Polymer composition and porous membrane
US-2015343392-A1 · Dec 3, 2015 · US
US10130918B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10130918-B2 |
| Application number | US-201615267652-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 16, 2016 |
| Priority date | Sep 16, 2016 |
| Publication date | Nov 20, 2018 |
| Grant date | Nov 20, 2018 |
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Disclosed are fluoropolymers with low CWST values and porous membranes made from the fluoropolymers. The fluoropolymer is made up of polymerized monomeric units of the formula A-X—CH 2 —B, wherein A is C 6 F 13 —(CH 2 ) 2 , X is O or S, and B is vinylphenyl, and the fluoropolymer has a weight average molecular weight (Mw) of at least 100 Kd and/or a glass transition temperature of at least 33° C. copolymer. The porous membranes are suitable for degassing a variety of fluids.
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The invention claimed is: 1. A porous membrane comprising a porous polymeric support and a fluoropolymer, wherein the fluoropolymer comprises polymerized monomeric units of the formula A-X—CH 2 —B, wherein A is C 6 F 13 —(CH 2 ) 2 , X is O or S, and B is vinylphenyl, and the fluoropolymer has a weight average molecular weight (Mw) of at least 100 Kd and/or a glass transition temperature of at least 33° C., wherein the porous polymeric support is selected from PVC/PAN, polysulfone, polyamide, cellulose, polyester, PPS, PPSU (polyphenyl sulfone), PVDF, PVF (polyvinyl fluoride), FEP (fluorinated ethylene-propylene), ETFE (polyethylenetetrafluoroethylene), PFPE (perfluoropolyether), PFSA (perfluorosulfonic acid), perfluoropolyoxetane, polyimide, polyether imide, polycarbonate, and polystyrene, and wherein the porous membrane has a CWST of 15 to 23 dynes/cm. 2. The porous membrane of claim 1 , wherein B is meta-vinylphenyl, para-vinylphenyl, or a mixture thereof. 3. The porous membrane of claim 1 , wherein the monomeric unit is meta-[perfluorohexylethylenethiomethyl] styrene, para-[perfluorohexylethylenethiomethyl] styrene, or a mixture thereof. 4. The porous membrane of claim 1 , wherein the monomeric unit is meta-[perfluorohexylethyleneoxymethyl] styrene, para-[perfluorohexylethyleneoxymethyl] styrene, or a mixture thereof. 5. The porous membrane of claim 1 , wherein the fluoropolymer has a an Mw of at least 200 Kd. 6. The porous membrane of claim 1 , wherein the fluoropolymer has an Mw of 400 to 1300 Kd. 7. The porous membrane of claim 1 , wherein the fluoropolymer has an Mw of 1100 to 1300 Kd. 8. The porous membrane of claim 1 , wherein the porous polymeric support is selected from PVC/PAN, polysulfone, polyamide, cellulose, polyethersulfone, PPS, PPSU (polyphenyl sulfone), PFPE (perfluoropolyether), PFSA (perfluorosulfonic acid), perfluoropolyoxetane, polyimide, polyether imide, and polycarbonate. 9. A method of preparing a porous membrane according to claim 1 , the method comprising: (i) dissolving the fluoropolymer in a solvent or mixture of solvents to obtain a solution comprising the fluoropolymer; (ii) coating the solution from (i) on the porous polymeric support; and (iii) evaporating the solvent or mixture of solvents from the coating to obtain the porous membrane. 10. The method of claim 9 , wherein the solvent or mixture of solvents comprises a halogenated solvent, optionally in combination with an alcohol. 11. The method of claim 10 , wherein the solvent or mixture of solvents is selected from methoxy nona-fluorobutane, methoxy nona-fluorobutane, chloroform, dichloromethane, 1,2-dichloroethane; 1,1,2-trichloro-1,2,2-trifluoroethane, 1,1,1,2,2-pentafluoro-3,3-dichloropropane, optionally in combination with isopropanol and/or 1,1,1,3,3,3-hexafluoro-2-propanol. 12. A method of filtering a fluid, the method comprising passing the fluid through the porous membrane of claim 1 . 13. The method of claim 12 , wherein a gas present in the fluid is removed from the fluid.
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Coating · CPC title
After-treatment (C08J9/22 takes precedence) · CPC title
Sulfur · CPC title
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