Monolayer, composite, gas separation material, filter, gas separation device and method for manufacturing composite
US-12128366-B2 · Oct 29, 2024 · US
US11420154B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11420154-B2 |
| Application number | US-201917051620-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 3, 2019 |
| Priority date | May 2, 2018 |
| Publication date | Aug 23, 2022 |
| Grant date | Aug 23, 2022 |
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The invention is an improved method of making an improved carbon molecular sieve (CMS) membrane in which a precursor polymer (e.g., polyimide) is pyrolyzed at a pyrolysis temperature to form a CMS membrane that is cooled to ambient temperature (about 40° C. or 30° C. to about 20° C.). The CMS membrane is then reheated to a reheating temperature less than the pyrolysis temperature to form the improved CMS membrane. The improved CMS membranes have shown an improved combination of selectivity and permeance as well as stability for separating hydrogen from gas molecules (e.g., methane, ethane, propane, ethylene, propylene, butane, carbon dioxide, nitrogen, butylene, and combinations thereof).
Opening claim text (preview).
What is claimed is: 1. A method of making a carbon molecular sieve membrane comprising, (i) providing a precursor polymer; (ii) heating said precursor polymer to a pyrolysis temperature where the precursor polymer undergoes pyrolysis to form the carbon molecular sieve membrane; (iii) cooling the carbon molecular sieve membrane to a cooling temperature less than or equal to 50° C.; and (iv) after the cooling, heating the carbon molecular sieve membrane to a reheating temperature of at least 60° C. to at most 200° C. for a reheating time from 30 minutes to 500 hours under a reheating atmosphere and then (v) cooling back to below 50° C.; wherein there is a pressure differential across the carbon molecular sieve membrane such that the reheating atmosphere is drawn through the carbon molecular sieve membrane during reheating. 2. The method of claim 1 , wherein the reheating temperature is from 90° C. to 200° C. 3. The method of claim 1 , wherein the reheating time is 1 hour to 25 hours. 4. The method of claim 1 , wherein the cooling temperature is from 20 to 30° C. 5. The method of claim 1 , wherein the reheating atmosphere is an inert gas, nitrogen, air or mixture thereof. 6. The method of claim 1 , wherein the reheating atmosphere is at atmospheric pressure or above. 7. The method of claim 1 , wherein the reheating atmosphere is at a pressure above atmospheric pressure. 8. The method of claim 1 , wherein the pressure differential is from 1 to 100 pounds per square inch. 9. The method of claim 1 , wherein the precursor polymer is a polyimide. 10. A method for separating hydrogen from a gas feed comprised of hydrogen and at least one other gas molecule comprising (i) providing the carbon molecular sieve membrane made by the method of claim 1 ; and (ii) flowing the gas feed through said carbon molecular sieve membrane to produce a first stream having an increased concentration of hydrogen and a second stream having an increased concentration of the other gas molecule. 11. The process of claim 10 , wherein the other gas molecule is comprised of at least one of the following: ethylene, ethane, propylene, propane, oxygen, nitrogen, carbon dioxide, methane, butane or butylene. 12. The method of claim 11 , wherein the other gas molecule is comprised of at least one of ethylene, ethane, propylene or propane.
by using hydrogen storage media (reversible storage of hydrogen C01B3/0005) · CPC title
Thermal after-treatment · CPC title
characterised by specific membranes · CPC title
with hollow fibres · CPC title
Methane · CPC title
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