US2013220119A1PendingUtilityA1
Crosslinked Membrane And Polymer For Making Same And Method Of Using Membrane
Est. expiryDec 20, 2021(expired)· nominal 20-yr term from priority
B01D 67/00931B01D 65/109B01D 67/00933B01D 71/643B01D 71/82B01D 69/08Y10S55/05B01D 53/228B01D 2257/504Y02C20/40B01D 2323/30
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Claims
Abstract
A composition of and a method of making high performance crosslinked membranes are described. The membranes have a high resistance to plasticization by use of crosslinking. The preferred polymer material for the membrane is a polyimide polymer comprising covalently bonded ester crosslinks. The resultant membrane exhibits a high permeability of CO 2 in combination with a high CO 2 /CH 4 selectivity. Another embodiment provides a method of making the membrane from a monesterified polymer followed by final crosslinking after the membrane is formed.
Claims
exact text as granted — not AI-modifiedWhat is claimed is:
1 . A hollow fiber polymer membrane, comprising:
a hollow fiber crosslinked polymer selected from the group consisting of polyimides, poyletherimides, polyethersulfones and polysulfones, having covalent ester crosslinks; and having a CO 2 permeance of at least 20 GPU and a CO 2 /CH 4 selectivity of greater than 20, at 35 degrees C. and a pressure of 100 psia.
2 . The hollow fiber polymer membrane of claim 1 wherein the polymer has an average molecular weight of between 20,000 and 200,000.
3 . The hollow fiber polymer membrane of claim 1 wherein the membrane material has an average molecular weight greater than the entanglement MW of the polymer.
4 . The hollow fiber polymer membrane of claim 1 wherein:
the polymer is made from the monomers A+B+C; where A is a dianhydride of the formula;
where X 1 and X 2 are the same or different halogenated alkyl group, phenyl or halogen;
where R 1 , R 2 , R 3 , R 4 , R 5 , and R 6 are H, alkyl, or halogen;
where B is a diamino cyclic compound without a carboxylic acid functionality;
where C is a diamino cyclic compound with a carboxylic acid functionality;
wherein the ratio of B to C is between 1:4 and 8:1.
5 . A method of making a crosslinked hollow fiber membrane comprising:
preparing a polymer comprising a predetermined quantity of crosslinkable sites, the polymer selected from the group consisting of polyimides, poyletherimides, polyethersulfones and polysulfones, having covalent ester crosslinks having a CO 2 permeance of at least 20 GPU and a CO 2 /CH 4 selectivity of greater than 20, at 35 degrees C. and a pressure of 100 psi; and forming a hollow fiber from the polymer.
6 . A process for producing hydrocarbon products comprising:
separating two gases having different molecular sizes in a feedstream including these two gas components, the process including: (a) providing a hollow fiber crosslinked polymer selected from the group consisting of polyimides, poyletherimides, polyethersulfones and polysulfones, having covalent ester crosslinks; and having a CO 2 permeance of at least 20 GPU and a CO 2 /CH 4 selectivity of greater than 20, at 35 degrees C. and a pressure of 100 psi and (b) directing a feedstream including the first and second gas components to the feed side of the membrane and withdrawing a retentate stream depleted in the first gas component and withdrawing a permeate stream enriched in the first gas component from the permeate side of the membrane.
7 . A hollow fiber polymer membrane, comprising:
a hollow fiber polymer membrane including a porous support layer and a skin layer which is supported by the support layer, the skin layer including a crosslinked polymer selected from the group consisting of polyimides, poyletherimides, polyethersulfones and polysulfones and having covalent ester crosslinks; wherein the hollow fiber polymer membrane has a CO 2 permeance of at least 20 GPU and a CO 2 /CH 4 selectivity of greater than 20, at 35 degrees C. and a pressure of 100 psia.Cited by (0)
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