IP Library Granted Patent US 8,388,744
Granted Patent B1
US 8,388,744 · App. 13/221,657 · Granted Mar 5, 2013

Systems and methods for using a boehmite bond-coat with polyimide membranes for gas separation

Inventor: Kimberly Ann Polishchuk (Niskayuna, NY)
Assignee: General Electric Company
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Quick Facts
Patent No.
US 8,388,744
App. No.
13/221,657
Granted
Mar 5, 2013
Kind
B1
Abstract

The subject matter disclosed herein relates to gas separation membranes and, more specifically, to polyimide gas separation membranes. In an embodiment, a gas separation membrane includes a porous substrate, a substantially continuous polyimide membrane layer, and one or more layers of boehmite nanoparticles disposed between the porous substrate and the polyimide membrane layer to form a bond-coat layer. The bond-coat layer is configured to improve the adhesion of the polyimide membrane layer to the porous substrate, and the polyimide membrane layer has a thickness approximately 100 nm or less.

Claims (31)

1. A gas separation membrane comprising:

a porous substrate;

a substantially continuous polyimide membrane layer; and

one or more layers of boehmite nanoparticles disposed between the porous substrate and the polyimide membrane layer to form a bond-coat layer, wherein the polyimide membrane layer has a thickness approximately 100 nm or less.

2. The gas separation membrane of claim 1 , wherein the bond-coat layer is configured to improve the adhesion of the polyimide membrane layer to the porous substrate.

3. The gas separation membrane of claim 1 , wherein the boehmite nanoparticles are substantially between approximately 40 nm and 60 nm in diameter.

4. The gas separation membrane of claim 1 , wherein the one or more layers of boehmite nanoparticles form a contiguous bond-coat layer on the porous substrate.

5. The gas separation membrane of claim 1 , wherein the polyimide membrane layer has a thickness between approximately 20 nm and 100 nm.

6. The gas separation membrane of claim 1 , wherein the gas separation membrane has a hydrogen to carbon dioxide selectivity ratio greater than approximately 4.7 and a hydrogen permeance greater than approximately 10 GPU.

7. The gas separation membrane of claim 1 , wherein the gas separation membrane has a hydrogen permeance greater than approximately 350 GPU at 250° C.

8. The gas separation membrane of claim 1 , wherein the gas separation membrane has a hydrogen to carbon dioxide selectivity ratio greater than approximately 5.

9. A method of manufacturing a gas separation membrane comprising:

depositing one or more layers of boehmite nanoparticles onto a porous support structure to form a bond-coat layer; and

depositing a polyimide precursor onto the bond-coat layer; and

performing a thermal treatment of the bond-coat layer and the polyimide precursor at approximately 300° C. or less to form a polyimide membrane layer, wherein the polyimide membrane layer has a thickness approximately 150 nm or less.

10. The method of claim 9 , wherein the support structure comprises a porous ceramic or metallic substrate having a pore size less than approximately 40 nm.

11. The method of claim 9 , wherein the one or more layers of boehmite particles are deposited on the porous support structure using a wet processing method comprising spin-coating, dip-coating, or spray-coating.

12. The method of claim 9 , wherein the bond-coat layer has a thickness between approximately 50 nm and 400 nm.

13. The method of claim 9 , wherein the thermal treatment of the bond-coat layer and the polyimide precursor to form the polyimide membrane layer is performed between approximately 200° C. and 300° C.

14. The method of claim 9 , wherein the polyimide layer has a thickness between approximately 20 nm and 100 nm.

15. The method of claim 9 , wherein the polyimide precursor comprises a polyamic acid solution.

16. The method of claim 15 , wherein the polyimide precursor is deposited on the porous support structure using a wet processing method comprising spin-coating, dip-coating, or spray-coating of the polyamic acid solution.

17. A membrane for gas separation comprising:

a support layer;

an intermediate layer disposed on top of the support layer and providing a surface having a pore size less than approximately 40 nm and having a thickness between approximately 50 and 400 nm;

a bond-coat layer comprising boehmite nanoparticles disposed on top of the intermediate layer and having a thickness between approximately 50 nm and 400 nm; and

a polyimide membrane layer disposed on top of the bond-coat layer having a thickness between approximately 20 and 150 nm.

18. The membrane of claim 17 , wherein the support layer comprises a porous ceramic or metallic substrate having a pore size greater than approximately 30 nm.

19. The membrane of claim 17 , wherein the support layer, the intermediate layer, or both, comprise alumina or silica.

20. The membrane of claim 17 , wherein the membrane has a hydrogen permeance greater than 350 GPU at 250° C.

21. The membrane of claim 17 , wherein the bond-coat layer enhances the adhesion between the polyimide membrane layer and the intermediate layer.

Assignments (2)
CONFIRMATORY LICENSE Recorded Dec 13, 2012
From: GE GLOBAL RESEARCH
To: ENERGY, UNITED STATES DEPARTMENT OF
Reel/Frame 029496/0200 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 30, 2011
From: POLISHCHUK, KIMBERLY ANN
To: GENERAL ELECTRIC COMPANY
Reel/Frame 026831/0330 →