High Flux Mixed Matrix Membranes for Separations

Abstract

The present invention discloses a new class of high flux mixed matrix membranes that are made by incorporating porous inorganic fillers (e.g. microporous and mesoporous molecular sieves, carbon molecular sieves, porous metal-organic frameworks) into a high flux high surface area microporous organic polymer matrix. These microporous organic polymers are referred to as “polymers of intrinsic microporosity” or PIMs. The high flux membranes are promising for a wide range of separations including liquid separations such as pervaporation of phenol/water and also gas separations in the petrochemical, refinery, and natural gas industries such as methane/carbon dioxide, olefin/paraffin and iso/normal paraffins separations.

Description

Claims

1. A process for separating at least one gas from a mixture of gases, the process comprising: a) providing a mixed matrix gas separation membrane comprising a porous inorganic filler material dispersed in a continuous phase consisting essentially of an organic microporous polymer which is permeable to said at least one gas;b) contacting the mixture on one side of the mixed matrix membrane to cause said at least one gas to permeate the mixed matrix membrane; andc) removing from the opposite side of the membrane a permeate gas composition comprising a portion of said at least one gas which permeated said membrane.

2. The process of claim 1 wherein said organic microporous polymer material consists essentially of organic macromolecules comprised of first generally planar species connected by rigid linkers predominantly to a maximum of two other said first species, said rigid linkers having a point of contortion such that two adjacent first planar species connected by the linker are held in non-coplanar orientation.

3. The process of claim 2 wherein said point of contortion is provided by a substituted or unsubstituted spiro-indane, bicyclo-octane, biphenyl or binaphthyl moiety.

4. The process of claim 2 wherein each of the first planar species comprises at least one aromatic ring.

5. The process of claim 1 wherein said porous inorganic filler material is selected from the group consisting of microporous molecular sieves, mesoporous molecular sieves, carbon molecular sieves and porous metal-organic frameworks.

6. The process of claim 5 wherein said microporous molecular sieves are selected from the group consisting of NaX, NaA, AlPO-18, AlPO-14, SAPO-34, SAPO-18, AlPO-17, AlPO-25, AlPO-EN3, AlPO-34, SAPO-44, SAPO-47, SAPO-17, CVX-7, SAPO-35, SAPO-56, AlPO-52, SAPO-43, SSZ-62, SSZ-13, UZM-5, MAPO-34, UZM-9, UZM-26, UZM-27, UZM-25, CDS-1, Nu-6(2), silicalite, Si-MEL, MCM-65, MCM-47, Si-DDR, Si-BEA, 3A, 4A, ITO-3, ITQ-12, Si-CHA, 5A, and mixtures thereof.

7. The process of claim 5 wherein said mesoporous molecular sieves are selected from the group consisting of MCM-41, SBA-15, and surface functionalized MCM-41 and SBA-15 molecular sieves.

8. The process of claim 5 wherein said porous inorganic filler material is a metal organic framework material.

9. The process of claim 1 wherein said mixture of gases comprises a pair of gases selected from the group consisting of hydrogen/methane, carbon dioxide/methane, carbon dioxide/nitrogen, methane/nitrogen and olefin/paraffin.

10. A mixed matrix membrane comprising a porous inorganic filler material dispersed in a continuous phase consisting essentially of an organic microporous polymer.

11. The mixed matrix membrane of claim 10 wherein said microporous polymer material consists essentially of organic macromolecules comprised of first generally planar species connected by rigid linkers predominantly to a maximum of two other said first species, said rigid linkers having a point of contortion such that two adjacent first planar species connected by the linker are held in non-coplanar orientation.

12. The mixed matrix membrane of claim 11 wherein the point of contortion of said microporous polymer material is provided by a substituted or unsubstituted spiro-indane, bicyclo-octane, biphenyl or binaphthyl moiety.

13. The mixed matrix membrane of claim 11 wherein each of the first planar species comprises at least one aromatic ring.

14. The mixed matrix membrane of claim 11 wherein each of the first planar species comprises a substituted or unsubstituted moiety of the formula:

15. The mixed matrix membrane of claim 11 wherein the microporous polymer material comprises repeating units of formula:

16. The mixed matrix membrane of claim 11 wherein the microporous polymer material comprises repeating units of formula:

17. The mixed matrix membrane of claim 11 wherein the microporous polymer material comprises repeating units of formula:

18. The mixed matrix membrane of claim 11 wherein the microporous polymer material comprises repeating units of formula:

19. The mixed matrix membrane of claim 11 wherein the microporous polymer material comprises repeating units of formula:

20. The mixed matrix membrane of claim 10 wherein said porous inorganic filler material is selected from the group consisting of microporous molecular sieves, mesoporous molecular sieves, carbon molecular sieves and porous metal-organic frameworks.

21. The mixed matrix membrane of claim 20 wherein said microporous molecular sieves are selected from the group consisting of NaX, NaA, AlPO-18, AlPO-14, SAPO-34, SAPO-18, AlPO-17, AlPO-25, AlPO-EN3, AlPO-34, SAPO-44, SAPO-47, SAPO-17, CVX-7, SAPO-35, SAPO-56, AlPO-52, SAPO-43, SSZ-62, SSZ-13, UZM-5, MAPO-34, UZM-9, UZM-26, UZM-27, UZM-25, CDS-1, Nu-6(2), silicalite, Si-MEL, MCM-65, MCM-47, Si-DDR, Si-BEA, 3A, 4A, ITO-3, ITQ-12, Si-CHA, 5A, and mixtures thereof.

22. The mixed matrix membrane of claim 20 wherein said mesoporous molecular sieves are selected from the group consisting of MCM-41, SBA-15, and surface functionalized MCM-41 and SBA-15 molecular sieves.

23. The mixed matrix membrane of claim 20 wherein said porous inorganic filler material is a metal organic framework material.