WO2011153085A2 - Process for making coated porous materials - Google Patents
Process for making coated porous materials Download PDFInfo
- Publication number
- WO2011153085A2 WO2011153085A2 PCT/US2011/038283 US2011038283W WO2011153085A2 WO 2011153085 A2 WO2011153085 A2 WO 2011153085A2 US 2011038283 W US2011038283 W US 2011038283W WO 2011153085 A2 WO2011153085 A2 WO 2011153085A2
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- coatable composition
- polymerizable compound
- substrate
- solvent
- coated porous
- Prior art date
Links
- 239000011148 porous material Substances 0.000 title claims abstract description 115
- 238000000034 method Methods 0.000 title claims abstract description 48
- 230000008569 process Effects 0.000 title claims abstract description 43
- 239000000758 substrate Substances 0.000 claims abstract description 116
- 239000000203 mixture Substances 0.000 claims abstract description 80
- 238000000576 coating method Methods 0.000 claims abstract description 40
- 239000011248 coating agent Substances 0.000 claims abstract description 38
- 150000001875 compounds Chemical class 0.000 claims abstract description 33
- 239000002904 solvent Substances 0.000 claims abstract description 32
- 230000000379 polymerizing effect Effects 0.000 claims abstract description 8
- 238000002360 preparation method Methods 0.000 claims abstract description 6
- 238000009738 saturating Methods 0.000 claims abstract description 3
- 239000012528 membrane Substances 0.000 claims description 43
- 239000000463 material Substances 0.000 claims description 38
- 239000000178 monomer Substances 0.000 claims description 38
- -1 poly(ethyleneoxy) ethanol Polymers 0.000 claims description 35
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 29
- 238000006116 polymerization reaction Methods 0.000 claims description 23
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical group CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 19
- 229920001223 polyethylene glycol Polymers 0.000 claims description 17
- 239000002202 Polyethylene glycol Substances 0.000 claims description 16
- 229920000642 polymer Polymers 0.000 claims description 16
- 229920006037 cross link polymer Polymers 0.000 claims description 14
- 230000005855 radiation Effects 0.000 claims description 11
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims description 10
- 229920001577 copolymer Polymers 0.000 claims description 10
- 239000004094 surface-active agent Substances 0.000 claims description 10
- 239000003431 cross linking reagent Substances 0.000 claims description 8
- 125000004386 diacrylate group Chemical group 0.000 claims description 8
- 229920002678 cellulose Polymers 0.000 claims description 7
- 150000004676 glycans Chemical class 0.000 claims description 7
- 229920001282 polysaccharide Polymers 0.000 claims description 7
- 239000005017 polysaccharide Substances 0.000 claims description 7
- 229920002981 polyvinylidene fluoride Polymers 0.000 claims description 6
- 239000002356 single layer Substances 0.000 claims description 6
- 239000001913 cellulose Substances 0.000 claims description 5
- STVZJERGLQHEKB-UHFFFAOYSA-N ethylene glycol dimethacrylate Chemical compound CC(=C)C(=O)OCCOC(=O)C(C)=C STVZJERGLQHEKB-UHFFFAOYSA-N 0.000 claims description 5
- 230000000977 initiatory effect Effects 0.000 claims description 5
- 239000011780 sodium chloride Substances 0.000 claims description 5
- 239000002033 PVDF binder Substances 0.000 claims description 4
- 239000004952 Polyamide Substances 0.000 claims description 4
- 229920002647 polyamide Polymers 0.000 claims description 4
- 229920002451 polyvinyl alcohol Polymers 0.000 claims description 4
- LWZFANDGMFTDAV-BURFUSLBSA-N [(2r)-2-[(2r,3r,4s)-3,4-dihydroxyoxolan-2-yl]-2-hydroxyethyl] dodecanoate Chemical compound CCCCCCCCCCCC(=O)OC[C@@H](O)[C@H]1OC[C@H](O)[C@H]1O LWZFANDGMFTDAV-BURFUSLBSA-N 0.000 claims description 3
- 238000001704 evaporation Methods 0.000 claims description 3
- 125000000951 phenoxy group Chemical group [H]C1=C([H])C([H])=C(O*)C([H])=C1[H] 0.000 claims description 3
- 235000011067 sorbitan monolaureate Nutrition 0.000 claims description 3
- 229920002307 Dextran Polymers 0.000 claims description 2
- 229920001612 Hydroxyethyl starch Polymers 0.000 claims description 2
- 239000004372 Polyvinyl alcohol Substances 0.000 claims description 2
- GSEJCLTVZPLZKY-UHFFFAOYSA-N Triethanolamine Chemical compound OCCN(CCO)CCO GSEJCLTVZPLZKY-UHFFFAOYSA-N 0.000 claims description 2
- 239000002657 fibrous material Substances 0.000 claims description 2
- 229940050526 hydroxyethylstarch Drugs 0.000 claims description 2
- 229920000609 methyl cellulose Polymers 0.000 claims description 2
- 239000001923 methylcellulose Substances 0.000 claims description 2
- 235000010981 methylcellulose Nutrition 0.000 claims description 2
- 229920000570 polyether Polymers 0.000 claims description 2
- 229920000036 polyvinylpyrrolidone Polymers 0.000 claims description 2
- 239000001267 polyvinylpyrrolidone Substances 0.000 claims description 2
- 235000013855 polyvinylpyrrolidone Nutrition 0.000 claims description 2
- 229950006451 sorbitan laurate Drugs 0.000 claims description 2
- BDHFUVZGWQCTTF-UHFFFAOYSA-M sulfonate Chemical compound [O-]S(=O)=O BDHFUVZGWQCTTF-UHFFFAOYSA-M 0.000 claims description 2
- 239000003960 organic solvent Substances 0.000 claims 2
- LNAZSHAWQACDHT-XIYTZBAFSA-N (2r,3r,4s,5r,6s)-4,5-dimethoxy-2-(methoxymethyl)-3-[(2s,3r,4s,5r,6r)-3,4,5-trimethoxy-6-(methoxymethyl)oxan-2-yl]oxy-6-[(2r,3r,4s,5r,6r)-4,5,6-trimethoxy-2-(methoxymethyl)oxan-3-yl]oxyoxane Chemical compound CO[C@@H]1[C@@H](OC)[C@H](OC)[C@@H](COC)O[C@H]1O[C@H]1[C@H](OC)[C@@H](OC)[C@H](O[C@H]2[C@@H]([C@@H](OC)[C@H](OC)O[C@@H]2COC)OC)O[C@@H]1COC LNAZSHAWQACDHT-XIYTZBAFSA-N 0.000 claims 1
- RPZANUYHRMRTTE-UHFFFAOYSA-N 2,3,4-trimethoxy-6-(methoxymethyl)-5-[3,4,5-trimethoxy-6-(methoxymethyl)oxan-2-yl]oxyoxane;1-[[3,4,5-tris(2-hydroxybutoxy)-6-[4,5,6-tris(2-hydroxybutoxy)-2-(2-hydroxybutoxymethyl)oxan-3-yl]oxyoxan-2-yl]methoxy]butan-2-ol Chemical compound COC1C(OC)C(OC)C(COC)OC1OC1C(OC)C(OC)C(OC)OC1COC.CCC(O)COC1C(OCC(O)CC)C(OCC(O)CC)C(COCC(O)CC)OC1OC1C(OCC(O)CC)C(OCC(O)CC)C(OCC(O)CC)OC1COCC(O)CC RPZANUYHRMRTTE-UHFFFAOYSA-N 0.000 claims 1
- 239000001856 Ethyl cellulose Substances 0.000 claims 1
- ZZSNKZQZMQGXPY-UHFFFAOYSA-N Ethyl cellulose Chemical compound CCOCC1OC(OC)C(OCC)C(OCC)C1OC1C(O)C(O)C(OC)C(CO)O1 ZZSNKZQZMQGXPY-UHFFFAOYSA-N 0.000 claims 1
- 229920000663 Hydroxyethyl cellulose Polymers 0.000 claims 1
- 239000004354 Hydroxyethyl cellulose Substances 0.000 claims 1
- 229920001479 Hydroxyethyl methyl cellulose Polymers 0.000 claims 1
- 229920002153 Hydroxypropyl cellulose Polymers 0.000 claims 1
- 238000001035 drying Methods 0.000 claims 1
- 229920001249 ethyl cellulose Polymers 0.000 claims 1
- 235000019325 ethyl cellulose Nutrition 0.000 claims 1
- 235000019447 hydroxyethyl cellulose Nutrition 0.000 claims 1
- 239000001863 hydroxypropyl cellulose Substances 0.000 claims 1
- 235000010977 hydroxypropyl cellulose Nutrition 0.000 claims 1
- 239000001866 hydroxypropyl methyl cellulose Substances 0.000 claims 1
- 229920003088 hydroxypropyl methyl cellulose Polymers 0.000 claims 1
- 235000010979 hydroxypropyl methyl cellulose Nutrition 0.000 claims 1
- UFVKGYZPFZQRLF-UHFFFAOYSA-N hydroxypropyl methyl cellulose Chemical compound OC1C(O)C(OC)OC(CO)C1OC1C(O)C(O)C(OC2C(C(O)C(OC3C(C(O)C(O)C(CO)O3)O)C(CO)O2)O)C(CO)O1 UFVKGYZPFZQRLF-UHFFFAOYSA-N 0.000 claims 1
- 150000003457 sulfones Chemical class 0.000 claims 1
- 238000005406 washing Methods 0.000 claims 1
- 238000001914 filtration Methods 0.000 description 16
- 239000003999 initiator Substances 0.000 description 16
- 239000010410 layer Substances 0.000 description 15
- 239000000243 solution Substances 0.000 description 11
- 238000002145 thermally induced phase separation Methods 0.000 description 10
- NIXOWILDQLNWCW-UHFFFAOYSA-M Acrylate Chemical compound [O-]C(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-M 0.000 description 8
- 239000003795 chemical substances by application Substances 0.000 description 7
- 238000012360 testing method Methods 0.000 description 7
- 230000004907 flux Effects 0.000 description 6
- 150000001252 acrylic acid derivatives Chemical class 0.000 description 5
- 239000007864 aqueous solution Substances 0.000 description 5
- 238000006243 chemical reaction Methods 0.000 description 5
- 238000000151 deposition Methods 0.000 description 5
- 238000006384 oligomerization reaction Methods 0.000 description 5
- 229920001155 polypropylene Polymers 0.000 description 5
- 238000007725 thermal activation Methods 0.000 description 5
- 238000009281 ultraviolet germicidal irradiation Methods 0.000 description 5
- MYRTYDVEIRVNKP-UHFFFAOYSA-N 1,2-Divinylbenzene Chemical compound C=CC1=CC=CC=C1C=C MYRTYDVEIRVNKP-UHFFFAOYSA-N 0.000 description 4
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 4
- 239000004698 Polyethylene Substances 0.000 description 4
- 239000004743 Polypropylene Substances 0.000 description 4
- ISAOCJYIOMOJEB-UHFFFAOYSA-N benzoin Chemical compound C=1C=CC=CC=1C(O)C(=O)C1=CC=CC=C1 ISAOCJYIOMOJEB-UHFFFAOYSA-N 0.000 description 4
- 230000002209 hydrophobic effect Effects 0.000 description 4
- 229920000573 polyethylene Polymers 0.000 description 4
- 238000010998 test method Methods 0.000 description 4
- OZAIFHULBGXAKX-UHFFFAOYSA-N 2-(2-cyanopropan-2-yldiazenyl)-2-methylpropanenitrile Chemical compound N#CC(C)(C)N=NC(C)(C)C#N OZAIFHULBGXAKX-UHFFFAOYSA-N 0.000 description 3
- TXBCBTDQIULDIA-UHFFFAOYSA-N 2-[[3-hydroxy-2,2-bis(hydroxymethyl)propoxy]methyl]-2-(hydroxymethyl)propane-1,3-diol Chemical compound OCC(CO)(CO)COCC(CO)(CO)CO TXBCBTDQIULDIA-UHFFFAOYSA-N 0.000 description 3
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 3
- 244000028419 Styrax benzoin Species 0.000 description 3
- 235000000126 Styrax benzoin Nutrition 0.000 description 3
- 235000008411 Sumatra benzointree Nutrition 0.000 description 3
- DAKWPKUUDNSNPN-UHFFFAOYSA-N Trimethylolpropane triacrylate Chemical compound C=CC(=O)OCC(CC)(COC(=O)C=C)COC(=O)C=C DAKWPKUUDNSNPN-UHFFFAOYSA-N 0.000 description 3
- 229960002130 benzoin Drugs 0.000 description 3
- 238000004132 cross linking Methods 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 235000019382 gum benzoic Nutrition 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 238000005259 measurement Methods 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 229920001515 polyalkylene glycol Polymers 0.000 description 3
- 229920000728 polyester Polymers 0.000 description 3
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- 239000012266 salt solution Substances 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 description 2
- AFFLGGQVNFXPEV-UHFFFAOYSA-N 1-decene Chemical compound CCCCCCCCC=C AFFLGGQVNFXPEV-UHFFFAOYSA-N 0.000 description 2
- LIKMAJRDDDTEIG-UHFFFAOYSA-N 1-hexene Chemical compound CCCCC=C LIKMAJRDDDTEIG-UHFFFAOYSA-N 0.000 description 2
- KWKAKUADMBZCLK-UHFFFAOYSA-N 1-octene Chemical compound CCCCCCC=C KWKAKUADMBZCLK-UHFFFAOYSA-N 0.000 description 2
- LEJBBGNFPAFPKQ-UHFFFAOYSA-N 2-(2-prop-2-enoyloxyethoxy)ethyl prop-2-enoate Chemical compound C=CC(=O)OCCOCCOC(=O)C=C LEJBBGNFPAFPKQ-UHFFFAOYSA-N 0.000 description 2
- XFCMNSHQOZQILR-UHFFFAOYSA-N 2-[2-(2-methylprop-2-enoyloxy)ethoxy]ethyl 2-methylprop-2-enoate Chemical compound CC(=C)C(=O)OCCOCCOC(=O)C(C)=C XFCMNSHQOZQILR-UHFFFAOYSA-N 0.000 description 2
- INQDDHNZXOAFFD-UHFFFAOYSA-N 2-[2-(2-prop-2-enoyloxyethoxy)ethoxy]ethyl prop-2-enoate Chemical compound C=CC(=O)OCCOCCOCCOC(=O)C=C INQDDHNZXOAFFD-UHFFFAOYSA-N 0.000 description 2
- KUDUQBURMYMBIJ-UHFFFAOYSA-N 2-prop-2-enoyloxyethyl prop-2-enoate Chemical compound C=CC(=O)OCCOC(=O)C=C KUDUQBURMYMBIJ-UHFFFAOYSA-N 0.000 description 2
- FIHBHSQYSYVZQE-UHFFFAOYSA-N 6-prop-2-enoyloxyhexyl prop-2-enoate Chemical compound C=CC(=O)OCCCCCCOC(=O)C=C FIHBHSQYSYVZQE-UHFFFAOYSA-N 0.000 description 2
- 239000004971 Cross linker Substances 0.000 description 2
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 description 2
- 239000004642 Polyimide Substances 0.000 description 2
- XBDQKXXYIPTUBI-UHFFFAOYSA-N Propionic acid Chemical compound CCC(O)=O XBDQKXXYIPTUBI-UHFFFAOYSA-N 0.000 description 2
- DKGAVHZHDRPRBM-UHFFFAOYSA-N Tert-Butanol Chemical compound CC(C)(C)O DKGAVHZHDRPRBM-UHFFFAOYSA-N 0.000 description 2
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 2
- OKKRPWIIYQTPQF-UHFFFAOYSA-N Trimethylolpropane trimethacrylate Chemical compound CC(=C)C(=O)OCC(CC)(COC(=O)C(C)=C)COC(=O)C(C)=C OKKRPWIIYQTPQF-UHFFFAOYSA-N 0.000 description 2
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 description 2
- FHLPGTXWCFQMIU-UHFFFAOYSA-N [4-[2-(4-prop-2-enoyloxyphenyl)propan-2-yl]phenyl] prop-2-enoate Chemical compound C=1C=C(OC(=O)C=C)C=CC=1C(C)(C)C1=CC=C(OC(=O)C=C)C=C1 FHLPGTXWCFQMIU-UHFFFAOYSA-N 0.000 description 2
- ROOXNKNUYICQNP-UHFFFAOYSA-N ammonium persulfate Chemical compound [NH4+].[NH4+].[O-]S(=O)(=O)OOS([O-])(=O)=O ROOXNKNUYICQNP-UHFFFAOYSA-N 0.000 description 2
- 239000011127 biaxially oriented polypropylene Substances 0.000 description 2
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- 125000000524 functional group Chemical group 0.000 description 2
- 238000003475 lamination Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 2
- 229910052753 mercury Inorganic materials 0.000 description 2
- 150000002734 metacrylic acid derivatives Chemical class 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000005191 phase separation Methods 0.000 description 2
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- 229920000233 poly(alkylene oxides) Polymers 0.000 description 2
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- 238000012545 processing Methods 0.000 description 2
- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical compound CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 description 2
- 230000000717 retained effect Effects 0.000 description 2
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- 239000011550 stock solution Substances 0.000 description 2
- 238000002834 transmittance Methods 0.000 description 2
- MXFQRSUWYYSPOC-UHFFFAOYSA-N (2,2-dimethyl-3-prop-2-enoyloxypropyl) prop-2-enoate Chemical compound C=CC(=O)OCC(C)(C)COC(=O)C=C MXFQRSUWYYSPOC-UHFFFAOYSA-N 0.000 description 1
- OAKFFVBGTSPYEG-UHFFFAOYSA-N (4-prop-2-enoyloxycyclohexyl) prop-2-enoate Chemical compound C=CC(=O)OC1CCC(OC(=O)C=C)CC1 OAKFFVBGTSPYEG-UHFFFAOYSA-N 0.000 description 1
- NWRZGFYWENINNX-UHFFFAOYSA-N 1,1,2-tris(ethenyl)cyclohexane Chemical compound C=CC1CCCCC1(C=C)C=C NWRZGFYWENINNX-UHFFFAOYSA-N 0.000 description 1
- BQCIDUSAKPWEOX-UHFFFAOYSA-N 1,1-Difluoroethene Chemical compound FC(F)=C BQCIDUSAKPWEOX-UHFFFAOYSA-N 0.000 description 1
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- MYWOJODOMFBVCB-UHFFFAOYSA-N 1,2,6-trimethylphenanthrene Chemical compound CC1=CC=C2C3=CC(C)=CC=C3C=CC2=C1C MYWOJODOMFBVCB-UHFFFAOYSA-N 0.000 description 1
- CYIGRWUIQAVBFG-UHFFFAOYSA-N 1,2-bis(2-ethenoxyethoxy)ethane Chemical compound C=COCCOCCOCCOC=C CYIGRWUIQAVBFG-UHFFFAOYSA-N 0.000 description 1
- QLLUAUADIMPKIH-UHFFFAOYSA-N 1,2-bis(ethenyl)naphthalene Chemical compound C1=CC=CC2=C(C=C)C(C=C)=CC=C21 QLLUAUADIMPKIH-UHFFFAOYSA-N 0.000 description 1
- MWZJGRDWJVHRDV-UHFFFAOYSA-N 1,4-bis(ethenoxy)butane Chemical compound C=COCCCCOC=C MWZJGRDWJVHRDV-UHFFFAOYSA-N 0.000 description 1
- ZDQNWDNMNKSMHI-UHFFFAOYSA-N 1-[2-(2-prop-2-enoyloxypropoxy)propoxy]propan-2-yl prop-2-enoate Chemical compound C=CC(=O)OC(C)COC(C)COCC(C)OC(=O)C=C ZDQNWDNMNKSMHI-UHFFFAOYSA-N 0.000 description 1
- YERHJBPPDGHCRJ-UHFFFAOYSA-N 1-[4-(1-oxoprop-2-enyl)-1-piperazinyl]-2-propen-1-one Chemical compound C=CC(=O)N1CCN(C(=O)C=C)CC1 YERHJBPPDGHCRJ-UHFFFAOYSA-N 0.000 description 1
- XQLXSGCTOLBFAK-UHFFFAOYSA-N 1-prop-2-enoyloxypentyl prop-2-enoate Chemical compound CCCCC(OC(=O)C=C)OC(=O)C=C XQLXSGCTOLBFAK-UHFFFAOYSA-N 0.000 description 1
- XMQHMLYURIVZJV-UHFFFAOYSA-N 10-prop-2-enoyloxydodecyl prop-2-enoate Chemical compound C=CC(=O)OC(CC)CCCCCCCCCOC(=O)C=C XMQHMLYURIVZJV-UHFFFAOYSA-N 0.000 description 1
- KWVGIHKZDCUPEU-UHFFFAOYSA-N 2,2-dimethoxy-2-phenylacetophenone Chemical compound C=1C=CC=CC=1C(OC)(OC)C(=O)C1=CC=CC=C1 KWVGIHKZDCUPEU-UHFFFAOYSA-N 0.000 description 1
- NEBBLNDVSSWJLL-UHFFFAOYSA-N 2,3-bis(2-methylprop-2-enoyloxy)propyl 2-methylprop-2-enoate Chemical compound CC(=C)C(=O)OCC(OC(=O)C(C)=C)COC(=O)C(C)=C NEBBLNDVSSWJLL-UHFFFAOYSA-N 0.000 description 1
- GJKGAPPUXSSCFI-UHFFFAOYSA-N 2-Hydroxy-4'-(2-hydroxyethoxy)-2-methylpropiophenone Chemical compound CC(C)(O)C(=O)C1=CC=C(OCCO)C=C1 GJKGAPPUXSSCFI-UHFFFAOYSA-N 0.000 description 1
- JFZBUNLOTDDXNY-UHFFFAOYSA-N 2-[2-(2-methylprop-2-enoyloxy)propoxy]propyl 2-methylprop-2-enoate Chemical compound CC(=C)C(=O)OCC(C)OCC(C)OC(=O)C(C)=C JFZBUNLOTDDXNY-UHFFFAOYSA-N 0.000 description 1
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- OWDBMKZHFCSOOL-UHFFFAOYSA-N 2-[2-[2-(2-methylprop-2-enoyloxy)propoxy]propoxy]propyl 2-methylprop-2-enoate Chemical compound CC(=C)C(=O)OC(C)COC(C)COC(C)COC(=O)C(C)=C OWDBMKZHFCSOOL-UHFFFAOYSA-N 0.000 description 1
- HCLJOFJIQIJXHS-UHFFFAOYSA-N 2-[2-[2-(2-prop-2-enoyloxyethoxy)ethoxy]ethoxy]ethyl prop-2-enoate Chemical compound C=CC(=O)OCCOCCOCCOCCOC(=O)C=C HCLJOFJIQIJXHS-UHFFFAOYSA-N 0.000 description 1
- KMNCBSZOIQAUFX-UHFFFAOYSA-N 2-ethoxy-1,2-diphenylethanone Chemical compound C=1C=CC=CC=1C(OCC)C(=O)C1=CC=CC=C1 KMNCBSZOIQAUFX-UHFFFAOYSA-N 0.000 description 1
- GTELLNMUWNJXMQ-UHFFFAOYSA-N 2-ethyl-2-(hydroxymethyl)propane-1,3-diol;prop-2-enoic acid Chemical class OC(=O)C=C.OC(=O)C=C.OC(=O)C=C.CCC(CO)(CO)CO GTELLNMUWNJXMQ-UHFFFAOYSA-N 0.000 description 1
- XMLYCEVDHLAQEL-UHFFFAOYSA-N 2-hydroxy-2-methyl-1-phenylpropan-1-one Chemical group CC(C)(O)C(=O)C1=CC=CC=C1 XMLYCEVDHLAQEL-UHFFFAOYSA-N 0.000 description 1
- BQZJOQXSCSZQPS-UHFFFAOYSA-N 2-methoxy-1,2-diphenylethanone Chemical compound C=1C=CC=CC=1C(OC)C(=O)C1=CC=CC=C1 BQZJOQXSCSZQPS-UHFFFAOYSA-N 0.000 description 1
- YTTFFPATQICAQN-UHFFFAOYSA-N 2-methoxypropan-1-ol Chemical compound COC(C)CO YTTFFPATQICAQN-UHFFFAOYSA-N 0.000 description 1
- RIWRBSMFKVOJMN-UHFFFAOYSA-N 2-methyl-1-phenylpropan-2-ol Chemical compound CC(C)(O)CC1=CC=CC=C1 RIWRBSMFKVOJMN-UHFFFAOYSA-N 0.000 description 1
- DMQYPVOQAARSNF-UHFFFAOYSA-N 3-[2,3-bis(3-prop-2-enoyloxypropoxy)propoxy]propyl prop-2-enoate Chemical compound C=CC(=O)OCCCOCC(OCCCOC(=O)C=C)COCCCOC(=O)C=C DMQYPVOQAARSNF-UHFFFAOYSA-N 0.000 description 1
- VFXXTYGQYWRHJP-UHFFFAOYSA-N 4,4'-azobis(4-cyanopentanoic acid) Chemical compound OC(=O)CCC(C)(C#N)N=NC(C)(CCC(O)=O)C#N VFXXTYGQYWRHJP-UHFFFAOYSA-N 0.000 description 1
- DBCAQXHNJOFNGC-UHFFFAOYSA-N 4-bromo-1,1,1-trifluorobutane Chemical compound FC(F)(F)CCCBr DBCAQXHNJOFNGC-UHFFFAOYSA-N 0.000 description 1
- JHWGFJBTMHEZME-UHFFFAOYSA-N 4-prop-2-enoyloxybutyl prop-2-enoate Chemical compound C=CC(=O)OCCCCOC(=O)C=C JHWGFJBTMHEZME-UHFFFAOYSA-N 0.000 description 1
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical group CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 1
- 241000894006 Bacteria Species 0.000 description 1
- 239000004342 Benzoyl peroxide Substances 0.000 description 1
- OMPJBNCRMGITSC-UHFFFAOYSA-N Benzoylperoxide Chemical compound C=1C=CC=CC=1C(=O)OOC(=O)C1=CC=CC=C1 OMPJBNCRMGITSC-UHFFFAOYSA-N 0.000 description 1
- XWUNIDGEMNBBAQ-UHFFFAOYSA-N Bisphenol A ethoxylate diacrylate Chemical compound C=1C=C(OCCOC(=O)C=C)C=CC=1C(C)(C)C1=CC=C(OCCOC(=O)C=C)C=C1 XWUNIDGEMNBBAQ-UHFFFAOYSA-N 0.000 description 1
- 229920002134 Carboxymethyl cellulose Polymers 0.000 description 1
- FNEVRFUPVLHRSK-UHFFFAOYSA-N Cc1cc(C)c(C(=O)c2ccccc2O[PH2]=O)c(C)c1 Chemical group Cc1cc(C)c(C(=O)c2ccccc2O[PH2]=O)c(C)c1 FNEVRFUPVLHRSK-UHFFFAOYSA-N 0.000 description 1
- 229920000089 Cyclic olefin copolymer Polymers 0.000 description 1
- FBPFZTCFMRRESA-FSIIMWSLSA-N D-Glucitol Natural products OC[C@H](O)[C@H](O)[C@@H](O)[C@H](O)CO FBPFZTCFMRRESA-FSIIMWSLSA-N 0.000 description 1
- 239000004641 Diallyl-phthalate Substances 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- 229920007925 Ethylene chlorotrifluoroethylene (ECTFE) Polymers 0.000 description 1
- 241000422980 Marietta Species 0.000 description 1
- 239000004677 Nylon Substances 0.000 description 1
- 229920002292 Nylon 6 Polymers 0.000 description 1
- 229920001054 Poly(ethylene‐co‐vinyl acetate) Polymers 0.000 description 1
- 239000004695 Polyether sulfone Substances 0.000 description 1
- 239000004721 Polyphenylene oxide Substances 0.000 description 1
- 229920006362 Teflon® Polymers 0.000 description 1
- 238000003848 UV Light-Curing Methods 0.000 description 1
- GQPVFBDWIUVLHG-UHFFFAOYSA-N [2,2-bis(hydroxymethyl)-3-(2-methylprop-2-enoyloxy)propyl] 2-methylprop-2-enoate Chemical compound CC(=C)C(=O)OCC(CO)(CO)COC(=O)C(C)=C GQPVFBDWIUVLHG-UHFFFAOYSA-N 0.000 description 1
- CQHKDHVZYZUZMJ-UHFFFAOYSA-N [2,2-bis(hydroxymethyl)-3-prop-2-enoyloxypropyl] prop-2-enoate Chemical compound C=CC(=O)OCC(CO)(CO)COC(=O)C=C CQHKDHVZYZUZMJ-UHFFFAOYSA-N 0.000 description 1
- ULQMPOIOSDXIGC-UHFFFAOYSA-N [2,2-dimethyl-3-(2-methylprop-2-enoyloxy)propyl] 2-methylprop-2-enoate Chemical compound CC(=C)C(=O)OCC(C)(C)COC(=O)C(C)=C ULQMPOIOSDXIGC-UHFFFAOYSA-N 0.000 description 1
- GCNKJQRMNYNDBI-UHFFFAOYSA-N [2-(hydroxymethyl)-2-(2-methylprop-2-enoyloxymethyl)butyl] 2-methylprop-2-enoate Chemical compound CC(=C)C(=O)OCC(CO)(CC)COC(=O)C(C)=C GCNKJQRMNYNDBI-UHFFFAOYSA-N 0.000 description 1
- TUOBEAZXHLTYLF-UHFFFAOYSA-N [2-(hydroxymethyl)-2-(prop-2-enoyloxymethyl)butyl] prop-2-enoate Chemical compound C=CC(=O)OCC(CO)(CC)COC(=O)C=C TUOBEAZXHLTYLF-UHFFFAOYSA-N 0.000 description 1
- JUDXBRVLWDGRBC-UHFFFAOYSA-N [2-(hydroxymethyl)-3-(2-methylprop-2-enoyloxy)-2-(2-methylprop-2-enoyloxymethyl)propyl] 2-methylprop-2-enoate Chemical compound CC(=C)C(=O)OCC(CO)(COC(=O)C(C)=C)COC(=O)C(C)=C JUDXBRVLWDGRBC-UHFFFAOYSA-N 0.000 description 1
- HVVWZTWDBSEWIH-UHFFFAOYSA-N [2-(hydroxymethyl)-3-prop-2-enoyloxy-2-(prop-2-enoyloxymethyl)propyl] prop-2-enoate Chemical compound C=CC(=O)OCC(CO)(COC(=O)C=C)COC(=O)C=C HVVWZTWDBSEWIH-UHFFFAOYSA-N 0.000 description 1
- INXWLSDYDXPENO-UHFFFAOYSA-N [2-(hydroxymethyl)-3-prop-2-enoyloxy-2-[[3-prop-2-enoyloxy-2,2-bis(prop-2-enoyloxymethyl)propoxy]methyl]propyl] prop-2-enoate Chemical compound C=CC(=O)OCC(COC(=O)C=C)(CO)COCC(COC(=O)C=C)(COC(=O)C=C)COC(=O)C=C INXWLSDYDXPENO-UHFFFAOYSA-N 0.000 description 1
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- 238000004026 adhesive bonding Methods 0.000 description 1
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- 239000012670 alkaline solution Substances 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910001870 ammonium persulfate Inorganic materials 0.000 description 1
- 239000012736 aqueous medium Substances 0.000 description 1
- 239000003125 aqueous solvent Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- RWCCWEUUXYIKHB-UHFFFAOYSA-N benzophenone Chemical compound C=1C=CC=CC=1C(=O)C1=CC=CC=C1 RWCCWEUUXYIKHB-UHFFFAOYSA-N 0.000 description 1
- 239000012965 benzophenone Substances 0.000 description 1
- 229940024874 benzophenone Drugs 0.000 description 1
- 235000019400 benzoyl peroxide Nutrition 0.000 description 1
- 235000013361 beverage Nutrition 0.000 description 1
- 229920006378 biaxially oriented polypropylene Polymers 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- QUDWYFHPNIMBFC-UHFFFAOYSA-N bis(prop-2-enyl) benzene-1,2-dicarboxylate Chemical compound C=CCOC(=O)C1=CC=CC=C1C(=O)OCC=C QUDWYFHPNIMBFC-UHFFFAOYSA-N 0.000 description 1
- QUZSUMLPWDHKCJ-UHFFFAOYSA-N bisphenol A dimethacrylate Chemical compound C1=CC(OC(=O)C(=C)C)=CC=C1C(C)(C)C1=CC=C(OC(=O)C(C)=C)C=C1 QUZSUMLPWDHKCJ-UHFFFAOYSA-N 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 239000001768 carboxy methyl cellulose Substances 0.000 description 1
- 235000010948 carboxy methyl cellulose Nutrition 0.000 description 1
- 239000008112 carboxymethyl-cellulose Substances 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- UUAGAQFQZIEFAH-UHFFFAOYSA-N chlorotrifluoroethylene Chemical group FC(F)=C(F)Cl UUAGAQFQZIEFAH-UHFFFAOYSA-N 0.000 description 1
- 239000008199 coating composition Substances 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 229910021641 deionized water Inorganic materials 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- USIUVYZYUHIAEV-UHFFFAOYSA-N diphenyl ether Natural products C=1C=CC=CC=1OC1=CC=CC=C1 USIUVYZYUHIAEV-UHFFFAOYSA-N 0.000 description 1
- PODOEQVNFJSWIK-UHFFFAOYSA-N diphenylphosphoryl-(2,4,6-trimethoxyphenyl)methanone Chemical compound COC1=CC(OC)=CC(OC)=C1C(=O)P(=O)(C=1C=CC=CC=1)C1=CC=CC=C1 PODOEQVNFJSWIK-UHFFFAOYSA-N 0.000 description 1
- AFOSIXZFDONLBT-UHFFFAOYSA-N divinyl sulfone Chemical compound C=CS(=O)(=O)C=C AFOSIXZFDONLBT-UHFFFAOYSA-N 0.000 description 1
- 239000000975 dye Substances 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 229940052303 ethers for general anesthesia Drugs 0.000 description 1
- 230000001747 exhibiting effect Effects 0.000 description 1
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- 239000012530 fluid Substances 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
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- 239000000446 fuel Substances 0.000 description 1
- 230000004927 fusion Effects 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 239000012510 hollow fiber Substances 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 229920001477 hydrophilic polymer Polymers 0.000 description 1
- 229920001600 hydrophobic polymer Polymers 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 230000001939 inductive effect Effects 0.000 description 1
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- 239000011147 inorganic material Substances 0.000 description 1
- 229910017053 inorganic salt Inorganic materials 0.000 description 1
- ZFSLODLOARCGLH-UHFFFAOYSA-N isocyanuric acid Chemical compound OC1=NC(O)=NC(O)=N1 ZFSLODLOARCGLH-UHFFFAOYSA-N 0.000 description 1
- 238000010030 laminating Methods 0.000 description 1
- CDOSHBSSFJOMGT-UHFFFAOYSA-N linalool Chemical compound CC(C)=CCCC(C)(O)C=C CDOSHBSSFJOMGT-UHFFFAOYSA-N 0.000 description 1
- 239000002609 medium Substances 0.000 description 1
- PSGAAPLEWMOORI-PEINSRQWSA-N medroxyprogesterone acetate Chemical compound C([C@@]12C)CC(=O)C=C1[C@@H](C)C[C@@H]1[C@@H]2CC[C@]2(C)[C@@](OC(C)=O)(C(C)=O)CC[C@H]21 PSGAAPLEWMOORI-PEINSRQWSA-N 0.000 description 1
- 125000005641 methacryl group Chemical group 0.000 description 1
- 125000000956 methoxy group Chemical group [H]C([H])([H])O* 0.000 description 1
- 238000001471 micro-filtration Methods 0.000 description 1
- 239000012982 microporous membrane Substances 0.000 description 1
- LKIPOGBWSIFYFM-UHFFFAOYSA-N n,n-bis(ethenyl)formamide Chemical compound C=CN(C=C)C=O LKIPOGBWSIFYFM-UHFFFAOYSA-N 0.000 description 1
- TVMXDCGIABBOFY-UHFFFAOYSA-N n-Octanol Natural products CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 description 1
- QHQMBOKYHCJVKF-UHFFFAOYSA-N n-[12-(prop-2-enoylamino)dodecyl]prop-2-enamide Chemical compound C=CC(=O)NCCCCCCCCCCCCNC(=O)C=C QHQMBOKYHCJVKF-UHFFFAOYSA-N 0.000 description 1
- YQCFXPARMSSRRK-UHFFFAOYSA-N n-[6-(prop-2-enoylamino)hexyl]prop-2-enamide Chemical compound C=CC(=O)NCCCCCCNC(=O)C=C YQCFXPARMSSRRK-UHFFFAOYSA-N 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 229920001778 nylon Polymers 0.000 description 1
- 230000003606 oligomerizing effect Effects 0.000 description 1
- 239000011368 organic material Substances 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 description 1
- FSDNTQSJGHSJBG-UHFFFAOYSA-N piperidine-4-carbonitrile Chemical compound N#CC1CCNCC1 FSDNTQSJGHSJBG-UHFFFAOYSA-N 0.000 description 1
- 238000009832 plasma treatment Methods 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920001983 poloxamer Polymers 0.000 description 1
- 229920001200 poly(ethylene-vinyl acetate) Polymers 0.000 description 1
- 229920002627 poly(phosphazenes) Polymers 0.000 description 1
- 229920002492 poly(sulfone) Polymers 0.000 description 1
- 229920005569 poly(vinylidene fluoride-co-hexafluoropropylene) Polymers 0.000 description 1
- 229920006393 polyether sulfone Polymers 0.000 description 1
- 229920006380 polyphenylene oxide Polymers 0.000 description 1
- 229920001451 polypropylene glycol Polymers 0.000 description 1
- 229920002689 polyvinyl acetate Polymers 0.000 description 1
- 239000011118 polyvinyl acetate Substances 0.000 description 1
- 229920002620 polyvinyl fluoride Polymers 0.000 description 1
- USHAGKDGDHPEEY-UHFFFAOYSA-L potassium persulfate Chemical compound [K+].[K+].[O-]S(=O)(=O)OOS([O-])(=O)=O USHAGKDGDHPEEY-UHFFFAOYSA-L 0.000 description 1
- 239000002243 precursor Substances 0.000 description 1
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 1
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000010791 quenching Methods 0.000 description 1
- 230000000171 quenching effect Effects 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 239000013557 residual solvent Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 230000035945 sensitivity Effects 0.000 description 1
- 238000002791 soaking Methods 0.000 description 1
- 239000011877 solvent mixture Substances 0.000 description 1
- 239000000600 sorbitol Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000004544 sputter deposition Methods 0.000 description 1
- 230000008093 supporting effect Effects 0.000 description 1
- 230000008961 swelling Effects 0.000 description 1
- 238000000108 ultra-filtration Methods 0.000 description 1
- 238000007740 vapor deposition Methods 0.000 description 1
- 229920001567 vinyl ester resin Polymers 0.000 description 1
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 1
- 229920002554 vinyl polymer Polymers 0.000 description 1
- 239000011800 void material Substances 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
- 239000004711 α-olefin Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/10—Supported membranes; Membrane supports
- B01D69/107—Organic support material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
- B01D67/0002—Organic membrane manufacture
- B01D67/0006—Organic membrane manufacture by chemical reactions
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
- B01D67/0081—After-treatment of organic or inorganic membranes
- B01D67/0088—Physical treatment with compounds, e.g. swelling, coating or impregnation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/10—Supported membranes; Membrane supports
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/14—Dynamic membranes
- B01D69/141—Heterogeneous membranes, e.g. containing dispersed material; Mixed matrix membranes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
- B01D2239/04—Additives and treatments of the filtering material
- B01D2239/0471—Surface coating material
- B01D2239/0478—Surface coating material on a layer of the filter
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
- B01D2239/10—Filtering material manufacturing
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2323/00—Details relating to membrane preparation
- B01D2323/02—Hydrophilization
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2323/00—Details relating to membrane preparation
- B01D2323/28—Pore treatments
Definitions
- This invention relates to coated porous materials that include hydrophilic coatings and which are useful as separation or filtration media, and to processes for the preparation of coated porous materials.
- a filtration substrate e.g., a membrane
- Reducing the hydrophobicity (or increasing the hydrophilicity) of a filtration substrate is desired in order to reduce fouling during use.
- a filtration substrate e.g., a membrane
- hydrophobic polymers e.g., polyethylene glycol
- the art has developed methods for modifying the polymer surface of a substrate to render it hydrophilic and thus more readily wettable with water.
- the art has known to either chemically modify the surface and pore -walls of a substrate or, alternatively, to coat the walls of the pores in the substrate with a hydrophilic layer, the layer usually being polymeric in nature.
- the hydrophilic layer improves the affinity of the substrate material towards water, increasing its wettability and, in some cases, making the substrate completely wettable by water.
- the present invention provides a process for making hydrophilic filtration media which demonstrates a low level of swelling when wet and possesses a surface that is rich in polar functional groups.
- the filtration media experiences minimal pore-plugging in use and typically demonstrates a high surface energy.
- the filtration media is readily made using an efficient process.
- the invention provides a process for the preparation of coated porous material, the process comprising:
- a porous substrate comprising a plurality of pores extending through the substrate from a first major surface to a second major surface, each pore comprising an inner pore wall defining the internal dimension of the pore;
- the invention provides a coated porous material made from the foregoing process.
- hydrophilic is used as being indicative of a property in which a molecule, substance or article demonstrates an affinity for water by, for example, hydrogen bonding with water.
- interpenetrating polymer network refers to two or more polymer networks which are at least partially interlaced on a molecular scale but not covalently bonded to each other. Such a network cannot be separated unless chemical bonds are broken.
- any recitation of a numerical range by endpoints includes all numbers subsumed within that range (e.g., 1 to 5 includes 1, 1.5, 2, 2.75, 3, 3.80, 4, 5, etc.).
- Composite materials and, more particularly, coated porous materials are provided having a porous substrate and a hydrophilic coating on the walls of at least some of the pores within the substrate.
- the hydrophilic coating is a single layer of materials that includes at least one crosslinked polymer and a second compatible component (e.g., compatible with the crosslinked polymer and a precursor thereof).
- the presence of the hydrophilic coating within the pores of the substrate alters the surface properties of the substrate.
- the coated porous material is made according to a process wherein a coatable composition is deposited within the pores of a porous substrate, the coatable composition comprising polymerizable compound such as one or more polymerizable monomer(s) and/or prepolymer(s) or oligomer(s); and a second compatible component.
- the polymerizable compound is reacted (e.g., polymerized) to create the hydrophilic coating.
- a porous substrate serves as a base material in the construction of filtration articles according to the various embodiments of the invention.
- Suitable porous substrates for use in the embodiments of the invention include any of a variety of materials having sufficient porosity for use in filtration applications.
- the substrate includes a first major surface and a second major surface with a plurality of pores extending through the substrate from the first major surface to the second major surface. The pores are dimensioned to permit the passage of a liquid or gas feed through the substrate while trapping particulates or other matter contained within the feed.
- Suitable porous substrates include, but are not limited to, microporous membranes, nonwoven webs, and porous fibers.
- the porous base substrate may be formed from any material.
- the substrate comprises one or more polymeric material(s) which can include, but are not limited to, polyolefms, poly(isoprenes), poly(butadienes), fluorinated polymers, chlorinated polymers, polyesters, polyamides, polyimides, polyethers, poly(ether sulfones), poly(sulfones), polyphenylene oxides, poly( vinyl acetate), copolymers of vinyl acetate, poly(phosphazenes), poly( vinyl esters), poly(vinyl ethers), poly(vinyl alcohols), and poly(carbonates).
- Suitable polyolefms include, but are not limited to, poly(ethylene), poly(propylene), poly(l-butene), copolymers of ethylene and propylene, alpha olefin copolymers (such as copolymers of 1-butene, 1-hexene, 1-octene, and 1-decene), poly(ethylene-co-l-butene) and
- Suitable fluorinated polymers include, but are not limited to, poly( vinyl fluoride), poly(vinylidene fluoride), copolymers of vinylidene fluoride (such as poly(vinylidene fluoride-co-hexafluoropropylene), and copolymers of chlorotrifluoro ethylene (such as poly(ethylene-co-chlorotrifluoroethylene).
- Suitable polyamides include, but are not limited to, poly(imino(l-oxohexamethylene)),
- Suitable polyimides include, but are not limited to,
- Suitable poly(ether sulfones) include, but are not limited to, poly(diphenylether sulfone) and poly(diphenylsulfone-co-diphenylene oxide sulfone).
- Suitable copolymers of vinyl acetate include, but are not limited to, poly(ethylene-co-vinyl acetate) and such copolymers in which at least some of the acetate groups have been hydrolyzed to afford various poly( vinyl alcohols).
- the porous substrate is a microporous substrate having an average pore size less than about 1.0 microns.
- Suitable microporous substrates include, but are not limited to, microporous membranes, and microporous fibers.
- a microporous substrate comprising one or more of the above-mentioned polymeric materials may be hydrophobic.
- the microporous substrate comprises a hydrophobic microporous membrane made by a process comprising thermally-induced phase separation (TIPS) membrane.
- TIPS membranes and methods of making the same include those disclosed in U.S. Pat. Nos. 4,539,256,
- TIPS membrane suitable for use in embodiments of the present invention is a membrane comprising
- TIPS membrane suitable for use in other embodiments of the invention is a TIPS membrane comprising polyolefin such as polypropylene.
- TIPS membrane comprises ethylene- chlorotrifluoro ethylene (ECTFE) copolymer such as are described in PCT International Pub. No. WO 2010/071764.
- ECTFE ethylene- chlorotrifluoro ethylene
- Another suitable PVDF membrane is one prepared using a solvent induced phase separation process (SIPS) such as those commercially available from Millipore Corporation.
- SIPS solvent induced phase separation process
- the polymer is a polyolefin made by thermally induced phase separation (TIPS), or by non- solvent induced phase separation.
- TIPS thermally induced phase separation
- Specific examples of commercially available polyolefin support materials include SUPOR® polyethersulfone membranes manufactured by Pall Corporation, Cole-Parmer® Teflon® membranes, Cole-Parmer® nylon membranes, cellulose ester membranes manufactured by Gelman Sciences, and Whatman® filter and papers.
- Non-polymeric support members, such as ceramic-based supports, can also be used.
- porous substrates comprise fibrous materials.
- fibrous porous substrate include nonwoven webs, woven materials, melt blown materials, and the like.
- fibrous polyolefms are used such as non-woven fibrous polyesters or nonwoven fibrous polypropylenes, including those commercially available, for example, from Hollingsworth and Vose Company.
- Suitable melt blown or woven materials can comprise, for example, polyolefms, polyesters, polyamides or cellulosic materials.
- Suitable porous substrates can be of various shapes and sizes, such as, for example, flat sheets, hollow fibers, and tubular membranes.
- the support member is in the form of a flat sheet that has a thickness of from about 10 to about 1000 microns, in other embodiments from about 10 to about 500 microns, and in still other embodiments from about 10 to about 300 microns.
- Coated porous materials of the invention include a hydrophilic coating on the surfaces of a porous substrate.
- the hydrophilic coating is a single layer of crosslinked polymer and second compatible component, and the hydrophilic coating is formed from a coatable composition formulated to include polymerizable compound and second compatible component in a suitable solvent.
- the second compatible component is thought to facilitate the uniform deposition of polymerizable compound on the surfaces of the porous substrate.
- Any material which can assist in the uniform deposition of the polymerizable compound onto the hydrophobic substrate is suitable for use in a coatable composition according to the present invention.
- suitable second compatible components include surfactants.
- the surfactant may be sorbitan laurate such as is commercially available under the designation "SPAN 20" from Uniqema of New Castle, Delaware.
- a suitable surfactant is triethanolamine dodecylbenze sulfonate.
- suitable surfactant is nonionic alkylphenoxy poly(ethyleneoxy) ethanol.
- sutiable surfactant is propylene oxide - ethylene oxide copolymer, such as is available
- suitable surfactant may include combinations of two or more of the aforementioned surfactants.
- second compatible component is polysaccharide.
- suitable polysaccharide is carboxymethyl cellulose, methyl cellulose, hydropropyl cellulose, in some embodiments hydroethyl cellulose, in some embodiments hydropropylmethyl cellulose, in some embodiments hydrobutylmethyl cellulose, in some embodiments dextran, in some embodiments hydroxyethyl starch.
- suitable polysaccharide may comprise combinations of two or more of the aforementioned polysaccharides.
- second compatible component is a polymer.
- Suitable polymer includes polyvinyl alcohol.
- suitable polymer includes polyvinylpyrrolidone.
- suitable polymer includes combinations of two or more of the aforementioned polymers.
- the polymerizable compound is hydrophilic while being polymerizable in situ (e.g., after being deposited within the pores of the substrate).
- Suitable polymerizable compounds include monomers, prepolymers and/or oligomers having a (a) free-radically polymerizable group that is a first ethylenically unsaturated group and (b) an additional functional group that is a second ethylenically unsaturated group.
- Suitable monomers having two ethylenically unsaturated groups include, but are not limited to, polyalkylene glycol di(meth)acrylates.
- polyalkylene glycol di(meth)acrylate is used interchangeably with the term polyalkylene oxide di(meth)acrylate.
- (meth)acryl as in (meth)acrylate is used to encompass both acryl groups as in acrylates and methacryl groups as in methacrylates.
- the crosslinked polymer results from the reaction of polyethylene glycol di(meth)acrylate monomer and crosslinking agent upon exposure to ultraviolet ("UV") radiation.
- UV ultraviolet
- the polymerization of such monomer converts an otherwise hydrophobic porous substrate into a hydrophilic coated porous material with the hydrophilicity being attributable to the presence of polyalkylene oxide groups.
- the polyethylene glycol diacrylate monomer is a polyethylene glycol di(meth)acrylate monomer (e.g., polyethylene glycol dimethacrylate having an average molecular weight of about 400 g/mole) alone or in combination with other monomers.
- the resulting hydrophilic coating can have a number of desired properties such as instant wettability.
- a suitable monomer will be of a certain minimum molecular weight or larger so as to provide a highly crosslinked polymer in the resulting hydrophilic coating.
- Exemplary polyalkylene glycol di(meth)acrylates include
- Suitable polyethylene glycol diacrylate monomer include those having an average molecular weight of about 300 g/mole or greater, 400 g/mole or greater or 600 g/mole or greater.
- a suitable polyethylene glycol diacrylate monomer having a molecular weight of about 508 g/mole is commercially available, for example, under the trade designation "SR344;” a polyethylene glycol dimethacrylate monomer having an average molecular weight of about 598 g/mole is commercially available under the trade designation "SR603;” and a polyethylene glycol dimethacrylate monomer having a molecular weight of about 742 g/mole is commercially available under the trade designation "SR610," methoxy polyethylene glycol acrylate having a molecular weight of 693 is commercially available under the designation "CD552" all of which are available from Sartomer Co., Inc., Exton, PA.
- Polyethylene glycol diacrylates and polyethylene glycol di(meth)acrylates may be selected based on their general stability or lack of significant volatility so that, once deposited onto a porous substrate, the monomer will be retained in the pores of the substrate at the elevated temperatures used to evaporate solvent from the coatable composition.
- trifunctional monomers such as trifunctional methacrylates and esters thereof.
- trifunctional monomers may comprise those having a molecular weight of about 1 ,000 or greater.
- Suitable trifunctional monomers are commercially available such as, for example, that available under the trade designation "SR9011," having a molecular weight of 1,073 available from Sartomer Co.
- the resulting coated porous material can have a number of desired properties such as instant water-wettability as well as low adhesion to bacteria.
- polymerization of polymerizable compound such as the foregoing monomer(s) results in a highly crosslinked polymer that is included within a single layer along with the aforementioned second compatible component.
- Crosslinked polymers can be obtained by polymerization of monomer, oligomer or prepolymer together with a polyfunctional compound (e.g., a crosslinker).
- a polyfunctional compound e.g., a crosslinker
- crosslinking is accomplished by use of a highly crosslinkable polymer, in a suitable solvent.
- any of a variety of crosslinking agents may be included in the coatable composition.
- crosslinking agents include compounds containing at least two vinyl or acryl groups, for example, 2,2-bis[ 4-(2- acryloxyethoxy)phenyl] propane, 2,2-bis( 4-methacryloxyphenyl)propane, butanediol diacrylate and dimethacrylate, trimethylolpropane diacrylate and dimethacrylate;
- crosslinking agents include ⁇ , ⁇ ',-methylenebisacrylamide, diethylene glycol diacrylate and dimethacrylate, ethylene glycol diacrylate and dimethacrylate, tetra( ethylene glycol) diacrylate, 1,6-hexanediol diacrylate, divinylbenzene, poly(ethylene glycol) diacrylate (e.g., having a mw of 300 or greater as previously mentioned herein), trimethylolpropane triacrylate (TRIM).
- the polymerization reaction is initiated using thermal activation or ultraviolet (UV) irradiation.
- UV ultraviolet
- the coatable composition typically includes a suitable
- photoinitiator which may be selected from, for example, 2-hydroxy-l[4- 2(hydroxyethoxy)phenyl]-2-methyl-l-propanone (IRGACURE 2959), and 2,2-dimethoxy- 2-phenylacetophenone (DMPA).
- Another initiator is 2-hydroxy-2-methyl-l -phenyl- 1- propanone available commercially under the trade designation DAROCUR 1173 (Ciba Specialty Chemicals Corporation, Tarrytown NY).
- Still another suitable photoinitiator is 2,4,6-trimethylbenzoylphenyl phosphinate available from BASF under the trade designation "Lucirin TPO.”
- photoinitiators include benzophenone, benzoin and benzoin ethers such as benzoin ethyl ether and benzoin methyl ether, dialkoxyacetophenones,
- the coatable composition is formulated with a reactive photoinitiator which acts to photoinitiate the polymerization reaction and is itself polyfunctional and, therefore, capable of acting like a crosslinking agent.
- a suitable reactive photoinitiator is VAZPIA which is 2-[4-(2-hydroxy-2- methylpropanoyl)phenoxy]ethyl-2-methyl-2-N-propenoylamino propanoate, as described in U.S. Pat. No. 5,506,279.
- the coatable composition includes solvent.
- a suitable solvent is an aqueous based solvent, typically including an alcohol and optionally another small organic molecule miscible with water and useful in compatibilizing the solvent with the various organic components therein.
- Suitable solvent include, for example, a 70:30 volume/volume mixture of ethanol / water.
- aqueous based solvents may be formulated to organic components other than ethanol such as, for example, n-propanol (up to 90%), isopropanol, t-butanol, butanol, 2-methoxypropanol, acetone, THF.
- solvent should be chosen for its compatibility with the other materials included in the coatable composition and for the ease by which it can be volatilized, as is explained elsewhere herein.
- thermal initiator is included in the coatable composition.
- Thermal initiator may be desired in embodiments wherein the monomer in the coatable composition is prepolymerized in that at least a portion of the composition is partially polymerized or oligomerized prior to applying the coatable composition to the substrate. Prepolymerization may be achieved by thermal activation using a thermal initiator.
- Suitable thermal initiators include for example l, -azobis(cyclohexanecarbonitrile) (VAZO® catalyst 88), azobis(isobutyronitrile) (AIBN), 4,4'-azobis(4-cyanopentanoic acid), potassium persulfate, ammonium persulfate, and benzoyl peroxide.
- the coatable composition is prepared by mixing the foregoing components in a solvent.
- a solvent Those of ordinary skill in the art will appreciate that the exact order of mixing and the relative proportions of the foregoing components and solvent are not limiting. The exact amounts of the various components may be varied within fairly broad limits.
- Second compatible component may be provided in the coatable composition at a concentration less than 15%, in some embodiments less than 10%, in some embodiments less that 5% and in some embodiments less that 2%.
- Polymerizable compound may be present at a concentration less than 15%, in some embodiments less than 10% and in some embodiments less that 5%.
- Photoinitiator may be present in the coatable composition at a concentration of less than 6%, in some embodiments less than 2% and in some
- the solvent is an aqueous solvent with a compatible organic component.
- the solvent can comprise a water/alcohol mixture wherein the volume percentage of alcohol is between about 40% and 90%>, between about 55% and 80%>, between about 65%> and 75%, and in some embodiments the volume percentage of alcohol is about 70%.
- articles are provided in the form of coated porous materials suitable for use in filtration applications.
- the coated porous materials are made according to the process(es) described herein so that finished materials includes a porous substrate, as described herein, with a first major surface and a second major surface and a plurality of pores extending through the substrate generally from the first major surface to the second major surface.
- Each pore includes an inner pore wall which defines the internal dimension or diameter of the pore.
- a hydrophilic coating covers at least a portion of the surfaces of the porous substrate, and the coating is affixed or adhered to at least such surfaces of the substrate, including the inner pore walls.
- the hydrophilic coating comprises second compatible component and at least one crosslinked polymer in a single layer.
- the second compatible component remains substantially unreacted with the crosslinked polymer, and the hydrophilic coating is neither grafted nor covalently bonded to the surfaces of the porous substrate.
- the hydrophilic coating covers the surfaces of the porous substrate without fully occupying the void volume within the pores of the substrate. Liquid passing through the pores of the coated porous material will flow in proximity to the hydrophilic coating and generally not between the coating and the surfaces of the substrate.
- the hydrophilic coating is "affixed or adhered to" the surfaces of the porous substrate in the sense that the hydrophilic coating is substantially retained within the pores of the substrate when water or an aqueous solution is passed through the coated porous material. In embodiments of the described materials, less than one percent by weight of the hydrophilic coating is lost when the coated porous material is submerged in water for up to 30 days.
- the coated porous material comprises a porous substrate in the form of a TIPS membrane such as a membrane formed from polypropylene or from polyvinylidene fluoride, for example.
- the hydrophilic coating is comprised of highly crosslinked polymer derived from polyethylene glycol di(meth)acrylate and VAZPIA reactive photoinitiator provided in sufficient amount to serve as a crosslinker and second compatible component.
- the coated porous materials exhibit a desirable flux or water flow rate as is described in the Test Methods employed for the various Examples herein. This test measures the time for a predetermined volume of water to pass through a substrate, and the water flow rate (flux) is calculated using the time, vacuum pressure, and area of the substrate and is expressed in L/(m 2 .h.psi).
- the flux water flow rate
- the flux is typically similar to the flux for the uncoated porous substrate, thus indicating that the hydrophilic coating produces little change in pore size as compared with the uncoated porous substrate.
- embodiments of the coated porous materials exhibit a high surface energy (e.g., higher than the surface energy of the uncoated porous substrate).
- the coated porous material exhibits a surface energy of 50 dynes/cm or greater, in some embodiments the coated porous material exhibits a surface energy of 65 dynes/cm or greater, in other embodiments the coated porous material exhibits a surface energy of 80 dynes/cm or greater, and in still other embodiments the coated porous material exhibits a surface energy of 85 dynes/cm or greater.
- coatable composition prepared as described herein, is applied to a porous substrate.
- the coatable composition may be prepared and applied without first
- the coatable composition is prepared with an unreacted polymerizable compound that consists of or comprises monomer, and the composition is applied to the porous substrate without creating conditions under which the monomer would normally react to oligomerize.
- the coatable composition is prepared by simply mixing one or more monomer(s), optionally one or more crosslinking agents, optionally one or more initiators, second compatible component in one or more suitable solvents. Suitable examples of the foregoing materials are given above.
- compositions of the coatable composition are blended so that the composition is substantially homogeneous, but may be slightly heterogeneous.
- the coatable composition is then applied to a suitable porous substrate, typically by soaking the substrate in the coatable composition for a sufficient amount of time to allow the composition to enter and substantially fill the pores of the substrate. Excess coatable composition may be removed from the outer surfaces of the porous substrate by known lamination techniques or the like.
- the coated porous substrate is rewetted with a suitable rewetting agent such as water or a suitable aqueous solution including, for example, an aqueous salt (e.g., sodium chloride or other inorganic salt) solution or another aqueous solution of known inorganic or organic materials or the like.
- a suitable rewetting agent such as water or a suitable aqueous solution including, for example, an aqueous salt (e.g., sodium chloride or other inorganic salt) solution or another aqueous solution of known inorganic or organic materials or the like.
- a suitable salt solution comprises an aqueous solution of sodium chloride at a concentration less than about 30% and in some embodiments at a concentration of about 20%.
- Rewetting agent serves several functions such as, for example, elimination of the inhibiting effects of oxygen during UV curing. Additionally, the rewetting agent reduces the impact of heat generated by UV sources, particularly from medium pressure mercury lamps. Also, the rewetting agent helps to organize polar groups in the monomer molecules of the coatable composition so that, once cured, the hydrophilic coating comprises a high density of polar groups, which contribute to a high surface energy on the finished coated porous material.
- polymerizable compound in the coatable composition comprises one or more polar monomer(s) selected to have limited solubility in the rewetting agent to prevent the loss of monomer into the rewetting agent along with a reduction of the initial monomer concentration.
- the polar monomer(s) is(are) selected to provide a highly crosslinked polymer possessing certain physical properties such as heat stability, resistance to biomolecule adsorption, resistance to strong alkaline solutions, and having low levels of extractable matter, for example.
- polymerization reaction is initiated and allowed to run to completion to form the hydrophilic coating.
- polymerization may be initiated by, for example, thermal activation or by UV irradiation. Thermal activation is generally less preferred because of the tendency of the
- the porous substrate containing a coatable composition of monomer (or oligomer), crosslinking agent and photo initiator is subjected to UV irradiation at wavelengths of from about 200 nm to about 600 nm, for a period of a few seconds to a few hours.
- UV irradiation can be broad band or narrow band and the intensity of the UV source may be varied within known parameters, typically with peak power densities ranging from 5 to 600 mW/cm 2 or higher.
- the porous substrate is provided as a continuous web of material which, following saturation by the coatable composition, may undergo the polymerization reaction in a continuous process in which the web is exposed to UV radiation as it passes underneath or in proximity to a UV source at a controlled speed.
- the porous substrate and coatable composition therein are exposed to UV radiation along both major surfaces, either sequentially or simultaneously. Sequential exposure to a UV source typically requires a first exposure to a UV source that has been positioned on one side of the web or substrate. Thereafter, the web is turned over and the second side of the substrate is exposed to substantially the same dose of UV radiation to essentially completely polymerize the polymerizable compound in the pores of the substrate.
- the continuous web may be supported on a carrier.
- the web carrier may be selected to permit transmittance of the UV radiation therethrough so that the radiation is not blocked from initiating the polymerization reaction within the pores of the substrate.
- biaxially oriented polypropylene (BOPP) film is an example of a material suitable for supporting the substrate during UV irradiation and polymerization.
- the saturated porous substrate may be positioned between (e.g., "sandwiched") layers of BOPP during irradiation. The layers of film on either side of the porous substrate served to support the substrate, allow for the transmittance of UV radiation therethrough and prevent the loss of rewetting solution in and maintain a level of moisture in the substrate during processing.
- the coated porous material may be washed to remove remaining salt solution, unreacted materials, residual solvent, and the like.
- the coated porous material may be dried by evaporation of the remaining liquid (e.g., wash water) by evaporation at room temperature or at an elevated temperature.
- the foregoing process additionally involves an optional prepolymerization or oligomerization step prior to applying the coatable composition to the porous substrate.
- the prepolymerization step may be achieved by thermal initiation, in the presence of a thermal initiator, of the polymerization reaction before the coatable composition is applied to a porous substrate.
- the degree of polymerization achieved in this step is controlled in a known manner by, for example, using a limiting amount of initiator, control of the reaction time and temperature (e.g., by quenching at a predetermined time after initiation) and the like.
- the coatable composition may be applied to the porous substrate and further processed as described herein. Suitable thermal initiators may be selected from known materials including those previously mentioned.
- the coatable composition is formulated with UV initiator and applied to the porous substrate.
- the composition Prior to removing solvent from the coatable composition as described herein, the composition is subjected to a first or initial exposure of UV radiation to initiate a prepolymerization step.
- the prepolymerization reaction is controlled to permit the reaction of monomer and to provide oligomers but to avoid running the reaction to completion (e.g., full polymerization) at this stage of the manufacturing process.
- the degree of pre -polymerization or oligomerization may be controlled by, for example, the use of a limited amount of a first initiator as is further explained herein, by control of the UV exposure (e.g., control of exposure time) or the like.
- the initiator may be selected for its sensitivity to a selected first UV wavelength that is used only during the prepolymerization step, and wherein the first UV wavelength is different than the UV wavelength that is used to fully polymerize the polymerizable compound.
- the coatable composition can be formulated to include more than one UV initiator - i.e., a first initiator to sensitive to a first UV wavelength effective to initiate the oligomerization reaction and a second initiator sensitive to a second UV wavelength that is effective to initiate the polymerization reaction previously described.
- a rewetting solution e.g., aqueous NaCl
- solvent is removed from the coatable composition and a rewetting solution (e.g., aqueous NaCl) is applied to the substrate and the rewetted substrate is again UV irradiated to complete the polymerization reaction and provide a hydrophilic coating.
- a rewetting solution e.g., aqueous NaCl
- the various embodiments of the invention include articles (e.g., coated porous materials) and processes (e.g., for the manufacture of coated porous materials).
- coated porous materials of the invention may be used in any of a variety of filtration applications including ultrafiltration, wherein the hydrophilic coating can be either charged or neutral, and in microfiltration for use in, for example, health care, food & beverage, and/or industrial markets.
- Specific applications can include fuel cell and battery separator applications, for example.
- the coated porous materials of the invention may be used to carry out separations in aqueous media as well as in non-aqueous fluids.
- the coated porous materials may be provided as membranes, films and/or as components in any of a variety of articles made for filtration applications.
- the coated porous materials of the invention are capable of being flexed, folded, or pleated without breaking or crumbling to the touch, making them suitable for use in a filter cartridge or in other filtration devices requiring high surface area materials.
- coated porous materials comprised of membrane materials as the porous substrate can provide low fouling propensity and a high filtration efficiency.
- the coated porous materials described herein may be further modified by depositing any of a variety of compositions thereon using known coating or deposition techniques.
- the coated porous materials may be metal coated using vapor deposition or sputtering techniques, or the coated porous materials may be coated with adhesive, aqueous or solvent based coating compositions or dyes, for example.
- unique articles are provided by laminating coated porous materials to another structure or material, such as other sheet materials (e.g., fabric layers, woven, nonwoven, knitted, or mesh fabrics), polymeric film layers, metal foil layers, foam layers, or any combination thereof to provide composite structures. Lamination can be accomplished using conventional techniques that include adhesive bonding, spot welding, or by other techniques that do not destroy or otherwise interfere with the desired porosity of the coated porous material.
- Multilayered filtration articles may additionally be made from (i) one or more layers of coated porous materials based on a porous substrate in the form of a membrane as described herein, and (ii) one or more layers of coated porous materials based on a porous substrate in the form of a nonwoven, for example.
- other materials may also be included in a multilayered filtration article so that some of the layers are coated porous materials, as described herein, and the other layers comprise membrane(s) or fibrous filtration constructions other than those described herein.
- Dyne solutions from two different sets (30-70 dynes/cm from Jemmco, LLC, Mequon WI; 73-87 dyne/cm solutions formulated according to Handbook of Chemistry and Physics, 71 st edition, CRC press) were used. All solutions were dropped onto a substrate (e.g., a membrane) using a plastic pipette. The drop volume was about 0.5ml. The time for a dyne solution to penetrate through the membrane was recorded by a stopwatch. A light trans-illuminator was used for easy detection of the dyne solution penetration. The membrane surface energy was recorded as the surface tension of the highest dyne solution which penetrated through the membrane in less than one second. Three test replicates were used and averaged for each measurement.
- a 47 mm disk of a test substrate was mounted in a Gelman magnetic holder (Gelman Sciences, Inc., Ann Arbor, Mich.).
- the active substrate diameter in the holder was 34 mm.
- a vacuum pump running at approximately 60 cm (23.5 inches) of mercury Hg) was applied to draw water through the substrate.
- the time for 100 ml water to pass through the substrate was recorded with a stopwatch.
- the water flow rate (flux) was calculated using the time, vacuum pressure, and area of the substrate and expressed in L/(m 2 .h.psi). Two to three test replicates were used and averaged for each measurement.
- the bubble point pore sizes of the substrates were measured according to ASTM-F316-03.
- a substrate was pre-wetted with isopropanol and then mounted onto a test holder. Pressurized nitrogen gas was gradually applied to one side of the substrate until the gas flow detected at the other side reached 100%. The pressure at 100% gas flow through the substrate was recorded and used to calculate the bubble point pore size. Two to three replicates were used and averaged for each measurement.
- sample substrates were first completely wetted by immersing in them in deionized water and then placed between a sandwich of two paper towel sheets.
- the test sandwich was placed in a Thelco Lab Oven (Thermo Electron Corporation, Marietta, Ohio) for 30 min with a set point temperature of 136°C.
- the substrate was then tested for water wettability and surface energy according to the above test methods.
- Example 1 (prophetic)
- a 5.0 wt% stock solution is made by dissolving one or more of the second compatible components listed herein in an ethanol (AAPER Alcohol and Chemical Co. Shelbyville, KY)/water solvent mixture (70.0 vol% ethanol) in a water bath at a temperature within the range of 70-80°C.
- a coatable composition is made from the above stock solution by adding 4.0 wt% polyethylene glycol diacrylate (SR610, Sartomer, Warrington, PA) and 1.0 wt% reactive photoinitiator VAZPIA ( 2-[4-(2-hydroxy-2- methylpropanoyl)phenoxy]ethyl-2-methyl-2-N-propenoylamino propanoate, (disclosed in U.S. Pat. No. 5,506,279) in ethanol/water mixture solvent (70.0 vol% ethanol).
- the final concentration of the copolymer in the coatable composition is 1.0 wt%.
- a microporous polypropylene membrane (F100, 3M Purification Inc. Meriden,
- CT is saturated with the coatable composition by placing samples of the membrane ranging from 516 cm 2 to 1426cm 2 in a heavy weight polyethylene (PE) bag along with 10 to 100 ml of coatable composition and letting the composition soak into the membrane for a minute or less. Excess coatable composition on the surface of the membrane is then removed with by blotting on a paper towel after the membrane is removed from the PE bag. The membrane is allowed to dry at room temperature for 10-12 hours. The dried membrane is placed into another PE bag and 10 to 100 ml of rewetting solution, - i.e., 20.0 wt% NaCl aqueous solution was added into the bag. The membrane is instantly wetted with the salt solution and is then removed from the bag.
- PE polyethylene
- the coatable composition is cured by passing the membrane on a conveying belt through a nitrogen inert Fusion UV system equipped with an H-bulb with an aluminum reflector.
- the speed of the belt was 6.1 meters/min (20 feet/minute).
- the membrane is then turned over to expose the other side to the UV source and passed through the UV system again at 6.1 meters/min
- the coated porous material is then washed in de -ionized water and dried at 90°C
- the coated porous material is tested according to the above test methods.
- the material will exhibit a surface energy greater than about 50 dynes/cm, a bubble point pore size of about 0.30 ⁇ or greater and water flow rate of about 500 L/m 2 . h.psi, or greater.
- the uncoated base membrane is also tested, exhibiting a bubble point pore size and water flow rate that are comparable to those for the coated porous material, thus indicating that the cured membrane will maintain its pore microstructure.
Abstract
A process for the preparation of coated porous material, the process including the steps of: a) providing a porous substrate with a plurality of pores extending through the substrate from a first major surface to a second major surface, each pore having an inner pore wall defining the internal dimension of the pore; b) applying a coatable composition to at least a portion of the inner pore walls of the porous substrate, the coatable composition made with at least one polymerizable compound, a second compatible component and solvent; c) removing the solvent from the coatable composition; d) saturating the porous substrate and the coatable composition with a rewetting solution; and e) polymerizing the polymerizable compound to form a hydrophilic coating on the pore walls and to provide the coated porous material, the hydrophilic coating. In other aspects, coated porous material made from the foregoing process is also provided.
Description
PROCESS FOR MAKING COATED POROUS MATERIALS
Cross Reference to Related Application
This application claims the benefit of U.S. Provisional Patent Application Nos. 61/350,154, filed June 1, 2010; and 61/351,447, filed June 4, 2010, the disclosures of which are incorporated by reference herein in their entireties.
Technical Field
This invention relates to coated porous materials that include hydrophilic coatings and which are useful as separation or filtration media, and to processes for the preparation of coated porous materials.
Background
Reducing the hydrophobicity (or increasing the hydrophilicity) of a filtration substrate (e.g., a membrane) is desired in order to reduce fouling during use. While many of the least expensive and most stable substrate-forming materials are hydrophobic polymers, the art has developed methods for modifying the polymer surface of a substrate to render it hydrophilic and thus more readily wettable with water. To decrease the hydrophobicity inherent to many polymeric materials, the art has known to either chemically modify the surface and pore -walls of a substrate or, alternatively, to coat the walls of the pores in the substrate with a hydrophilic layer, the layer usually being polymeric in nature. The hydrophilic layer improves the affinity of the substrate material towards water, increasing its wettability and, in some cases, making the substrate completely wettable by water.
Early efforts in the art to adhere the hydrophilic layer to a substrate included activating the walls of the pores in the substrate (e.g., with a plasma treatment) such that a hydrophilic coating could be chemically attached to the pore walls. The attachment of grafted coatings can also be made by depositing a mixture of monomers within the pores of the substrate and inducing a polymerization reaction in a manner that promotes grafting of the thus formed hydrophilic polymer to the walls of the substrate. However, in the absence of substantial crosslinking, a grafted layer can become hydrated and expand to the point of essentially filling and blocking the pores of the substrate.
Although the art of hydrophilic filtration media has seen some advances, more improvements are desired.
Summary
The present invention provides a process for making hydrophilic filtration media which demonstrates a low level of swelling when wet and possesses a surface that is rich in polar functional groups. The filtration media experiences minimal pore-plugging in use and typically demonstrates a high surface energy. Moreover, the filtration media is readily made using an efficient process.
In various embodiments, the invention provides a process for the preparation of coated porous material, the process comprising:
a) Providing a porous substrate comprising a plurality of pores extending through the substrate from a first major surface to a second major surface, each pore comprising an inner pore wall defining the internal dimension of the pore;
b) Applying a coatable composition to at least a portion of the inner pore walls of the porous substrate, the coatable composition comprising at least one polymerizable compound, a second compatible component and solvent; c) Removing the solvent from the coatable composition;
d) Saturating the porous substrate and the coatable composition with a
rewetting solution; and
e) Polymerizing the polymerizable compound to form a hydrophilic coating on the pore walls and to provide the coated porous material, the hydrophilic coating comprising both the second compatible component and a crosslinked polymer in a single layer.
In other embodiments, the invention provides a coated porous material made from the foregoing process.
Various terms used herein to describe aspects of the various embodiments of the invention will be understood to have the meaning known to persons of ordinary skill in the art. For clarity, certain terms will be understood to have the meaning set forth herein.
As used herein, "hydrophilic" is used as being indicative of a property in which a molecule, substance or article demonstrates an affinity for water by, for example, hydrogen bonding with water.
As used herein, "interpenetrating polymer network" refers to two or more polymer networks which are at least partially interlaced on a molecular scale but not covalently bonded to each other. Such a network cannot be separated unless chemical bonds are broken.
As used herein, "a," "an," "the," "at least one," and "one or more" are used interchangeably. Thus, for example, an article that comprises "a" membrane can be interpreted to mean that the article includes "one or more" membranes.
Also herein, any recitation of a numerical range by endpoints includes all numbers subsumed within that range (e.g., 1 to 5 includes 1, 1.5, 2, 2.75, 3, 3.80, 4, 5, etc.).
Unless otherwise indicated, all numbers expressing feature sizes, amounts, and physical properties used in the specification and claims are to be understood as being modified in all instances by the term "about." Accordingly, unless indicated to the contrary, the numerical parameters set forth in the foregoing specification and attached claims are approximations that can vary depending upon the desired properties sought to be obtained by those skilled in the art utilizing the teachings disclosed herein.
The above summary is not intended to describe all possible embodiments or every implementation of the present invention. Those of ordinary skill in the art will more fully understand the scope of the invention upon consideration of description that follows.
Detailed Description
Composite materials and, more particularly, coated porous materials are provided having a porous substrate and a hydrophilic coating on the walls of at least some of the pores within the substrate. The hydrophilic coating is a single layer of materials that includes at least one crosslinked polymer and a second compatible component (e.g., compatible with the crosslinked polymer and a precursor thereof). The presence of the hydrophilic coating within the pores of the substrate alters the surface properties of the substrate. The coated porous material is made according to a process wherein a coatable composition is deposited within the pores of a porous substrate, the coatable composition comprising polymerizable compound such as one or more polymerizable monomer(s)
and/or prepolymer(s) or oligomer(s); and a second compatible component. The polymerizable compound is reacted (e.g., polymerized) to create the hydrophilic coating.
Porous Substrate
A porous substrate serves as a base material in the construction of filtration articles according to the various embodiments of the invention. Suitable porous substrates for use in the embodiments of the invention include any of a variety of materials having sufficient porosity for use in filtration applications. Typically, the substrate includes a first major surface and a second major surface with a plurality of pores extending through the substrate from the first major surface to the second major surface. The pores are dimensioned to permit the passage of a liquid or gas feed through the substrate while trapping particulates or other matter contained within the feed.
Suitable porous substrates include, but are not limited to, microporous membranes, nonwoven webs, and porous fibers. The porous base substrate may be formed from any material. In some embodiments, the substrate comprises one or more polymeric material(s) which can include, but are not limited to, polyolefms, poly(isoprenes), poly(butadienes), fluorinated polymers, chlorinated polymers, polyesters, polyamides, polyimides, polyethers, poly(ether sulfones), poly(sulfones), polyphenylene oxides, poly( vinyl acetate), copolymers of vinyl acetate, poly(phosphazenes), poly( vinyl esters), poly(vinyl ethers), poly(vinyl alcohols), and poly(carbonates). Suitable polyolefms include, but are not limited to, poly(ethylene), poly(propylene), poly(l-butene), copolymers of ethylene and propylene, alpha olefin copolymers (such as copolymers of 1-butene, 1-hexene, 1-octene, and 1-decene), poly(ethylene-co-l-butene) and
poly(ethylene-co-l-butene-co-l-hexene). Suitable fluorinated polymers include, but are not limited to, poly( vinyl fluoride), poly(vinylidene fluoride), copolymers of vinylidene fluoride (such as poly(vinylidene fluoride-co-hexafluoropropylene), and copolymers of chlorotrifluoro ethylene (such as poly(ethylene-co-chlorotrifluoroethylene). Suitable polyamides include, but are not limited to, poly(imino(l-oxohexamethylene)),
poly(iminoadipoyliminohexamethylene), poly(iminoadipoyliminodecamethylene), and polycaprolactam. Suitable polyimides include, but are not limited to,
poly(pyromellitimide). Suitable poly(ether sulfones) include, but are not limited to, poly(diphenylether sulfone) and poly(diphenylsulfone-co-diphenylene oxide sulfone).
Suitable copolymers of vinyl acetate include, but are not limited to, poly(ethylene-co-vinyl acetate) and such copolymers in which at least some of the acetate groups have been hydrolyzed to afford various poly( vinyl alcohols).
In one exemplary embodiment, the porous substrate is a microporous substrate having an average pore size less than about 1.0 microns. Suitable microporous substrates include, but are not limited to, microporous membranes, and microporous fibers. A microporous substrate comprising one or more of the above-mentioned polymeric materials may be hydrophobic. In some embodiments, the microporous substrate comprises a hydrophobic microporous membrane made by a process comprising thermally-induced phase separation (TIPS) membrane. Suitable TIPS membranes and methods of making the same include those disclosed in U.S. Pat. Nos. 4,539,256,
4,726,989, 4,867,881, 5,120,594 and 5,260,360. One exemplary TIPS membrane suitable for use in embodiments of the present invention is a membrane comprising
poly(vinylidene fluoride) (i.e., PVDF). Another exemplary TIPS membrane suitable for use in other embodiments of the invention is a TIPS membrane comprising polyolefin such as polypropylene. Still another exemplary TIPS membrane comprises ethylene- chlorotrifluoro ethylene (ECTFE) copolymer such as are described in PCT International Pub. No. WO 2010/071764. Another suitable PVDF membrane is one prepared using a solvent induced phase separation process (SIPS) such as those commercially available from Millipore Corporation.
Many porous materials can be used as the substrate. In specific embodiments, the polymer is a polyolefin made by thermally induced phase separation (TIPS), or by non- solvent induced phase separation. Specific examples of commercially available polyolefin support materials include SUPOR® polyethersulfone membranes manufactured by Pall Corporation, Cole-Parmer® Teflon® membranes, Cole-Parmer® nylon membranes, cellulose ester membranes manufactured by Gelman Sciences, and Whatman® filter and papers. Non-polymeric support members, such as ceramic-based supports, can also be used.
In some embodiments, porous substrates comprise fibrous materials. Examples of fibrous porous substrate include nonwoven webs, woven materials, melt blown materials, and the like. In some embodiments, fibrous polyolefms are used such as non-woven fibrous polyesters or nonwoven fibrous polypropylenes, including those commercially
available, for example, from Hollingsworth and Vose Company. Suitable melt blown or woven materials can comprise, for example, polyolefms, polyesters, polyamides or cellulosic materials.
Suitable porous substrates can be of various shapes and sizes, such as, for example, flat sheets, hollow fibers, and tubular membranes. In some embodiments, the support member is in the form of a flat sheet that has a thickness of from about 10 to about 1000 microns, in other embodiments from about 10 to about 500 microns, and in still other embodiments from about 10 to about 300 microns. Components of a Coatable Composition
Coated porous materials of the invention include a hydrophilic coating on the surfaces of a porous substrate. The hydrophilic coating is a single layer of crosslinked polymer and second compatible component, and the hydrophilic coating is formed from a coatable composition formulated to include polymerizable compound and second compatible component in a suitable solvent.
In general and without wishing to be bound by theory, the second compatible component is thought to facilitate the uniform deposition of polymerizable compound on the surfaces of the porous substrate. Any material which can assist in the uniform deposition of the polymerizable compound onto the hydrophobic substrate is suitable for use in a coatable composition according to the present invention. Examples of suitable second compatible components include surfactants. In some embodiments, the surfactant may be sorbitan laurate such as is commercially available under the designation "SPAN 20" from Uniqema of New Castle, Delaware. In some embodiments, a suitable surfactant is triethanolamine dodecylbenze sulfonate. In some embodiments, suitable surfactant is nonionic alkylphenoxy poly(ethyleneoxy) ethanol. In some embodiments, sutiable surfactant is propylene oxide - ethylene oxide copolymer, such as is available
commercially under the trade designation "PLURONICS" from BASF Corporation. In still other embodiments, suitable surfactant may include combinations of two or more of the aforementioned surfactants.
In some embodiments, second compatible component is polysaccharide. In some embodiments suitable polysaccharide is carboxymethyl cellulose, methyl cellulose, hydropropyl cellulose, in some embodiments hydroethyl cellulose, in some embodiments
hydropropylmethyl cellulose, in some embodiments hydrobutylmethyl cellulose, in some embodiments dextran, in some embodiments hydroxyethyl starch. And, in some embodiments suitable polysaccharide may comprise combinations of two or more of the aforementioned polysaccharides.
In some embodiments, second compatible component is a polymer. Suitable polymer includes polyvinyl alcohol. In some embodiments, suitable polymer includes polyvinylpyrrolidone. In still other embodiments, suitable polymer includes combinations of two or more of the aforementioned polymers.
Those of ordinary skill in the art will appreciate that other materials may also be suitable as second compatible components including without limitation additional surfactants, polysaccharides, polymers and combinations of any of these materials.
In embodiments of the invention, the polymerizable compound is hydrophilic while being polymerizable in situ (e.g., after being deposited within the pores of the substrate). Suitable polymerizable compounds include monomers, prepolymers and/or oligomers having a (a) free-radically polymerizable group that is a first ethylenically unsaturated group and (b) an additional functional group that is a second ethylenically unsaturated group. Suitable monomers having two ethylenically unsaturated groups include, but are not limited to, polyalkylene glycol di(meth)acrylates. As used herein, the term polyalkylene glycol di(meth)acrylate is used interchangeably with the term polyalkylene oxide di(meth)acrylate. The term "(meth)acryl" as in (meth)acrylate is used to encompass both acryl groups as in acrylates and methacryl groups as in methacrylates.
In one exemplary embodiment, the crosslinked polymer results from the reaction of polyethylene glycol di(meth)acrylate monomer and crosslinking agent upon exposure to ultraviolet ("UV") radiation. The polymerization of such monomer converts an otherwise hydrophobic porous substrate into a hydrophilic coated porous material with the hydrophilicity being attributable to the presence of polyalkylene oxide groups. In one desired embodiment, the polyethylene glycol diacrylate monomer is a polyethylene glycol di(meth)acrylate monomer (e.g., polyethylene glycol dimethacrylate having an average molecular weight of about 400 g/mole) alone or in combination with other monomers. The resulting hydrophilic coating can have a number of desired properties such as instant wettability.
In certain embodiments, a suitable monomer will be of a certain minimum molecular weight or larger so as to provide a highly crosslinked polymer in the resulting hydrophilic coating. Exemplary polyalkylene glycol di(meth)acrylates include
polyethylene glycol di(meth)acrylate monomers and polypropylene glycol
di(meth)acrylates monomers. Suitable polyethylene glycol diacrylate monomer include those having an average molecular weight of about 300 g/mole or greater, 400 g/mole or greater or 600 g/mole or greater. A suitable polyethylene glycol diacrylate monomer having a molecular weight of about 508 g/mole is commercially available, for example, under the trade designation "SR344;" a polyethylene glycol dimethacrylate monomer having an average molecular weight of about 598 g/mole is commercially available under the trade designation "SR603;" and a polyethylene glycol dimethacrylate monomer having a molecular weight of about 742 g/mole is commercially available under the trade designation "SR610," methoxy polyethylene glycol acrylate having a molecular weight of 693 is commercially available under the designation "CD552" all of which are available from Sartomer Co., Inc., Exton, PA. Polyethylene glycol diacrylates and polyethylene glycol di(meth)acrylates may be selected based on their general stability or lack of significant volatility so that, once deposited onto a porous substrate, the monomer will be retained in the pores of the substrate at the elevated temperatures used to evaporate solvent from the coatable composition.
Additionally, some embodiments comprise trifunctional monomers such as trifunctional methacrylates and esters thereof. In some embodiments, trifunctional monomers may comprise those having a molecular weight of about 1 ,000 or greater.
Suitable trifunctional monomers are commercially available such as, for example, that available under the trade designation "SR9011," having a molecular weight of 1,073 available from Sartomer Co.
More than one specific monomer may be included within a coatable composition. With further processing, explained herein, the resulting coated porous material can have a number of desired properties such as instant water-wettability as well as low adhesion to bacteria.
In the various embodiments of the invention, polymerization of polymerizable compound such as the foregoing monomer(s) results in a highly crosslinked polymer that is included within a single layer along with the aforementioned second compatible
component. Crosslinked polymers can be obtained by polymerization of monomer, oligomer or prepolymer together with a polyfunctional compound (e.g., a crosslinker). In some embodiments, crosslinking is accomplished by use of a highly crosslinkable polymer, in a suitable solvent. To achieve and/or enhance the degree of crosslinking of the polymer in the hydrophilic coating, any of a variety of crosslinking agents may be included in the coatable composition. Examples of crosslinking agents include compounds containing at least two vinyl or acryl groups, for example, 2,2-bis[ 4-(2- acryloxyethoxy)phenyl] propane, 2,2-bis( 4-methacryloxyphenyl)propane, butanediol diacrylate and dimethacrylate, trimethylolpropane diacrylate and dimethacrylate;
pentanediol diacrylate and dimethacrylate, pentaerythritol diacrylate and dimethacrylate
1,6-hexanediol diacrylate; 1 ,4-cyclohexanediol diacrylate and dimethacrylate, bisphenol A diacrylate and dimethacrylates; ethyoxylated bisphenol A diacrylate and dimethacrylates; 1,10-dodecanediol diacrylate and dimethacrylate, 2,2-dimethylpropanediol diacrylate and dimethacrylate, dipropylene glycol diacrylate and dimethacrylate; tripropylene glycol diacrylate and dimethacrylate; poly(propylene) diacrylate and diamethacrylate, triethylene glycol diacrylate and dimethacrylate, dipentaerythritol dimethacrylate and diacrylate, glycerol tris(acryloxypropyl) ether, trimethylolpropane triacrylate and trimethacrylate, ethoxylated trimethylolpropane triacrylate and trimethacrylate; glycerol trimethacrylate, pentaerythritol triacrylate and trimethacrylate, dipentaerythritol trimethacrylate and triacrylate, isocyanurate triacrylate; pentaerythritol tetraacrylate and tetramethacrylate, dipentaerythritol tetramethacrylate and tetraacrylate, sorbitol pentamethacrylate;
dipentaerythritol penta-/hexaacrylate, 1 ,4-butanediol divinyl ether; triethylene glycol divinyl ether; diallylphthalate; divinylbenzene, trivinylbenzene, divinylnaphthalene, trivinylcyclohexane, divinylsulfone; divinylformamide; Ν,Ν',-methylenebisacrylamide; 1 ,4-diacryloylpiperazine, N,N'-hexamethylenebisacrylamide,
Ν,Ν'-octamethylenebisacrylamide, N,N-dodecamethylenebisacrylamide,
Ν,Ν'-bisacrylamidoacetic acid. Particularly preferred crosslinking agents include Ν,Ν',-methylenebisacrylamide, diethylene glycol diacrylate and dimethacrylate, ethylene glycol diacrylate and dimethacrylate, tetra( ethylene glycol) diacrylate, 1,6-hexanediol diacrylate, divinylbenzene, poly(ethylene glycol) diacrylate (e.g., having a mw of 300 or greater as previously mentioned herein), trimethylolpropane triacrylate (TRIM).
In some embodiments, the polymerization reaction is initiated using thermal activation or ultraviolet (UV) irradiation. In embodiments where the polymerization reaction is UV initiated, the coatable composition typically includes a suitable
photoinitiator which may be selected from, for example, 2-hydroxy-l[4- 2(hydroxyethoxy)phenyl]-2-methyl-l-propanone (IRGACURE 2959), and 2,2-dimethoxy- 2-phenylacetophenone (DMPA). Another initiator is 2-hydroxy-2-methyl-l -phenyl- 1- propanone available commercially under the trade designation DAROCUR 1173 (Ciba Specialty Chemicals Corporation, Tarrytown NY). Still another suitable photoinitiator is 2,4,6-trimethylbenzoylphenyl phosphinate available from BASF under the trade designation "Lucirin TPO."
Other photoinitiators include benzophenone, benzoin and benzoin ethers such as benzoin ethyl ether and benzoin methyl ether, dialkoxyacetophenones,
hydroxyalkylphenones, and a-hydroxymethyl benzoin sulfonic esters.
In certain embodiments, the coatable composition is formulated with a reactive photoinitiator which acts to photoinitiate the polymerization reaction and is itself polyfunctional and, therefore, capable of acting like a crosslinking agent. In such an embodiments, a suitable reactive photoinitiator is VAZPIA which is 2-[4-(2-hydroxy-2- methylpropanoyl)phenoxy]ethyl-2-methyl-2-N-propenoylamino propanoate, as described in U.S. Pat. No. 5,506,279.
The coatable composition includes solvent. In various embodiments, a suitable solvent is an aqueous based solvent, typically including an alcohol and optionally another small organic molecule miscible with water and useful in compatibilizing the solvent with the various organic components therein. Suitable solvent include, for example, a 70:30 volume/volume mixture of ethanol / water. In some embodiments, aqueous based solvents may be formulated to organic components other than ethanol such as, for example, n-propanol (up to 90%), isopropanol, t-butanol, butanol, 2-methoxypropanol, acetone, THF. Other materials can be used as will be known by those of ordinary skill in the art. In general, solvent should be chosen for its compatibility with the other materials included in the coatable composition and for the ease by which it can be volatilized, as is explained elsewhere herein.
In some embodiments, thermal initiator is included in the coatable composition. Thermal initiator may be desired in embodiments wherein the monomer in the coatable
composition is prepolymerized in that at least a portion of the composition is partially polymerized or oligomerized prior to applying the coatable composition to the substrate. Prepolymerization may be achieved by thermal activation using a thermal initiator.
Suitable thermal initiators include for example l, -azobis(cyclohexanecarbonitrile) (VAZO® catalyst 88), azobis(isobutyronitrile) (AIBN), 4,4'-azobis(4-cyanopentanoic acid), potassium persulfate, ammonium persulfate, and benzoyl peroxide.
The coatable composition is prepared by mixing the foregoing components in a solvent. Those of ordinary skill in the art will appreciate that the exact order of mixing and the relative proportions of the foregoing components and solvent are not limiting. The exact amounts of the various components may be varied within fairly broad limits.
Second compatible component may be provided in the coatable composition at a concentration less than 15%, in some embodiments less than 10%, in some embodiments less that 5% and in some embodiments less that 2%. Polymerizable compound may be present at a concentration less than 15%, in some embodiments less than 10% and in some embodiments less that 5%. Photoinitiator may be present in the coatable composition at a concentration of less than 6%, in some embodiments less than 2% and in some
embodiments less than 1%. In some embodiments, the solvent is an aqueous solvent with a compatible organic component. In some embodiments, the solvent can comprise a water/alcohol mixture wherein the volume percentage of alcohol is between about 40% and 90%>, between about 55% and 80%>, between about 65%> and 75%, and in some embodiments the volume percentage of alcohol is about 70%.
Coated Porous Material
In some embodiments of the invention, articles are provided in the form of coated porous materials suitable for use in filtration applications. The coated porous materials are made according to the process(es) described herein so that finished materials includes a porous substrate, as described herein, with a first major surface and a second major surface and a plurality of pores extending through the substrate generally from the first major surface to the second major surface. Each pore includes an inner pore wall which defines the internal dimension or diameter of the pore. A hydrophilic coating covers at least a portion of the surfaces of the porous substrate, and the coating is affixed or adhered to at least such surfaces of the substrate, including the inner pore walls. As mentioned, the
hydrophilic coating comprises second compatible component and at least one crosslinked polymer in a single layer. It is believed that the second compatible component remains substantially unreacted with the crosslinked polymer, and the hydrophilic coating is neither grafted nor covalently bonded to the surfaces of the porous substrate. The hydrophilic coating covers the surfaces of the porous substrate without fully occupying the void volume within the pores of the substrate. Liquid passing through the pores of the coated porous material will flow in proximity to the hydrophilic coating and generally not between the coating and the surfaces of the substrate.
Moreover, the hydrophilic coating is "affixed or adhered to" the surfaces of the porous substrate in the sense that the hydrophilic coating is substantially retained within the pores of the substrate when water or an aqueous solution is passed through the coated porous material. In embodiments of the described materials, less than one percent by weight of the hydrophilic coating is lost when the coated porous material is submerged in water for up to 30 days.
In one embodiment, the coated porous material comprises a porous substrate in the form of a TIPS membrane such as a membrane formed from polypropylene or from polyvinylidene fluoride, for example. The hydrophilic coating is comprised of highly crosslinked polymer derived from polyethylene glycol di(meth)acrylate and VAZPIA reactive photoinitiator provided in sufficient amount to serve as a crosslinker and second compatible component.
In various embodiments, the coated porous materials exhibit a desirable flux or water flow rate as is described in the Test Methods employed for the various Examples herein. This test measures the time for a predetermined volume of water to pass through a substrate, and the water flow rate (flux) is calculated using the time, vacuum pressure, and area of the substrate and is expressed in L/(m2.h.psi). For the Coated porous materials of the present invention, the flux (water flow rate) is typically similar to the flux for the uncoated porous substrate, thus indicating that the hydrophilic coating produces little change in pore size as compared with the uncoated porous substrate.
Additionally, embodiments of the coated porous materials exhibit a high surface energy (e.g., higher than the surface energy of the uncoated porous substrate). In some embodiments, the coated porous material exhibits a surface energy of 50 dynes/cm or greater, in some embodiments the coated porous material exhibits a surface energy of
65 dynes/cm or greater, in other embodiments the coated porous material exhibits a surface energy of 80 dynes/cm or greater, and in still other embodiments the coated porous material exhibits a surface energy of 85 dynes/cm or greater. Preparation of Coated Porous Materials
In the preparation of coated porous materials according to the invention, coatable composition, prepared as described herein, is applied to a porous substrate. A
polymerization reaction in the coatable composition facilitates the formation of the hydrophilic coating on the surfaces of the substrate. Embodiments of such a process are now described.
In some embodiments, to achieve a crosslinked hydrophilic coating as described herein, the coatable composition may be prepared and applied without first
prepolymerizing or oligomerizing the polymerizable compound prior to applying coatable composition to a porous substrate. In other word, the coatable composition is prepared with an unreacted polymerizable compound that consists of or comprises monomer, and the composition is applied to the porous substrate without creating conditions under which the monomer would normally react to oligomerize. In some embodiments, the coatable composition is prepared by simply mixing one or more monomer(s), optionally one or more crosslinking agents, optionally one or more initiators, second compatible component in one or more suitable solvents. Suitable examples of the foregoing materials are given above.
Components of the coatable composition are blended so that the composition is substantially homogeneous, but may be slightly heterogeneous. The coatable composition is then applied to a suitable porous substrate, typically by soaking the substrate in the coatable composition for a sufficient amount of time to allow the composition to enter and substantially fill the pores of the substrate. Excess coatable composition may be removed from the outer surfaces of the porous substrate by known lamination techniques or the like.
Following removal of solvent, the coated porous substrate is rewetted with a suitable rewetting agent such as water or a suitable aqueous solution including, for example, an aqueous salt (e.g., sodium chloride or other inorganic salt) solution or another aqueous solution of known inorganic or organic materials or the like. In some
embodiments, a suitable salt solution comprises an aqueous solution of sodium chloride at
a concentration less than about 30% and in some embodiments at a concentration of about 20%. Rewetting agent serves several functions such as, for example, elimination of the inhibiting effects of oxygen during UV curing. Additionally, the rewetting agent reduces the impact of heat generated by UV sources, particularly from medium pressure mercury lamps. Also, the rewetting agent helps to organize polar groups in the monomer molecules of the coatable composition so that, once cured, the hydrophilic coating comprises a high density of polar groups, which contribute to a high surface energy on the finished coated porous material.
In some embodiments, polymerizable compound in the coatable composition comprises one or more polar monomer(s) selected to have limited solubility in the rewetting agent to prevent the loss of monomer into the rewetting agent along with a reduction of the initial monomer concentration. In general, the polar monomer(s) is(are) selected to provide a highly crosslinked polymer possessing certain physical properties such as heat stability, resistance to biomolecule adsorption, resistance to strong alkaline solutions, and having low levels of extractable matter, for example.
Following rewetting of the dried substrate, the polymerization reaction is initiated and allowed to run to completion to form the hydrophilic coating. As already noted, polymerization may be initiated by, for example, thermal activation or by UV irradiation. Thermal activation is generally less preferred because of the tendency of the
polymerizable compound(s) (e.g., monomer) to be soluble in the rewetting agent at elevated temperatures. Moreover, initiation of the polymerization reaction by UV irradiation in the presence of a photoinitiator tends to be faster than a reaction initiated by thermal activation. When initiated by UV radiation, the porous substrate containing a coatable composition of monomer (or oligomer), crosslinking agent and photo initiator is subjected to UV irradiation at wavelengths of from about 200 nm to about 600 nm, for a period of a few seconds to a few hours. In some embodiments, UV irradiation can be broad band or narrow band and the intensity of the UV source may be varied within known parameters, typically with peak power densities ranging from 5 to 600 mW/cm2 or higher.
In certain embodiments, the porous substrate is provided as a continuous web of material which, following saturation by the coatable composition, may undergo the polymerization reaction in a continuous process in which the web is exposed to UV
radiation as it passes underneath or in proximity to a UV source at a controlled speed. In some embodiments, the porous substrate and coatable composition therein are exposed to UV radiation along both major surfaces, either sequentially or simultaneously. Sequential exposure to a UV source typically requires a first exposure to a UV source that has been positioned on one side of the web or substrate. Thereafter, the web is turned over and the second side of the substrate is exposed to substantially the same dose of UV radiation to essentially completely polymerize the polymerizable compound in the pores of the substrate.
Alternatively, multiple UV sources may be simultaneously directed to irradiate opposite sides of the continuous web. In any of the foregoing embodiments, the continuous web may be supported on a carrier. In some embodiments, the web carrier may be selected to permit transmittance of the UV radiation therethrough so that the radiation is not blocked from initiating the polymerization reaction within the pores of the substrate. In some embodiments, biaxially oriented polypropylene (BOPP) film is an example of a material suitable for supporting the substrate during UV irradiation and polymerization. In some embodiments, the saturated porous substrate may be positioned between (e.g., "sandwiched") layers of BOPP during irradiation. The layers of film on either side of the porous substrate served to support the substrate, allow for the transmittance of UV radiation therethrough and prevent the loss of rewetting solution in and maintain a level of moisture in the substrate during processing.
Following the polymerization reaction, the coated porous material may be washed to remove remaining salt solution, unreacted materials, residual solvent, and the like. The coated porous material may be dried by evaporation of the remaining liquid (e.g., wash water) by evaporation at room temperature or at an elevated temperature.
In specific embodiments, the foregoing process additionally involves an optional prepolymerization or oligomerization step prior to applying the coatable composition to the porous substrate. In such embodiments, the prepolymerization step may be achieved by thermal initiation, in the presence of a thermal initiator, of the polymerization reaction before the coatable composition is applied to a porous substrate. The degree of polymerization achieved in this step is controlled in a known manner by, for example, using a limiting amount of initiator, control of the reaction time and temperature (e.g., by quenching at a predetermined time after initiation) and the like. Following
prepolymerization, the coatable composition may be applied to the porous substrate and further processed as described herein. Suitable thermal initiators may be selected from known materials including those previously mentioned.
In still another optional embodiment, the coatable composition is formulated with UV initiator and applied to the porous substrate. Prior to removing solvent from the coatable composition as described herein, the composition is subjected to a first or initial exposure of UV radiation to initiate a prepolymerization step. In such embodiments, the prepolymerization reaction is controlled to permit the reaction of monomer and to provide oligomers but to avoid running the reaction to completion (e.g., full polymerization) at this stage of the manufacturing process. The degree of pre -polymerization or oligomerization may be controlled by, for example, the use of a limited amount of a first initiator as is further explained herein, by control of the UV exposure (e.g., control of exposure time) or the like. In embodiments utilizing UV radiation to initiate a prepolymerization or oligomerization reaction, the initiator may be selected for its sensitivity to a selected first UV wavelength that is used only during the prepolymerization step, and wherein the first UV wavelength is different than the UV wavelength that is used to fully polymerize the polymerizable compound. In such embodiments, the coatable composition can be formulated to include more than one UV initiator - i.e., a first initiator to sensitive to a first UV wavelength effective to initiate the oligomerization reaction and a second initiator sensitive to a second UV wavelength that is effective to initiate the polymerization reaction previously described. Following the oligomerization step, the remaining process is as previously described - i.e., following initial UV exposure, solvent is removed from the coatable composition and a rewetting solution (e.g., aqueous NaCl) is applied to the substrate and the rewetted substrate is again UV irradiated to complete the polymerization reaction and provide a hydrophilic coating. As already mentioned, the resulting coated porous material is then washed and dried.
Use of the Coated Porous Material
The various embodiments of the invention include articles (e.g., coated porous materials) and processes (e.g., for the manufacture of coated porous materials). The coated porous materials of the invention may be used in any of a variety of filtration applications including ultrafiltration, wherein the hydrophilic coating can be either
charged or neutral, and in microfiltration for use in, for example, health care, food & beverage, and/or industrial markets. Specific applications can include fuel cell and battery separator applications, for example.
The coated porous materials of the invention may be used to carry out separations in aqueous media as well as in non-aqueous fluids. The coated porous materials may be provided as membranes, films and/or as components in any of a variety of articles made for filtration applications. The coated porous materials of the invention are capable of being flexed, folded, or pleated without breaking or crumbling to the touch, making them suitable for use in a filter cartridge or in other filtration devices requiring high surface area materials. Moreover, coated porous materials comprised of membrane materials as the porous substrate can provide low fouling propensity and a high filtration efficiency.
In some embodiments, the coated porous materials described herein may be further modified by depositing any of a variety of compositions thereon using known coating or deposition techniques. For example, the coated porous materials may be metal coated using vapor deposition or sputtering techniques, or the coated porous materials may be coated with adhesive, aqueous or solvent based coating compositions or dyes, for example.
In some embodiments, unique articles are provided by laminating coated porous materials to another structure or material, such as other sheet materials (e.g., fabric layers, woven, nonwoven, knitted, or mesh fabrics), polymeric film layers, metal foil layers, foam layers, or any combination thereof to provide composite structures. Lamination can be accomplished using conventional techniques that include adhesive bonding, spot welding, or by other techniques that do not destroy or otherwise interfere with the desired porosity of the coated porous material. Multilayered filtration articles may additionally be made from (i) one or more layers of coated porous materials based on a porous substrate in the form of a membrane as described herein, and (ii) one or more layers of coated porous materials based on a porous substrate in the form of a nonwoven, for example. In some embodiments, other materials may also be included in a multilayered filtration article so that some of the layers are coated porous materials, as described herein, and the other layers comprise membrane(s) or fibrous filtration constructions other than those described herein.
Additional aspects of the invention and embodiments thereof are further illustrated in the following non-limiting Examples.
EXAMPLES
TEST METHODS
Membrane surface energy
Dyne solutions from two different sets (30-70 dynes/cm from Jemmco, LLC, Mequon WI; 73-87 dyne/cm solutions formulated according to Handbook of Chemistry and Physics, 71st edition, CRC press) were used. All solutions were dropped onto a substrate (e.g., a membrane) using a plastic pipette. The drop volume was about 0.5ml. The time for a dyne solution to penetrate through the membrane was recorded by a stopwatch. A light trans-illuminator was used for easy detection of the dyne solution penetration. The membrane surface energy was recorded as the surface tension of the highest dyne solution which penetrated through the membrane in less than one second. Three test replicates were used and averaged for each measurement.
Flux (Water flow rate)
A 47 mm disk of a test substrate was mounted in a Gelman magnetic holder (Gelman Sciences, Inc., Ann Arbor, Mich.). The active substrate diameter in the holder was 34 mm. A vacuum pump running at approximately 60 cm (23.5 inches) of mercury Hg) was applied to draw water through the substrate. The time for 100 ml water to pass through the substrate was recorded with a stopwatch. The water flow rate (flux) was calculated using the time, vacuum pressure, and area of the substrate and expressed in L/(m2.h.psi). Two to three test replicates were used and averaged for each measurement.
Bubble point pore size
The bubble point pore sizes of the substrates were measured according to ASTM-F316-03. A substrate was pre-wetted with isopropanol and then mounted onto a test holder. Pressurized nitrogen gas was gradually applied to one side of the substrate until the gas flow detected at the other side reached 100%. The pressure at 100% gas flow through the substrate was recorded and used to calculate the bubble point pore size. Two to three replicates were used and averaged for each measurement.
Thermal resistance testing
The sample substrates were first completely wetted by immersing in them in deionized water and then placed between a sandwich of two paper towel sheets. The test
sandwich was placed in a Thelco Lab Oven (Thermo Electron Corporation, Marietta, Ohio) for 30 min with a set point temperature of 136°C. The substrate was then tested for water wettability and surface energy according to the above test methods. Example 1 (prophetic)
A 5.0 wt% stock solution is made by dissolving one or more of the second compatible components listed herein in an ethanol (AAPER Alcohol and Chemical Co. Shelbyville, KY)/water solvent mixture (70.0 vol% ethanol) in a water bath at a temperature within the range of 70-80°C. A coatable composition is made from the above stock solution by adding 4.0 wt% polyethylene glycol diacrylate (SR610, Sartomer, Warrington, PA) and 1.0 wt% reactive photoinitiator VAZPIA ( 2-[4-(2-hydroxy-2- methylpropanoyl)phenoxy]ethyl-2-methyl-2-N-propenoylamino propanoate, (disclosed in U.S. Pat. No. 5,506,279) in ethanol/water mixture solvent (70.0 vol% ethanol). The final concentration of the copolymer in the coatable composition is 1.0 wt%.
A microporous polypropylene membrane (F100, 3M Purification Inc. Meriden,
CT) is saturated with the coatable composition by placing samples of the membrane ranging from 516 cm2 to 1426cm2 in a heavy weight polyethylene (PE) bag along with 10 to 100 ml of coatable composition and letting the composition soak into the membrane for a minute or less. Excess coatable composition on the surface of the membrane is then removed with by blotting on a paper towel after the membrane is removed from the PE bag. The membrane is allowed to dry at room temperature for 10-12 hours. The dried membrane is placed into another PE bag and 10 to 100 ml of rewetting solution, - i.e., 20.0 wt% NaCl aqueous solution was added into the bag. The membrane is instantly wetted with the salt solution and is then removed from the bag. The coatable composition is cured by passing the membrane on a conveying belt through a nitrogen inert Fusion UV system equipped with an H-bulb with an aluminum reflector. The speed of the belt was 6.1 meters/min (20 feet/minute). The membrane is then turned over to expose the other side to the UV source and passed through the UV system again at 6.1 meters/min
(20 feet/minute) to provide a coated porous material.
The coated porous material is then washed in de -ionized water and dried at 90°C
(194°F) in a speed dryer (Emerson Speed Dryer Model 130, Emerson Apparatus
Company, Gorham, ME) for about one hour.
The coated porous material is tested according to the above test methods. The material will exhibit a surface energy greater than about 50 dynes/cm, a bubble point pore size of about 0.30 μιη or greater and water flow rate of about 500 L/m2. h.psi, or greater. The uncoated base membrane is also tested, exhibiting a bubble point pore size and water flow rate that are comparable to those for the coated porous material, thus indicating that the cured membrane will maintain its pore microstructure.
Various embodiments of the invention have been described in detail. Those of ordinary skill in the art will appreciated that changes, both foreseeable and unforeseen, may be made to the described embodiments without departing from the true spirit and scope of the invention.
Claims
1. A process for the preparation of a coated porous material, the process comprising: a) providing a porous substrate comprising a plurality of pores extending through the substrate from a first major surface to a second major surface, each pore comprising an inner pore wall defining the internal dimension of the pore;
b) applying a coatable composition to at least a portion of the inner pore walls of the porous substrate, the coatable composition comprising a first component in the form of at least one polymerizable compound, a second compatible component and solvent; c) removing the solvent from the coatable composition;
d) saturating the porous substrate and the coatable composition with a rewetting solution; and
e) polymerizing the polymerizable compound to form a hydrophilic coating on the pore walls and to provide the coated porous material, the hydrophilic coating comprising both the second compatible component and a crosslinked polymer in a single layer.
2. The process of claim 1 further comprising partially polymerizing the
polymerizable compound in the coatable composition either before or after the step (b) of applying the coatable composition to at least a portion of the inner pore walls.
3. The process of claim 2 wherein the step of partially polymerizing the
polymerizable compound comprises thermally initiating a polymerization reaction in the coatable composition to partially polymerize the polymerizable compound before the step (b) of applying the coatable composition to at least a portion of the inner pore walls.
4. The process of claim 2 wherein the step of partially polymerizing the
polymerizable compound comprises photo-initiating a polymerization reaction in the coatable composition to partially polymerize the polymerizable compound after the step (b) of applying the coatable composition to at least a portion of the inner pore walls.
5. The process of claim 1, further comprising preparing the coatable composition prior to coating the pore walls therewith, the coatable composition prepared by combining the at least one polymerizable compound with the second compatible component in a solvent.
6. The process of claim 5 wherein the at least one polymerizable compound comprises monomer selected from polyethylene glycol diacrylate, polyethylene glycol dimethacrylate and combinations thereof.
7. The process of claim 5 wherein the at least one monomer is initially of a molecular weight greater than about 400.
8. The process of claim 5 wherein the at least one monomer is initially of a molecular weight greater than about 600.
9. The process of claim 5 wherein the solvent is a mixture of water and a compatible organic solvent.
10. The process of 9 wherein the compatible organic solvent is ethanol.
11. The process of 1 wherein the second compatible component is a material selected from surfactant, polymer, polysaccharide and combinations of two or more of the foregoing.
12. The process of 11 wherein the second compatible component is a surfactant selected from sorbitan laurate, triethanolamine dodecylbenze sulfonate, nonionic alkylphenoxy poly(ethyleneoxy) ethanol, propylene oxide - ethylene oxide copolymer and combinations of two or more of the foregoing.
13. The process of 11 wherein the second compatible component is polysaccharide selected from methyl cellulose, ethyl cellulose, hydroxypropyl cellulose, hydroxyethyl cellulose, hydroxypropyl methyl cellulose, hydroxybutylmethyl cellulose, hydroxyethyl methyl cellulose, carboxymeth cellulose, dextran, hydroxyethyl starch and combinations of two or more of the foregoing.
14. The process of 11 wherein the second compatible component is a polymer selected from polyvinyl alcohol, polyvinylpyrrolidone, coplymers and combinations thereof.
15. The process of claim 1 wherein the coatable composition further comprises at least one crosslinking agent and photoinitiator and wherein removing the solvent from the coatable composition and the porous substrate is accomplished by evaporating the solvent.
16. The process of claim 15 wherein the rewetting solution comprises a solution of sodium chloride, and step (e) of polymerizing the polymerizable compound comprises photo-polymerizing the at least one polymerizable compound using ultraviolet radiation.
17. The process of claim 15 wherein the photoinitiator comprises a reactive material comprising 2-[4-(2-hydroxy-2-methylpropanoyl)phenoxy]ethyl-2-methyl-2-N- propenoylamino propanoate.
18. The process of claim 1 further comprising: (f) washing the coated porous material with water and (g) thermally drying the coated porous material.
19. The process of claim 1 wherein the porous substrate is a membrane.
20. The process of claim 19 wherein the membrane comprises material selected from the group consisting of poly(ether)sulfone, polyolefms, polyvinylidene fluoride, polyamide, cellulose ester and combinations of two or more of the foregoing.
21. The process of claim 1 wherein the porous substrate comprises fibrous material selected from the group consisting of nonwoven material, woven material and knitted material.
22. The process of claim 1 wherein the step (e) of polymerizing the polymerizable compound results in the hydrophilic coating comprising both the crosslinked polymer and the second compatible component in an interpenetrating polymer network.
23. A coated porous material made according to the process of claim 1.
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US35015410P | 2010-06-01 | 2010-06-01 | |
US61/350,154 | 2010-06-01 | ||
US35144710P | 2010-06-04 | 2010-06-04 | |
US61/351,447 | 2010-06-04 |
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WO2011153085A2 true WO2011153085A2 (en) | 2011-12-08 |
WO2011153085A3 WO2011153085A3 (en) | 2012-04-05 |
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PCT/US2011/038283 WO2011153085A2 (en) | 2010-06-01 | 2011-05-27 | Process for making coated porous materials |
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