IP Library Granted Patent US 11,772,052
Granted Patent B2
US 11,772,052 · App. 17/276,368 · Granted Oct 3, 2023

Membranes for gas separation

Inventors: W. S. Winston Ho (Columbus, OH); Yang Han (Columbus, OH)
Assignee: OHIO STATE INNOVATION FOUNDATION
B01D69/148B01D53/228B01D67/0079B01D69/10B01D71/021B01D71/44B01D71/60B01D2257/504B01D2258/0283B01D2311/13B01D2315/10B01D2323/30B01D2325/36
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Quick Facts
Patent No.
US 11,772,052
App. No.
17/276,368
Granted
Oct 3, 2023
Kind
B2
Abstract

Membranes, methods of making the membranes, and methods of using the membranes are described herein. The membranes can comprise a support layer, and a selective polymer layer disposed on the support layer. The selective polymer layer can comprise a selective polymer matrix and carbon nanotubes dispersed within the selective polymer matrix. The carbon nanotubes can comprise multi-walled carbon nanotubes wrapped in a hydrophilic polymer, such as polyvinylpyrrolidone or a copolymer thereof, such as poly(1-vinylpyrrolidone-co-vinyl acetate). The membranes can exhibit selective permeability to gases. As such, the membranes can be for the selective removal of carbon dioxide and/or hydrogen sulfide from hydrogen and/or nitrogen.

Claims (26)

1. A membrane comprising:

a support layer; and

a selective polymer layer disposed on the support layer;

wherein the selective polymer layer comprises a selective polymer matrix and carbon nanotubes dispersed within the selective polymer matrix,

wherein the selective polymer matrix comprises an amine-containing polymer and a mobile carrier comprising 2-(1-piperazinyl)ethylamine-sarcosine salt (PZEA-Sar) and 2-(1-piperazinyl)ethylamine-aminoisobutyric acid (PZEA-AIBA); and

wherein the carbon nanotubes are wrapped in a hydrophilic polymer.

2. The membrane of claim 1 , wherein the selective polymer matrix has a CO 2 :N 2 selectivity of from 10 to 500 at 57° C. and 1 atm feed pressure.

3. The membrane of claim 1 , wherein the amine-containing polymer is selected from the group consisting of polyvinylamine, polyallylamine, polyethyleneimine, poly-N-isopropylallylamine, poly-N-tert-butylallylamine, poly-N-1,2-dimethylpropylallylamine, poly-N-methylallylamine, poly-N,N-dimethylallylamine, poly-2-vinylpiperidine, poly-4-vinylpiperidine, polyaminostyrene, chitosan, copolymers, and blends thereof.

4. The membrane of claim 1 , wherein the hydrophilic polymer comprises a polymer selected from the group consisting of polyvinylalcohol, polyvinylacetate, polyethylene oxide, polyvinylpyrrolidone, polyacrylamine, a polyamine, polysiloxane, copolymers thereof, and blends thereof.

5. The membrane of claim 1 , wherein the selective polymer matrix further comprises a cross-linking agent selected from the group consisting of formaldehyde, glutaraldehyde, maleic anhydride, glyoxal, divinylsulfone, toluenediisocyanate, trimethylol melamine, terephthalatealdehyde, epichlorohydrin, vinyl acrylate, and combinations thereof.

6. The membrane of claim 1 , wherein the carbon nanotubes comprise single-walled carbon nanotubes or multiwalled carbon nanotubes.

7. The membrane of claim 1 , wherein the selective polymer layer comprises from 0.5% to 5% by weight carbon nanotubes, based on the total dry weight of the selective polymer layer.

8. The membrane of claim 1 , wherein the carbon nanotubes have an average diameter of from 10 nm to 50 nm.

9. The membrane of claim 1 , wherein the carbon nanotubes have an average length of from 50 nm to 20 μm.

10. The membrane of claim 1 , wherein the carbon nanotubes comprise sidewall functionalized carbon nanotubes.

11. The membrane of claim 1 , wherein the support layer comprises a gas permeable polymer.

12. The membrane of claim 11 , wherein the gas permeable polymer comprises a polymer chosen from polyamides, polyimides, polypyrrolones, polyesters, sulfone-based polymers, nitrile-based polymers, polymeric organosilicones, fluorinated polymers, polyolefins, copolymers thereof, and blends thereof.

13. The membrane of claim 1 , wherein the support layer comprises a gas permeable polymer disposed on a base.

14. The membrane of claim 1 , wherein the membrane further comprises a permeable layer disposed between the support layer and the selective polymer layer.

15. A method for separating a first gas from a feed gas stream, the method comprising contacting a membrane defined by claim 1 with the feed gas stream comprising the first gas under conditions effective to afford transmembrane permeation of the first gas.

16. A method of making a membrane comprising depositing a selective polymer layer on a support layer, the selective polymer layer comprising a selective polymer matrix and carbon nanotubes dispersed within the selective polymer matrix,

wherein the selective polymer matrix comprises an amine-containing polymer and a mobile carrier comprising 2-(1-piperazinyl)ethylamine-sarcosine salt (PZEA-Sar) and 2-(1-piperazinyl)ethylamine-aminoisobutyric acid (PZEA-AIBA); and

wherein the carbon nanotubes are wrapped in a hydrophilic polymer.

17. The membrane of claim 1 , wherein the hydrophilic polymer comprises a polymer selected from the group consisting of polyallylamine, polyvinyl amine, polyethylenimine, copolymers thereof, and blends thereof.

18. The membrane of claim 10 , wherein the sidewall functionalized carbon nanotubes comprise hydroxy-functionalized carbon nanotubes, carboxy-functionalized carbon nanotubes, amine-functionalized carbon nanotubes, or a combination thereof.

19. The membrane of claim 13 , wherein the base comprises a non-woven fabric.

Assignments (2)
CONFIRMATORY LICENSE Recorded Apr 26, 2021
From: OHIO STATE UNIVERSITY
To: UNITED STATES DEPARTMENT OF ENERGY
Reel/Frame 056107/0351 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 15, 2021
From: HO, W.S. WINSTON; HAN, YANG
To: OHIO STATE INNOVATION FOUNDATION
Reel/Frame 055597/0420 →
Continuity (2)
Provisional Application 62731790 · Sep 14, 2018
Related Publication 20220032239A1 · Feb 3, 2022
Cited By (1)
US 12,447,436