Membrane-forming dope for carbon membranes and a method for producing a carbon hollow fiber membrane using the same
US-10150085-B2 · Dec 11, 2018 · US
US11517857B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11517857-B2 |
| Application number | US-201816634401-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 20, 2018 |
| Priority date | Aug 14, 2017 |
| Publication date | Dec 6, 2022 |
| Grant date | Dec 6, 2022 |
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A method of making a hollow fiber carbon molecular sieve is comprised of heating a hollow polymer fiber to a carbonization temperature in an atmosphere that is non-oxidizing to form a hollow fiber carbon molecular sieve, wherein during at least a portion of the heating a tensile force is applied to the hollow polymer fiber. The method may improve the separation of gases similar in size such a propylene from propane.
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What is claimed is: 1. A method of making a hollow fiber carbon molecular sieve membrane comprising, (i) providing a hollow polymer fiber comprised of a polyimide, wherein the polyimide is the reaction product of a dianhydride and a diamine, and wherein the dianhydride is comprised of an aromatic dianhydride that has no rotational freedom within the dianhydride, (ii) heating the hollow polymer fiber to a carbonization temperature in an atmosphere that is non-oxidizing to form a hollow fiber carbon molecular sieve, wherein during at least a portion of the heating a tensile force is applied to the hollow polymer fiber along a length of the hollow polymer fiber to form the hollow fiber carbon molecular sieve membrane. 2. The method of claim 1 , wherein the tensile force is applied throughout the heating of the fiber. 3. The method of claim 1 , wherein the atmosphere is nitrogen, inert gas, mixture of any of the preceding gases, or mixture of the preceding gases having oxygen in an amount of less than 300 ppm. 4. The method of claim 1 , wherein the tensile force is applied until a set elongation of the hollow polymer fiber is reached during the heating. 5. The method of claim 1 , wherein prior to heating to the carbonization temperature, the hollow polymer fiber is heated to a pre-treatment temperature below the carbonization temperature. 6. The method of claim 5 , wherein, at least during a portion of the heating to the pretreatment temperature, a tensile force is applied to the hollow polymer fiber. 7. The method of claim 1 , wherein the polyimide has a storage modulus minimum at a temperature greater than 250° C. that is less than the storage modulus at a temperature of 250° C., but no more than ten times less measured using dynamic mechanical thermal analysis from 250° C. to a temperature where the polyimide carbonizes. 8. The method of claim 7 , wherein the storage modulus minimum is at most 7.5 times less than the storage modulus at 250° C. 9. The method of claim 7 , wherein the storage modulus minimum is at most 5 times less than storage modulus at 250° C. 10. The method of claim 1 , wherein the dianhydride is comprised of the dianhydride that has no rotational freedom within the dianhydride and a diahydride that has rotational freedom within the dianhydride. 11. A method of making a hollow fiber carbon molecular sieve membrane comprising, (i) providing a hollow polymer fiber comprised of a polyimide, (ii) heating the hollow fiber polymer to a carbonization temperature in an atmosphere that is non-oxidizing to form a hollow fiber carbon molecular sieve, wherein during at least a portion of the heating a tensile force is applied to the hollow fiber along a length of the hollow polymer fiber to form the hollow fiber carbon molecular sieve membrane, wherein the polyimide is represented by: where X is 0.1 to 0.9 and Y is 0.1 to 0.9 and X+Y=1 and n is an integer that may be any that realizes a molecular weight of 30 to 200 kDa. 12. The method of claim 11 , wherein X is 0.1 to 0.35 and Y is 0.65 to 0.9. 13. A process for separating a gas molecule from a gas feed comprised of the gas molecule and at least one other gas molecule comprising (i) providing the hollow fiber carbon molecular sieve produced by any one of the the method of claim 1 ; and (ii) flowing the gas feed through said hollow fiber carbon molecular sieve to produce a first stream having an increased concentration of the gas molecule and a second stream having an increased concentration of the other gas molecule. 14. The process of claim 13 , wherein the gas molecule and other gas molecule is: hydrogen and ethylene; ethylene and ethane; propylene and propane; oxygen and nitrogen; hydrogen and methane; carbon dioxide and nitrogen; or carbon dioxide and methane. 15. The method of claim 14 , wherein the gas molecule and other gas molecule is propylene and propane. 16. A gas separating module comprising a sealable enclosure comprised of: a plurality of hollow fiber carbon molecular sieves, comprising at least one hollow fiber carbon molecular sieve produced by the method of claim 1 , contained within the sealable enclosure; an inlet for introducing a gas feed comprised of at least two differing gas molecules; a first outlet for permitting egress of a permeate gas stream; and a second outlet for egress of a retentate gas stream.
characterised by specific membranes · CPC title
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