain; Polyhydrazides; Polyamide acids or similar polyimide precursors
- C08L79/08—Polyimides; Polyester-imides; Polyamide-imides; Polyamide acids or similar polyimide precursors
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2205/00—Polymer mixtures characterised by other features
- C08L2205/02—Polymer mixtures characterised by other features containing two or more polymers of the same C08L -group
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
- Y02C20/00—Capture or disposal of greenhouse gases
- Y02C20/40—Capture or disposal of greenhouse gases of CO2
Abstract
The present invention provides a selectively gas permeable membrane that has a superior combination of permeability and selectively. The membrane compositi on includes a Type 1 copolyimide uniformly blended with a Type 2 copolyimide, which polymers are defined by chemical structure more specifically in this disclosure. The invention also provides a method of using the membrane of th e copolyimide blend to separate components of gas mixtures.
Claims (17)
1. A membrane for gas separation comprising a blend of at least one polymer of a Type 1 copolyimide and at least one polymer of a Type 2 copolyimide in which the Type 1 copolyimide comprises repeating units of formula I
in which R2 is a moiety having a composition selected from the group consisting of formula A, formula B, formula C and a mixture thereof, Z is a moiety having a composition selected from the group consisting of formula L, formula M, formula N and a mixture thereof; and R1 is a moiety having a composition selected from the group consisting of formula Q, formula S, formula T, and a mixture thereof, in which the Type 2 copolyimide comprises the repeating units of formulas IIa and IIb in which Ar is a moiety having a composition selected from the group consisting of formula U, formula V, and a mixture thereof, and in which X, X1, X2, X3 independently are hydrogen or an alkyl group having 1 to 6 carbon atoms, provided that at least two of X, X1, X2, or X3 on each of U and V are an alkyl group, Ar' is any aromatic moiety, R a and R b each independently have composition of formulas A, B, C, D or a mixture thereof, and Z is a moiety having composition selected from the group consisting of formula L, formula M, formula N and a mixture thereof.
in which R2 is a moiety having a composition selected from the group consisting of formula A, formula B, formula C and a mixture thereof, Z is a moiety having a composition selected from the group consisting of formula L, formula M, formula N and a mixture thereof; and R1 is a moiety having a composition selected from the group consisting of formula Q, formula S, formula T, and a mixture thereof, in which the Type 2 copolyimide comprises the repeating units of formulas IIa and IIb in which Ar is a moiety having a composition selected from the group consisting of formula U, formula V, and a mixture thereof, and in which X, X1, X2, X3 independently are hydrogen or an alkyl group having 1 to 6 carbon atoms, provided that at least two of X, X1, X2, or X3 on each of U and V are an alkyl group, Ar' is any aromatic moiety, R a and R b each independently have composition of formulas A, B, C, D or a mixture thereof, and Z is a moiety having composition selected from the group consisting of formula L, formula M, formula N and a mixture thereof.
2. The membrane of claim 1 in which the Type 1 copolyimide comprises repeating units of formula Ia.
3. The membrane of claim 2 in which R1 is formula Q in about 16% of the repeating units, formula S in about 64% of the repeating units and formula T
in about 20% of the repeating units.
in about 20% of the repeating units.
4. The membrane of claim 1 in which the Type 1 copolyimide comprises repeating units of formula Ib
5. The membrane of claim 4 in which R1 is a composition of formula Q in about 1-99 % of the repeating units, and of formula S in a complementary amount totaling 100 % of the repeating units.
6. The membrane of claim 1 in which the Type 1 copolyimide comprises repeating units having composition of formula Ia and repeating units having composition of formula Ib in which units of formula Ib constitute about 1 - 99% of the total repeating units of formulas Ia and Ib and in which R1 is a composition of formula Q in about 1-99% of the repeating units, and of formula S in a complementary amount totaling 100% of the repeating units.
7. The membrane of claim 6 in which the moiety R1 has a composition of formula Q in about 20% of the repeating units, and of formula S in about 80%
of the repeating units, and in which repeating units of formula Ib are about 40% of the total of repeating units of formulas Ia and Ib.
of the repeating units, and in which repeating units of formula Ib are about 40% of the total of repeating units of formulas Ia and Ib.
8. The membrane of claim 1 in which the ratio of Type 1 copolyimide to Type 2 copolyimide is greater than about 0.2.
9. The membrane of claim 8 in which the ratio of Type 1 copolyimide to Type 2 copolyimide is greater than about 1Ø
10. The membrane of claim 1 in which repeating units of formula IIa are at least about 25% of the total repeating units of formula IIa and IIb.
11. The membrane of claim 10 in which repeating units of formula IIa are at least about 50% of the total repeating units of formula IIa and IIb.
12. The membrane of claim 1 in which the Type 2 copolyimide is formed by polycondensation of an aromatic amine selected from the group consisting of 2,4-diaminomesitylene, 3,7-diamino-2,8-dimethyldiphenylsulfone and a mixture thereof, and a dianhydride selected from the group consisting of pyromellitic dianhydride, 3,3',4,4'-diphenylsulfone tetracarboxylic dianhydride, 3,3',4,4'-biphenyl tetracarboxylic dianhydride, 4,4'-(2,2,2-trifluoro-1-(trifluoromethyl)ethylidine)bis(1,2-benzene dicarboxylic acid dianhydride) and a mixture thereof.
13. The membrane of claim 1 in which the membrane is an asymmetric membrane.
14. The membrane of claim 13 in which the membrane is a hollow fiber.
15. A method of separating one or more gases from a gas mixture comprising (a) providing a gas separation membrane comprising a blend of at least one polymer of a Type 1 copolyimide and at least one polymer of a Type 2 copolyimide in which the Type 1 copolyimide comprises repeating units of formula I
in which R2 is a moiety having a composition selected from the group consisting of formula A, formula B, formula C and a mixture thereof, Z is a moiety having a composition selected from the group consisting of formula L, formula M, formula N and a mixture thereof; and R1 is a moiety having a composition selected from the group consisting of formula Q, formula S, formula T, and a mixture thereof, in which the Type 2 copolyimide comprises the repeating units of formulas IIa and IIb in which Ar is a moiety having a composition selected from the group consisting of formula U, formula V, and a mixture thereof, and in which X, X1, X2, X3 independently are hydrogen or an alkyl group having 1 to 6 carbon atoms, provided that at least two of X, X1, X2, or X3 on each of U and V are an alkyl group, Ar' is any aromatic moiety, R a and R b each independently have composition of formulas A, B, C, D or a mixture thereof, and Z is a moiety having composition selected from the group consisting of formula L, formula M, formula N and a mixture thereof, (b) contacting the gas mixture with one side of the gas separation membrane thereby causing more preferentially permeable gases of the mixture to permeate the membrane faster than less preferentially permeable gases to form a permeate gas mixture enriched in the more preferentially permeable gases on the opposite side of the membrane and a retentate gas mixture depleted in the more preferentially permeable gases on the one side of the membrane, and (c) withdrawing the permeate gas mixture and the retentate gas mixture separately from the membrane.
in which R2 is a moiety having a composition selected from the group consisting of formula A, formula B, formula C and a mixture thereof, Z is a moiety having a composition selected from the group consisting of formula L, formula M, formula N and a mixture thereof; and R1 is a moiety having a composition selected from the group consisting of formula Q, formula S, formula T, and a mixture thereof, in which the Type 2 copolyimide comprises the repeating units of formulas IIa and IIb in which Ar is a moiety having a composition selected from the group consisting of formula U, formula V, and a mixture thereof, and in which X, X1, X2, X3 independently are hydrogen or an alkyl group having 1 to 6 carbon atoms, provided that at least two of X, X1, X2, or X3 on each of U and V are an alkyl group, Ar' is any aromatic moiety, R a and R b each independently have composition of formulas A, B, C, D or a mixture thereof, and Z is a moiety having composition selected from the group consisting of formula L, formula M, formula N and a mixture thereof, (b) contacting the gas mixture with one side of the gas separation membrane thereby causing more preferentially permeable gases of the mixture to permeate the membrane faster than less preferentially permeable gases to form a permeate gas mixture enriched in the more preferentially permeable gases on the opposite side of the membrane and a retentate gas mixture depleted in the more preferentially permeable gases on the one side of the membrane, and (c) withdrawing the permeate gas mixture and the retentate gas mixture separately from the membrane.
16. The method of claim 15 in which the Type 1 copolyimide is P84, P84-HT325 or a mixture of them.
17. The method of claim 15 in which the gas mixture comprises carbon dioxide and methane.
Applications Claiming Priority (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US43027502P | 2002-12-02 | 2002-12-02 | |
US60/430,275 | 2002-12-02 | ||
US10/642,407 US7018445B2 (en) | 2002-12-02 | 2003-08-15 | Polyimide blends for gas separation membranes |
US10/642,407 | 2003-08-15 | ||
PCT/IB2003/004769 WO2004050223A2 (en) | 2002-12-02 | 2003-10-27 | Polyimide blends for gas separation membranes |
Publications (2)
Publication Number | Publication Date |
---|---|
CA2500346A1 true CA2500346A1 (en) | 2004-06-17 |
CA2500346C CA2500346C (en) | 2012-07-17 |
Family
ID=32474562
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA2500346A Expired - Lifetime CA2500346C (en) | 2002-12-02 | 2003-10-27 | Polyimide blends for gas separation membranes |
Country Status (8)
Country | Link |
---|---|
US (1) | US7018445B2 (en) |
EP (1) | EP1567250B1 (en) |
JP (1) | JP4249138B2 (en) |
AT (1) | ATE429971T1 (en) |
AU (1) | AU2003278411A1 (en) |
CA (1) | CA2500346C (en) |
DE (1) | DE60327461D1 (en) |
WO (1) | WO2004050223A2 (en) |
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US8083833B2 (en) * | 2006-03-10 | 2011-12-27 | Uop Llc | Flexible template-directed microporous partially pyrolyzed polymeric membranes |
US7846496B2 (en) * | 2006-03-10 | 2010-12-07 | Uop Llc | Mixed matrix membranes incorporating surface-functionalized molecular sieve nanoparticles and methods for making the same |
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-
2003
- 2003-08-15 US US10/642,407 patent/US7018445B2/en not_active Expired - Lifetime
- 2003-10-27 WO PCT/IB2003/004769 patent/WO2004050223A2/en active Application Filing
- 2003-10-27 AU AU2003278411A patent/AU2003278411A1/en not_active Abandoned
- 2003-10-27 JP JP2004570707A patent/JP4249138B2/en not_active Expired - Lifetime
- 2003-10-27 CA CA2500346A patent/CA2500346C/en not_active Expired - Lifetime
- 2003-10-27 DE DE60327461T patent/DE60327461D1/en not_active Expired - Lifetime
- 2003-10-27 EP EP03769717A patent/EP1567250B1/en not_active Expired - Lifetime
- 2003-10-27 AT AT03769717T patent/ATE429971T1/en not_active IP Right Cessation
Also Published As
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CA2500346C (en) | 2012-07-17 |
EP1567250A2 (en) | 2005-08-31 |
JP4249138B2 (en) | 2009-04-02 |
DE60327461D1 (en) | 2009-06-10 |
AU2003278411A8 (en) | 2004-06-23 |
WO2004050223A2 (en) | 2004-06-17 |
US7018445B2 (en) | 2006-03-28 |
US20040107830A1 (en) | 2004-06-10 |
WO2004050223A3 (en) | 2005-04-28 |
EP1567250B1 (en) | 2009-04-29 |
ATE429971T1 (en) | 2009-05-15 |
JP2006507939A (en) | 2006-03-09 |
AU2003278411A1 (en) | 2004-06-23 |
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