Porous asymmetric polyphenylene ether membranes and associated separation modules and methods
원문보기
IPC분류정보
국가/구분
United States(US) Patent
등록
국제특허분류(IPC7판)
A61M-001/16
C02F-001/44
C07K-001/34
B01D-061/14
B01D-061/36
B01D-063/02
B01D-067/00
B01D-069/02
B01D-069/06
B01D-069/08
B01D-069/12
B01D-071/28
B01D-071/52
B01D-071/56
B01D-071/76
B01D-071/78
B01D-071/80
C08B-037/00
C02F-101/32
출원번호
US-0302276
(2015-04-30)
등록번호
US-10252220
(2019-04-09)
국제출원번호
PCT/US2015/028546
(2015-04-30)
국제공개번호
WO2015/168423
(2015-11-05)
발명자
/ 주소
Berzinis, Albin Peter
Bajaj, Pooja
Halbfinger, Rachel Elizabeth
Bikel, Matias
출원인 / 주소
SABIC GLOBAL TECHNOLOGIES B.V.
대리인 / 주소
Cantor Colburn LLP
인용정보
피인용 횟수 :
0인용 특허 :
36
초록▼
A porous asymmetric membrane comprises a hydrophobic polymer comprising a poly(phenylene ether) or poly(phenylene ether) copolymer; and a polymer additive. A separation module can be fabricated from the porous asymmetric membrane. A method of forming the porous asymmetric membrane comprises: dissolv
A porous asymmetric membrane comprises a hydrophobic polymer comprising a poly(phenylene ether) or poly(phenylene ether) copolymer; and a polymer additive. A separation module can be fabricated from the porous asymmetric membrane. A method of forming the porous asymmetric membrane comprises: dissolving a hydrophobic polymer comprising a poly(phenylene ether) or poly(phenylene ether) copolymer and, a polymer additive in a water-miscible polar aprotic solvent to form a porous asymmetric membrane-forming composition; and phase-inverting the porous asymmetric membrane forming-composition in a first non-solvent composition to form the porous asymmetric membrane. The polymer additive comprises hydrophilic functional groups, copolymerized hydrophilic monomers, or blocks of hydrophilic monomer repeat units. For example, the polymer additive can comprise a hydrophilic polymer or amphiphilic polymer. The porous asymmetric membrane can be a flat membrane or hollow fiber.
대표청구항▼
1. A porous asymmetric membrane, comprising a poly(phenylene ether) copolymer comprising repeat units derived from 2,6-dimethylphenol and repeat units derived from 2-methyl-6-phenylphenol, and having an intrinsic viscosity of 0.7 to 1.5 deciliters per gram, measured in chloroform at 25° C. and a wei
1. A porous asymmetric membrane, comprising a poly(phenylene ether) copolymer comprising repeat units derived from 2,6-dimethylphenol and repeat units derived from 2-methyl-6-phenylphenol, and having an intrinsic viscosity of 0.7 to 1.5 deciliters per gram, measured in chloroform at 25° C. and a weight average molecular weight of 100,000 to 500,000 daltons, measured by gel permeation chromatography against polystyrene standards; and an amphiphilic copolymer comprising a hydrophobic block and a hydrophilic block or graft. 2. The porous asymmetric membrane of claim 1, wherein the poly(phenylene ether) copolymer comprising: 80 to 20 mole percent repeat units derived from 2,6-dimethylphenol; and20 to 80 mole percent repeat units derived from 2-methyl-6-phenol. 3. The porous asymmetric membrane of claim 1, wherein the amphiphilic copolymer comprises a block copolymer of poly(ethylene oxide) and poly(propylene oxide), polystyrene-graft-poly(ethylene glycol), or a combination thereof. 4. The porous asymmetric membrane of claim 1, wherein the hydrophobic block comprises polystyrene and the hydrophilic block or graft comprises poly(N,N-dimethylacrylamide) or poly(4-vinylpyridine). 5. The porous asymmetric membrane of claim 1, having a contact angle of 40 to 80 degrees. 6. A method of forming a porous asymmetric membrane, the method comprising: dissolving a poly(phenylene ether) copolymer comprising repeat units derived from 2,6-dimethylphenol and repeat units derived from 2-methyl-6-phenylphenol, and having an intrinsic viscosity of 0.7 to 1.5 deciliters per gram, measured in chloroform at 25° C. and a weight average molecular weight of 100,000 to 500,000 daltons, measured by gel permeation chromatography against polystyrene standards; and an amphiphilic copolymer comprising a hydrophobic block and a hydrophilic block or graft in a water-miscible polar aprotic solvent to form a porous asymmetric membrane-forming composition; andphase-inverting the porous asymmetric membrane forming-composition in a first non-solvent composition to form the porous asymmetric membrane. 7. The method of claim 6, further comprising washing the porous asymmetric membrane in a second non-solvent composition. 8. The method of claim 6, further comprising drying the porous asymmetric membrane. 9. The method of claim 6, wherein the first non-solvent composition comprises 10 to 100 weight percent water and 0 to 90 weight percent N-methyl-2-pyrrolidone, based on the total weight of the first non-solvent composition. 10. A method of making a hollow fiber by coextrusion through a spinneret comprising an annulus and a bore, wherein the method comprises coextruding: a membrane-forming composition comprising a hydrophobic polymer comprising a poly(phenylene ether) or poly(phenylene ether) copolymer comprising repeat units derived from 2,6-dimethylphenol and percent repeat units derived from 2-methyl-6-phenylphenol, and having an intrinsic viscosity of 0.7 to 1.5 deciliters per gram, measured in chloroform at 25° C. and a weight average molecular weight of 100,000 to 300,000 daltons, measured by gel permeation chromatography against polystyrene standards; and an amphiphilic copolymer comprising a hydrophobic block and a hydrophilic block or graft dissolved in a water-miscible polar aprotic solvent through the annulus, anda first non-solvent composition comprising water, a water-miscible polar aprotic solvent, or a combination comprising at least one of the foregoing, in the first non-solvent composition, through the bore,into a second non-solvent composition comprising water, a water-miscible polar aprotic solvent, or a combination comprising at least one of the foregoing, to form the hollow fiber. 11. The method of claim 10, further comprising washing the hollow fiber in a third non-solvent composition. 12. The method of claim 10, further comprising drying the hollow fiber. 13. A separation module comprising the porous asymmetric membrane of claim 1. 14. A hollow fiber made by the method of claim 10. 15. A separation module comprising the hollow fiber of claim 14. 16. The porous asymmetric membrane of claim 1, wherein the poly(phenylene ether) copolymer has a solubility in a water-miscible polar aprotic solvent of greater than 100 grams per kilogram at 25° C. 17. The porous asymmetric membrane of claim 1, wherein the poly(phenylene ether) copolymer has a solubility in a water-miscible polar aprotic solvent selected from the group consisting of N-methyl-2-pyrrolidone, N,N-dimethylformamide, and N,N-dimethylacetamide, of 100 to 400 grams per kilogram at 25° C. 18. The porous asymmetric membrane of claim 1, wherein the hydrophilic block of the amphiphilic block copolymer comprises an ethylenically unsaturated monomer selected from methoxy-capped poly(ethylene oxide) methacrylate, 4-vinylpyridine, N-vinylpyrrolidone, N,N-dimethylacrylamide, 4-acryloylmorpholine, or a combination comprising at least one of the foregoing. 19. The porous asymmetric membrane of claim 1, wherein the amphiphilic copolymer comprises a block copolymer of poly(ethylene oxide) and poly(propylene oxide).
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