Polyimide-based carbon molecular sieve membrane for ethylene/ethane separations

• US 8,911,534 B2
• Filed: 02/28/2012
• Issued: 12/16/2014
• Est. Priority Date: 03/07/2011
• Status: Active Grant

• Current Assignee: Georgia Tech Research Corporation (University System of Georgia)
• Original Assignee: Georgia Tech Research Corporation (University System of Georgia)
• Inventors: Koros, William J., Rungta, Meha, Xu, Liren
• Primary Examiner(s): Greene, Jason M
• Assistant Examiner(s): SHUMATE, ANTHONY R
• Application Number:
  US13/980,402
• Publication Number:
  US 20130333562A1
• Time in Patent Office: 1,022 Days
• Field of Search: 95/43, 95/45, 95/50, 96/4, 96/8, 96/10
• US Class Current: 95/50
• CPC Class Codes: B01D 2256/16 Hydrogen
• CPC Class Codes: B01D 2257/7025 Methane
• CPC Class Codes: B01D 2323/08 Specific temperatures applied
• CPC Class Codes: B01D 2323/081 Heating
• CPC Class Codes: B01D 53/228 characterised by specific membranes
• CPC Class Codes: B01D 67/0067 by carbonisation or pyrolysis
• CPC Class Codes: B01D 71/021 Carbon
• CPC Class Codes: B01D 71/028 Molecular sieves carbon B01D71/021
• CPC Class Codes: B01D 71/0281 Zeolites
• CPC Class Codes: Y02C 20/20 of methane

Abstract

Carbon molecular sieve membranes having desirable selectivity for ethylene/ethane separations are prepared from a 3,3′,4,4′-benzophenonetetracarboxylic acid dianhydride 5(6)-amino-1-(4′-aminophenyl)-1,3,3-trimethylindane 4,4-bismaleimidodiphenyl-methane (BTDA-DAPI) precursor solution that is then formed into films or hollow fibers which are pyrolyzed under vacuum or an inert atmosphere to form carbon molecular sieve membranes. Pyrolysis condition variables, including ramp rate, thermal soak time and temperature, are used to optimize the membrane'"'"'s separation performance.

Claims

1. An ethane/ethylene separation membrane prepared by a process comprising dissolving an amount of 3,3′

,4,4′

-benzophenone tetracarboxylic dianhydride 5(6)-amino-1-(4′

-aminopheny)-1,3,3-trimethylindane in a solvent such that a solution is formed;

forming asymmetric hollow fiber precursors from the solution;

at least partially drying the asymmetric hollow fiber precursors with a second solvent;

solvent-exchanging the asymmetric hollow fiber precursors in hexane; and

at least partially pyrolyzing the asymmetric hollow fiber precursors under vacuum or in an inert atmosphere to form an asymmetric hollow fiber carbon molecular sieve membrane therefrom, the asymmetric hollow fiber carbon molecular sieve membrane having an ethylene permeance of at least 0.25 Gas Permeation Units and an ethylene/ethane selectivity of at least 6.3.

2. The membrane of claim 1 wherein the pyrolyzing is carried out to a temperature ranging from 500°

C. to 800°

C.

3. The membrane of claim 1 wherein the pyrolyzing is carried out to a temperature ranging from 650°

C. to 700°

C.

4. The membrane of claim 1 wherein the pyrolyzing is done according to a protocol wherein the asymmetric hollow fibers are heated first from 50°

C. to 600°

C. at a ramp rate of 10°

C./minute;

then from 600°

C. to 675°

C. at a ramp rate of 2°

C./minute;

then soaked for 10 minutes at 675°

C.

5. A process for separating ethane and ethylene from one another comprising flowing a mixture of gases including ethane and ethylene through an ethane/ethylene separation membrane prepared by a process including dissolving an amount of 3,3′

,4,4′

-benzophenone tetracarboxylic dianhydride 5(6)-amino-1-(4′

-aminopheny)-1,3,3-trimethylindane in a solvent such that a solution is formed;

forming asymmetric hollow fiber precursors from the solution;

at least partially drying the asymmetric hollow fiber precursors with a second solvent;

solvent-exchanging the asymmetric hollow fiber precursors in hexane; and

at least partially pyrolyzing the asymmetric hollow fiber precursors under vacuum or in an inert atmosphere to form an asymmetric hollow fiber carbon molecular sieve membrane therefrom, the asymmetric hollow fiber carbon molecular sieve membrane having an ethylene permeance of at least 0.25 Gas Permeation Units and an ethylene/ethane selectivity of at least 6.3;

under conditions such that the ethylene and the ethane are separated from one another.

6. The process of claim 5 wherein the carbon molecular sieve membrane has an ethylene permeance of at least 0.25 Gas Permeation Units and an ethylene/ethane selectivity of at least 9.

7. The process of claim 5 wherein the carbon molecular sieve membrane has an ethylene permeance of at least 0.5 Gas Permeation Units and an ethylene/ethane selectivity of at least 10.

8. The process of claim 5 wherein the carbon molecular sieve membrane has an ethylene permeance of at least 1 Gas Permeation Units and an ethylene/ethane selectivity of at least 12.