Method of making a high-performance supported gas separation molecular sieve membrane using a shortened crystallization time
View Patent ↗A method of making a supported gas separation molecular sieve membrane. In this method a porous support, which is preferably pretreated, is contacted with a molecular sieve synthesis mixture under hydrothermal synthesis conditions. The contacting step is conducted for a shortened crystallization time period. The resulting coated porous support is calcined to yield the supported gas separation molecular sieve membrane having particularly good gas separation characteristics.
1. A method of making a supported gas separation molecular sieve membrane, wherein said method comprises:
applying molecular sieve crystals to a surface of a porous support to thereby provide a seeded porous support surface;
contacting under hydrothermal synthesis conditions said seeded porous support surface with a synthesis gel mixture for a shortened crystallization time in the range of less than 15 hours so as to provide a coated porous support, wherein said synthesis gel comprises:
an aluminum source, a phosphorus source, a silicon source, a quaternary ammonium templating agent (R), and water in amounts such that the composition of said synthesis gel has the following molar ratios:
1Al 2 O 3 :a P 2 O 5 :b SiO 2 :c R: d H 2 O;
wherein:
a is from 0.01 to 52;
b is from 0.03 to 196;
c is from 0.2 to 5; and
d is from 20 to 300; and
calcining said coated porous support under calcination conditions including a calcination temperature in the range of from 250° C. to 650° C. to thereby provide said supported gas separation molecular sieve membrane that is characterized as having a CO 2 /CH 4 separation selectivity (based on a pressure driving force of 138 kPa and a temperature of 22° C.) of at least 100.
2. A method as recited in claim 1 , wherein said shortened crystallization time exceeding about 1 hour and said hydrothermal synthesis conditions include a hydrothermal synthesis temperature in the range of from 50° C. to 300° C. with the hydrothermal synthesis being conducted at autogenous pressure.
3. A method as recited in claim 1 , wherein said coated porous support includes a membrane layer having a membrane thickness in the range of from 0.001 μm to 50 μm and comprising SAPO-34 molecular sieve crystals.
4. A method as recited in claim 1 , wherein said porous support includes a porous material selected from a group consisting of inorganic porous materials, a stainless steel, a molybdenum alloy, and an austenitic nickel-chromium-based alloy.
5. A method as recited in claim 1 , wherein said supported gas separation molecular sieve membrane is further characterized as having a separation index (based on a pressure driving force of 138 kPa and a temperature of 22° C.) of at least 7.
6. A method as recited in claim 1 , wherein said CO 2 /CH 4 separation selectivity is at least 110.
7. A method as recited in claim 1 , wherein said shortened crystallization time exceeds 2 hours.
8. A method as recited in claim 1 , wherein said shortened crystallization time exceeds 3 hours but is less than 14 hours.
9. A supported gas separation molecular sieve membrane made by the method of claim 1 .
10. A process for separating a first gas component from a gas mixture comprising said first gas component and a second gas component, wherein said process comprises:
providing a gas separation molecular sieve membrane according to the method of claim 1 , said gas separation molecular sieve membrane comprising a feed side with a feed inlet and a retentate outlet and a permeate side, wherein said gas separation molecular sieve membrane is selectively permeable to said first gas component over said second gas component;
introducing said gas mixture to said feed inlet of said gas separation molecular sieve membrane; and
yielding a permeate stream from said permeate side of said gas separation molecular sieve membrane and a retentate stream from said retentate outlet, wherein said retentate stream is depleted of said first gas component and said permeate stream is rich in said first gas component.
11. A process as recited in claim 10 , wherein said coated porous support includes a membrane layer having a membrane thickness in the range of from 0.001 to 50 μm and comprising SAPO-34 molecular sieve crystals.
12. A process as recited in claim 10 , wherein said gas separation molecular sieve membrane comprises a porous support and said porous support includes a porous material selected from a group consisting of inorganic porous materials, a stainless steel, a molybdenum alloy and an austenitic nickel-chromium-based alloy.
13. A process as recited in claim 10 , wherein said supported gas separation molecular sieve membrane is further characterized as having a separation index (based on a pressure driving force of 138 kPa and a temperature of 22° C.) of at least 7.
14. A process as recited in claim 10 , wherein said CO 2 /CH 4 separation selectivity is at least 110.
15. A process for separating a first gas component from a gas mixture comprising said first gas component and a second gas component, wherein said process comprises:
providing a gas separation molecular sieve membrane system comprising a porous support coated with a membrane layer of silicoaluminophosphate 34 molecular sieve crystals and a thickness in the range of from 0.001 μm to 50 μm crystallized for a time in a range of less than 15 hours, the system having a feed side with a feed inlet and a retentate outlet and a permeate side, wherein said gas separation molecular sieve membrane system is selectively permeable to said first gas component over said second gas component;
introducing said gas mixture to said feed inlet of said gas separation molecular sieve membrane system; and
yielding a permeate stream from said permeate side of said gas separation molecular sieve membrane system and a retentate stream from said retentate outlet, wherein said retentate stream is depleted of said first gas component and said permeate stream is rich in said first gas component.
16. A process as recited in claim 15 , wherein the membrane layer has a thickness less than 20 μm.
17. A process as recited in claim 15 , wherein said porous support includes a porous material selected from a group consisting of inorganic porous materials, a stainless steel, a molybdenum alloy, and an austenitic nickel-chromium-based alloy.
18. A process as recited in claim 15 , wherein said supported gas separation molecular sieve membrane is further characterized as having a separation index (based on a pressure driving force of 138 kPa and a temperature of 22° C.) of at least 7.
19. A process as recited in claim 15 , wherein said CO 2 /CH 4 separation selectivity is at least 110.
20. A method as recited in claim 1 , wherein contacting said seeded porous support surface with a synthesis gel comprises contacting said seeded porous support surface with a synthesis gel mixture for a single crystallization time.
21. A process as recited in claim 15 , wherein the silicoaluminophosphate 34 molecular sieve crystals are crystallized in a single crystallization step.
22. A method as recited in claim 1 , wherein said porous support comprises a porous material selected from a group consisting of alumina, titania and zirconia.
23. A process as recited in claim 10 , wherein said gas separation molecular sieve membrane comprises a porous support and said porous support comprises a porous material selected from a group consisting of alumina, titania and zirconia.
24. A process as recited in claim 15 , wherein said porous support comprises a porous material selected from a group consisting of alumina, titania and zirconia.