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WO2002018036A1 - Substrat poreux ou non poreux enduit d'une composition polymere immobilisee avec groupes sulfonyle et groupes fonctionnels hydrophiles et procede de fabrication - Google Patents

Substrat poreux ou non poreux enduit d'une composition polymere immobilisee avec groupes sulfonyle et groupes fonctionnels hydrophiles et procede de fabrication Download PDF

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Publication number
WO2002018036A1
WO2002018036A1 PCT/US2001/026720 US0126720W WO0218036A1 WO 2002018036 A1 WO2002018036 A1 WO 2002018036A1 US 0126720 W US0126720 W US 0126720W WO 0218036 A1 WO0218036 A1 WO 0218036A1
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Prior art keywords
porous
substituted
unsubstituted
article
immobilized
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English (en)
Inventor
Wilson Moya
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Entegris Inc
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Mykrolis Corp
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Priority to JP2002523004A priority Critical patent/JP2004507345A/ja
Priority to US10/344,058 priority patent/US7094469B2/en
Publication of WO2002018036A1 publication Critical patent/WO2002018036A1/fr
Anticipated expiration legal-status Critical
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    • 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
    • B01D67/0093—Chemical modification
    • B01D67/00931—Chemical modification by introduction of specific groups after membrane formation, e.g. by grafting
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
    • C08J5/20—Manufacture of shaped structures of ion-exchange resins
    • C08J5/22—Films, membranes or diaphragms
    • C08J5/2206—Films, membranes or diaphragms based on organic and/or inorganic macromolecular compounds
    • C08J5/2218—Synthetic macromolecular compounds
    • C08J5/2231—Synthetic macromolecular compounds based on macromolecular compounds obtained by reactions involving unsaturated carbon-to-carbon bonds
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
    • C08J5/20—Manufacture of shaped structures of ion-exchange resins
    • C08J5/22—Films, membranes or diaphragms
    • C08J5/2206—Films, membranes or diaphragms based on organic and/or inorganic macromolecular compounds
    • C08J5/2275—Heterogeneous membranes
    • C08J5/2281—Heterogeneous membranes fluorine containing heterogeneous membranes
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/10—Fuel cells with solid electrolytes
    • H01M8/1016—Fuel cells with solid electrolytes characterised by the electrolyte material
    • H01M8/1018—Polymeric electrolyte materials
    • H01M8/1058—Polymeric electrolyte materials characterised by a porous support having no ion-conducting properties
    • H01M8/106—Polymeric electrolyte materials characterised by a porous support having no ion-conducting properties characterised by the chemical composition of the porous support
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/10—Fuel cells with solid electrolytes
    • H01M8/1016—Fuel cells with solid electrolytes characterised by the electrolyte material
    • H01M8/1018—Polymeric electrolyte materials
    • H01M8/1058—Polymeric electrolyte materials characterised by a porous support having no ion-conducting properties
    • H01M8/1062—Polymeric electrolyte materials characterised by a porous support having no ion-conducting properties characterised by the physical properties of the porous support, e.g. its porosity or thickness
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/10—Fuel cells with solid electrolytes
    • H01M8/1016—Fuel cells with solid electrolytes characterised by the electrolyte material
    • H01M8/1018—Polymeric electrolyte materials
    • H01M8/1069—Polymeric electrolyte materials characterised by the manufacturing processes
    • H01M8/1086—After-treatment of the membrane other than by polymerisation
    • H01M8/1088—Chemical modification, e.g. sulfonation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2323/00—Details relating to membrane preparation
    • B01D2323/30—Cross-linking
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2323/00—Details relating to membrane preparation
    • B01D2323/38—Graft polymerization
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2327/00—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers
    • C08J2327/02—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers not modified by chemical after-treatment
    • C08J2327/12—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers not modified by chemical after-treatment containing fluorine atoms
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30—Hydrogen technology
    • Y02E60/50—Fuel cells
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50—Manufacturing or production processes characterised by the final manufactured product

Definitions

  • This invention relates to a porous or non-porous substrate comprising a fluorine- containing polymer including a fluorocarbon polymer substrate having a surface with improved hydrophilic characteristics, comprising an immobilized fluorocarbon polymeric composition having hydrophilic functional groups, comprising sulfonyl groups and to a process for forming the substrate having the improved hydrophilic characteristics.
  • this invention relates to a porous or non-porous substrate comprising a fluorine- containing polymer including a fluorocarbon substrate having a surface with improved hydrophilic characteristics, comprising an immobilized fluorocarbon polymeric composition having hydrophilic functional groups comprising sulfonyl groups wherein the immobilized fluorocarbon polymeric composition is immobilized in situ on the porous or nonporous substrate.
  • perfluorocarbon as used herein is meant a polymer comprising one or more perfluorocarbon monomers including homopolymers, copolymers, terpolymers, polymer blends or the like.
  • perfluorocarbons include polytetrafluoroethylene, fluorinated ethylene-propylene copolymer (FEP), polyvinylidene fluoride (PVDF) and perfluoroalkoxy polymer (PFA).
  • FEP fluorinated ethylene-propylene copolymer
  • PVDF polyvinylidene fluoride
  • PFA perfluoroalkoxy polymer
  • Porous membrane filters are utilized in a wide variety of environments to separate materials within a fluid stream.
  • Membranes are formed from a solid polymeric matrix and have highly precisely controlled and measurable porosity, pore size and thickness.
  • the membrane filters generally are incorporated into a device such as a cartridge, which in turn, is adapted to be inserted within a fluid stream to effect removal of particles, microorganisms or a solute from liquids and gases.
  • membrane filters must be resistant to the fluid being filtered so that they maintains their strength, porosity, chemical integrity and cleanliness, h addition, membrane filters must remain wetted with the process fluid in order to maintain filtration efficiency.
  • Perfluorocarbon-based membrane filters made from fluorine-containing polymers such as polytetrafluoroethylene, FEP or PFA are commonly utilized in these applications. Fluorine-containing polymers are well known for their chemical inertness, or excellent resistance to chemical attack.
  • Fluorine-containing polymers are well known for their chemical inertness, or excellent resistance to chemical attack.
  • One disadvantage of fluorine-containing polymers is that they are hydrophobic and therefore membranes made from such polymers are difficult to wet or to remain wet with aqueous fluids or other fluids which have a tendency to outgas.
  • membrane filters are used extensively to purify various outgassing process fluids to prevent contaminants from causing circuit failures.
  • a membrane filter having improved hydrophilic properties, which does not dewet during filtration in order to retain filtration efficiency.
  • Dewetting of a fluorine-containing polymeric surface also is a problem with a non- porous surface such as a hollow tube wherein the formation of gases therein restricts or prevents the controlled flow of an outgassing liquid therein.
  • the membrane having its surface modified should retain sufficient porosity to permit its use as a filtration member. Accordingly the amount of surface modifying composition applied to the membrane surface must be controlled in order to retain porosity of the modified membrane, hi contrast, when modifying a porous membrane for non-filtration applications such as in ion-exchange applications including electrodialysis, electrodeionization, fuel cells or the like, complete blockage of the membrane pores with the surface modifying composition is not a problem.
  • PCT application WO 99/38897 discloses cross -linked sulfonated polymers and the process for preparing them.
  • U.S. Patent 4,470,859 to Benezra et al discloses a process for modifying the surfaces of microporous substrates formed of a fluorocarbon such as polytetrafluoroethylene, with a coating of an uncross-linked perfluorocarbon copolymer composition including hydrophilic functional groups copolymer from a solution of the pefluorocarbon copolymer composition to render the surface of the membrane more water wettable.
  • the perfluorocarbon copolymer composition is dissolved in a nonaqueous solvent at elevated temperature.
  • the membrane then is immersed into the solution which, in turn, is placed into a vacuum chamber.
  • the pressure within the chamber then is reduced such as to approximately 150 millimeters of mercury (absolute) to remove air from within the filter. Thereafter, the pressure within the chamber is quickly returned to atmospheric pressure.
  • This coating process is repeated to ensure, what is described by Benezra et al, complete solution penetration into the pores of the membrane.
  • the membrane surfaces and the interior walls defining the interstices within the membrane are coated with the perfluorocarbon copolymer composition.
  • the solvent is removed by evaporation using heat and vacuum, or the solvated perfluorocarbon copolymer composition is precipitated with a substance in which the perfluorocarbon copolymer composition is effectively insoluble.
  • the solvents utilized to form the solution include halocarbon oil, perfluorooctanoic acid, decafluorobiphenyl, N-butylacetamide, and N, N-dimetliylacetamide.
  • Benezra et al teaches avoiding the use of a fluid containing a solvent for the modifying perfluorocarbon polymer composition on the membrane surface. Benezra et al. also disclose that alcohol solutions for the perfluorocarbon polymer composition should be avoided.
  • U.S. Patent 4,902,308 to Mallouk et al also describes a process for modifying the surface of a porous, expanded polytetrafluoroethylene membrane with a perfluorocation exchange polymer from an organic solution of the polymer.
  • Mallouk et al also teaches that contact of the surface modified membrane with fluids containing a solvent for the polymer also should be avoided.
  • U.S. Patents 4,259,226 and 4,327,010 disclose modifying a porous membrane surface with a fluorinated polymer having carboxylic acid salt groups. No process steps are disclosed for controlling extractables from the membrane or for controlling the extent of binding of the modifying composition to the membrane surface.
  • U.S. Patents 5,183,545 and 5,094,895 disclose a process for making a multilayer, composite, porous diaphragm from a porous, multilayer, expanded polytetrafluoroethylene substrate having its surface modified with an uncross-linked perfluoro ion exchange polymer composition.
  • the modifying polymer composition can contain a surfactant and may contain excess modifying composition, both of which are sources of undesirable extractables.
  • U.S. Patent 5,874,616 to Howells et al discloses a process for making linear polymeric bis(fluoroalkylenesulfonyl)imides by reacting a difunctional fluoroalkylene sulfonamide compound with a difunctional fluoroalkylene sulfonyl halide compound. Since this process relies on the use of low molecular weight reactants to produce the polymer, it is difficult to control the molecular weight distribution of the final linear polymeric composition and therefore it is undesirable. hi addition, the linear polymeric bis(fluoroalkylenesulfonyl)imides are not cross -linked.
  • U. S. Patent 5,463,005 to Desmarteau discloses a process for forming a copolymer of tetrafluoroethylene (TFE) and a unsaturated monomer wherein the monomer is derived from a sulfonimide-containing reagent. Since TFE is a toxic reagent, its use is undesirable. In addition, since this process relies on the use of low molecular weight unsaturated monomers, it is difficult to control the molecular weight distribution of the final polymeric composition.
  • TFE tetrafluoroethylene
  • PCT/CA99/00083 discloses polymers formed from fluorinated polymerizable difunctional monomers containing a sulfonyl group.
  • International Patent application PCT/CA99/38897 discloses a fluorinated cross -linked polymeric compositions containing sulfonyl groups.
  • a porous membrane formed from a fluorine-containing polymer having a surface with improved hydrophilic characteristics suitable for filtration applications Such a porous membrane would be chemically and thermally stable and have a surface sufficiently hydrophilic to enable filtration while avoiding dewetting.
  • Such a non-porous membrane would be chemically and thermally stable and would permit the transport of ionic species therethrough.
  • a surface modified article formed from a non-porous fluorine- containing polymeric substrate having its surface modified with a fluorocarbon polymeric composition having hydrophilic functional groups. Such a non-porous article would be useful for processing outgassing liquids while avoiding dewetting of the surface.
  • This invention provides a porous or non-porous membrane or article formed from a fluorine-containing polymer substrate having its surface modified with an immobilized, such as by crosslinking and/or grafting, fluorocarbon, preferably perfluorinated, polymeric composition having hydrophilic functional groups to provide a surface with improved hydrophilic characteristics as compared to the unmodified substrate.
  • improved hydrophilic characteristics is meant that the product having the modified surface is non-dewetting after being wet with an aqueous fluid or is directly wetted by an aqueous fluid.
  • the fluorine-containing polymer substrate can be a porous membrane or can be a non-porous article in any desired configuration such as a fiber, a woven or non-woven fabric formed from fibers, a mesh, a tube, a flat sheet, a corrugated sheet, a conduit, beads, rods or the like.
  • this invention provides a surface comprising an immobilized perfluorocarbon polymeric composition, which is immobilized such as by crosslinking and/or grafting with at least one monomer having hydrophilic functional groups.
  • immobilized perfluorocarbon polymeric compositions are formed from chemically stable monomers in that they are fluorinated and are immobilized with fluorinated linking moieties, which are stable against degradation by virtue of contact with highly reactive reagents such as liquid compositions containing a base such as ammonium hydroxide, an oxidizer such as hydrogen peroxide or ozone and water, having a pH greater than about 9 such as special cleaning (SC) solutions, for example SCI used during the manufacture of electronic components, h contrast, cross-linking moieties containing non-fluorinated organic groups become degraded upon contact with these reagents and these chemical crosslinks are destroyed so that the cross -linked polymer loses its original degree of cross- linking.
  • SC special cleaning
  • the surface-modifying composition comprising a cross-linked and/or grafted fluorocarbon, such as perfluorocarbon, polymeric composition having hydrophilic functional groups derived from at least one monomer having the formula: [T-SO 2 Y-SO 2 T'] " M + in which
  • -T and T' are identical or different and comprise an organic radical bearing at least one active polymerization function such as an unsaturation or a ring that can be opened;
  • -M comprises an inorganic or organic cation.
  • -Y comprises N or CQ in which Q comprises H, CN, F, SO 2 R , substituted or unsubstituted Ci-20 alkyl, substituted or unsubstituted Ci-20 aryl, substituted or un- substituted Ci-20 alkylene, in which the substituent comprises one or more halogens, and in which the chain comprises one or more F, SO2R, aza, oxa, thia or dioxathia substituents; and -R comprises F, substituted or unsubstituted Ci-20 alkyl, in which the substituted or unsubstituted Ci-20 aryl, substituted or unsubstituted Ci-20 alkylene, in which the substituent comprises one or more halogens.
  • M comprises a proton, the cation of a metal such as an alkali metal, an alkaline-earth metal, a rare-earth or a transition metal; an organometallic cation such as a metallocene, an arenemetallocene, an alkylsilyl, an alkylgermanyl or an alkyltin; or an organic cation optionally substituted by one or more organic radicals.
  • a metal such as an alkali metal, an alkaline-earth metal, a rare-earth or a transition metal
  • an organometallic cation such as a metallocene, an arenemetallocene, an alkylsilyl, an alkylgermanyl or an alkyltin
  • organic cation optionally substituted by one or more organic radicals.
  • preferential organic cations include an R" O (onium) group, NR" (ammonium) ⁇ R"C (NHR")2 + (amidinium), C(NHR")3+ (guanidinium), C 5 R"N + (pyridinium) C 3 R"N 2 + (imidazalium), C 2 R"N3 + (triazolium), C 3 R"N2 (imidazolinium), SR" + (sulfonium), PR” + (phosphonium), IR" + (iodonium), (C 6 R")3C + (carbonium), in which R" comprises:
  • alkyl alkenyl, oxaalkyl, oxaalkenyl, azaalkyl, azaalkenyl, thiaalkyl, thiaalkenyl, dialkylazo, silaalkyl radicals, optionally hydrolyzable; silaalkenyl radicals, optionally hydrolyzable; said radicals able to be linear, branched, or cyclic and comprising 1 to 18 carbon atoms;
  • radicals comprising several aromatic or heterocyclic nuclei; condensed or not, optionally containing one or more nitrogen, oxygen, sulfur or phosphorus atoms; and when an organic cation has at least two R" radicals different from H, these radicals can form together an aromatic or non-aromatic ring, optionally surrounding the center bearing the cationic charge.
  • the monomer or mixture of monomers can also be copolymerized/cross- linked/grafted with at least one monofunctional monomer, preferably of the formula (T- SO 3 )Tvf + or (T-SO2-Y-SO2W) " M + in which T, Y and M are defined above and W is a monovalent organic alkyl, alkenyl, aryl, alkylaryl, arylalkyl radical of 1-12 carbon atoms, optionally bearing one or more oxa, aza or thia substituents.
  • the surface modifying polymer is formed by coating the substrate with at least one of the above monomers under conditions to effect polymerization and cross-linking/grafting of the monomer.
  • the monomer When the monomer is polyfunctional, it can be cross-linked by adding a polymerization initiator followed by heat thereto or by exposing it to ionizing radiation such as electron beam radiation, ultraviolet light, plasma energy, Infrared radiation, gamma radiation, thermal energy or the like. When the monomer is monofunctional, a polyfunctional monomer is added to effect cross-linking.
  • the bulk properties of the porous or nonporous substrate include inertness to most organic solvents, inertness to many chemical reagents, good tensile strength and ductility.
  • the composite membranes of this invention can be used in filtration processes which are aqueous or which utilize organic solvents as in the pharmaceutical industry and with hquids containing concentrated acids as is commonly encountered in the electronic industries or in electrolysis applications such as in fuel cells.
  • fluorine-containing polymers useful for forming the porous or solid substrates for this invention include polytetrafluoroethylene (PTFE), perfluoroalkoxy polymers (PFA), fluorinated ethylene-propylene copolymers (FEP), ethylene-tefrafluoroethylene copolymers (ETFE), polyvinylidene fluoride (PVDF), polychlorotrifluoroethylene (PCTFE), polyvinyl fluoride (PVF), ethylene- chloiOtrifluoroethylene copolymer (ECTFE), or the like.
  • PTFE polytetrafluoroethylene
  • PFA perfluoroalkoxy polymers
  • FEP fluorinated ethylene-propylene copolymers
  • ETFE ethylene-tefrafluoroethylene copolymers
  • PVDF polyvinylidene fluoride
  • PCTFE polychlorotrifluoroethylene
  • PVF polyvinyl fluoride
  • fluorine-containing polymers useful for forming the substrates of this invention include functionalized polymers such as fluorocarbon polymers containing ionic groups, for example sulfonic acid groups, sulfonamide groups, sulfonimide groups, sulfonyl methide groups, sulfonyl methane groups, amide groups, imide groups or the like or the non-ionic precursors of such polymers.
  • functionalized polymers such as fluorocarbon polymers containing ionic groups, for example sulfonic acid groups, sulfonamide groups, sulfonimide groups, sulfonyl methide groups, sulfonyl methane groups, amide groups, imide groups or the like or the non-ionic precursors of such polymers.
  • Exemplary fluorocarbon, preferably perfluorinated, monomers from which the surface-modifying cross -linked fluorocarbon polymeric compositions having hydropl ilic functional groups include perfluoro-di(vinylethers) bearing highly dissociated imide of sulfone functions, such as di(sulfonylmethane), sulfonimide or tri(sulfonyhnethane), as a base for the formation of cross -linked surface-modifying polymeric composition.
  • a porous or non-porous substrate or article having the desired properties is directly applied in at least a portion of its surface area with a crosslinked polymerized derived from at least one monomer having hydrophilic functional groups.
  • the fluorocarbon polymeric composition is deposited on the surfaces of the porous or non-porous subsfrate by graft polymerization of the monomers and/or by deposition of the cross-linked polymer.
  • the monomer is multiunctional and cross-linking/grafting/ polymerization of the monomer(s) can be effected by adding a polymerization initiator thereto and exposing the resulting mixture to ionizing radiation or heat.
  • cross-linldng/grafting/polymerization can be effected by exposing the monomers to radiation energy such as ultraviolet light (UV), electron beam, heat, gamma radiationor the like.
  • the average pore size is between about 0.001 and 10 microns and more usually between about 0.01 and 5.0 microns.
  • the polymerizatiorjVgrafting/cross-lihLdng of the polymerizable monomers to the substrate by grafting and or deposition must be effected so that at least a portion of the surface of the substrate is modified with a cross-linked/grafted, or otherwise knmobilized polymer. Therefore, in a first step, the substrate is wet with a solvent composition that does not significantly swell or dissolve the substrate and which wets the surface of the subsfrate such as an organic solvent or a mixture of water and an organic solvent.
  • Suitable water-solvent compositions for this purpose include methanol/water, ethanol/water, acetone/water, tetrahydrofuran/water or the like.
  • the purpose of this wetting step is to assure that the monomer composition subsequently contacted with the substrate wets the surface of the substrate.
  • This preliminary wetting step can be eliminated when the reagent bath described below itself functions to wet the surface of the substrate. This can be effected when the reagent bath contains a high concentration of organic reactants, for example 15% by weight or higher.
  • the radical polymerizable monomer described below and a polymerization initiator in a solvent is contacted with the substrate and exposed to cross-linMng/graftin/polymerization conditions such as thermal energy at a temperature of at least about 30°C for a time of at least about 30 seconds, or UN light for at least about 1 second to effect polymerization of the monomer and deposition of the substrate with the cross-linked polymer.
  • cross-linMng/graftin/polymerization conditions such as thermal energy at a temperature of at least about 30°C for a time of at least about 30 seconds, or UN light for at least about 1 second to effect polymerization of the monomer and deposition of the substrate with the cross-linked polymer.
  • other sources of ionizing radiation can be used.
  • a polymerization initiator is not required although it can be present.
  • Examples of preferential monomers to form the cross -linked/grafted polymer include:
  • -X represents F, Cl, or CF 3 ;
  • -n varies between 0 and 10 inclusively
  • -E is absent, O, S or SO 2 ;
  • monomers useful as surface modifiers in the present invention can be .obtained by different processes.
  • monomers of the imide type are obtained in the following manner:
  • L is a labile group, for example, a halogen, a thiocyanate or an electrophilic group containing -at least one heteroatom, such as N-imidazolyl, N-triazolyl, or R-SO2O- in which
  • R is Ci-20 alkyl or Ci-20 alkylene, substituted or unsubstituted, in which the substituent is one or more halogens; and in which the chain includes one or more substituents chosen from among aza, oxa, thia, or dioxathia; and A is the element or the fraction of the * element corresponding to the cation M , and comprising hydrogen, a trialkylsilyl group, a trialkyltin or tertalkyl group, in which the al yl group comprises 1 to 6 carbon atoms.
  • tert-alkyl radical in definition A above is advantageous since it constitutes the precursor of an alkene being eliminated from the reaction medium and of a proton.
  • tert-butyl the following reaction is observed:
  • the trialkylsilyl group is advantageous when the labile group L is fluorine, given the high formation enthalpy of the Si-F bond.
  • A is a proton or a proton precursor, such as a tert-alkyl radical, it is advantageous to conduct the reaction in the presence of an obstructed base, for example a tertiary base.
  • bases examples include triethylamine, diisopropylamine, quinuclidinol, 1, 4-diazobicyclo[2.2.2]octane (DABCO), pyridine, alkylpyridines, dialkylaminopyridines, N- alkylimidazoles, imidazo[l,l-a]pyridine, amidines such as l,5-diazabicyclo[4.3.0]non-5-ene (DBN) or l,8-diazabicyclo[5.4.0]undec-7-ene (DBU), guanidines such as teframethylguanidine, 1, 3, 4, 7, 8-hexal ⁇ ydro-l-methyl-2H-pyrimido-[l, 2-a]pyrimidine (HPP).
  • DBN l,5-diazabicyclo[4.3.0]non-5-ene
  • DBU l,8-diazabicyclo[5.4.0]undec
  • the potassium salt of these monomers is insoluble or very poorly soluble in water, and can be precipitated therein from more soluble salts, i.e., H , Li or Na salts, and then purified by recrystallization. Recrystallization can be conducted in water, alone or in mixture with a miscible solvent, such as acetonitrile, dioxane, acetone or tetrahydrofuran (THF).
  • a miscible solvent such as acetonitrile, dioxane, acetone or tetrahydrofuran (THF).
  • DiaU ylammonium salts are usually insoluble in water and can therefore be extracted by means of various solvents, preferably halogenated solvents, such as dichloromethane, dichloroethane, trichloroethane, 1, 1, 1, 2-tetrafluoroethane, etc.
  • perfluorovinyl ether groups can be halogenated, in particular chlorinated or brominated, to give rise to a non- reactive perhalo ether.
  • the perfluorovinyl ether is possibly regenerated according to different processes well known to the person skilled in the art, for example, either by an electrochemical reaction, or with a reduction agent such as zinc powder, a bronze zinc- copper alloy, or tetrakis (dimethylamino)ethylene.
  • the following bifunctional monomers illustrate preferential monomers forming the surface modifiers cross-linked polymers of the invention.
  • M , Z, Q, X and Y are such as defined previously, arid n and m are identical or different and vary between 0 and 10 inclusively.
  • cross-linlced/grafted surface modifying polymers are obtained by homo-or copolymerizatio ⁇ VcrossU ⁇ l*d ⁇ g/grafting of the multifunctional monomers of the present invention.
  • the comonomers are advantageously chosen from among the salts of monofunctional monomers of the general formula:
  • Examples of preferential monofunctional monomers of the invention for a copolymerization graft include:
  • R' is a monovalent organic radical comprising 1 to 12 atoms, preferably perfluorinated, possibly having one or more oxa, aza, thia or dioxathia substituents; and p is 1 or 2.
  • the particular solvent employed for the polymerizable monomer will depend upon the particular monomer employed and upon the particular polymer substrate utilized. All that is necessary is that the monomer(s) dissolve in the solvent and that the solvent does not attack the subsfrate. Thus, the particular solvent system used will depend upon the monomer and substrate employed. Representative suitable solvents include water or organic solvents such as alcohols, esters, ethers, acetone or compatible aqueous mixtures thereof. Alternatively, the monomers can be polymerized/grafted/cross-linked in the absence of a solvent, particularly when the final product desired is of a non-porous nature.
  • the polymerizable monomer is present in the reactant solution at a concentration between about 0.01% and about 100%, preferably between about 1% and about 15% based upon the weight of the monomer when the final product is desired to be porous. Higher concentrations are utilized when the final product is non-porous.
  • Reaction can be effected while the subsfrate is immersed in solution. However, this will result in the polymerization of the monomer(s) throughout the solution. It is preferred to saturate the porous membrane with the reactant solution and to effect reaction outside of the solution so that monomer is not wasted. Thus, the reaction can be conducted batchwise or continuously.
  • a sheet of porous membrane is saturated with the reactant solution and then transferred to a reaction zone where it is exposed to radiation energy such as heat, ultraviolet light or other ionizing radiation to effect the polymerizatioriVgrafting/cross-liijidiig reaction.
  • suitable polymerization initiators which can be utilized include persulfates such as ammonium persulfate, benzophenone, benzoyl peroxide, azobisisobutyronitrile or the like.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Electrochemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Development (AREA)
  • Sustainable Energy (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Transplantation (AREA)
  • Graft Or Block Polymers (AREA)
  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
  • Treatments Of Macromolecular Shaped Articles (AREA)

Abstract

Cette invention concerne un substrat polymère poreux ou non poreux dont la surface est modifiée par un fluorocarbure immobilisé tel qu'une composition polymère perfluorocarburée. Le fluorocarbone immobilisé est constitué par un monomère de formule [T-SO2Y-SO2T']-M+ dans laquelle -T et T' sont identiques ou différentes et comprennent un radical organique doté d'au moins une fonction de polymérisation active telle qu'un insaturation ou un noyau qui peut être ouvert; -M+ comprend un cation inorganique ou organique. -Y comprend N ou CQ dans lequel Q renferme H, CN, F, SO¿2R?3, un alkyle en C¿1-20? substitué ou non, un aryle en C1-20 substitué ou non, un alkylène en C1-20 substitué ou non, dans lequel le substituant comprend un ou plusieurs halogènes, et dans laquelle la chaîne comprend un ou plusieurs F, SO2R, substituants aza, oxa, thia or dioxathia; et -R?3¿ comprend F, un alkyle en C¿1-20? substitué ou non, un aryle en C1-20 substitué ou non, un alkylène en C1-20 substitué ou non, dans lequel le substituant comprend un ou plusieurs halogènes.
PCT/US2001/026720 2000-08-31 2001-08-28 Substrat poreux ou non poreux enduit d'une composition polymere immobilisee avec groupes sulfonyle et groupes fonctionnels hydrophiles et procede de fabrication Ceased WO2002018036A1 (fr)

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JP2002523004A JP2004507345A (ja) 2000-08-31 2001-08-28 スルホニル基および親水性の官能基を有する固定化されたポリマー組成物で被覆された多孔質または非孔質の基材ならびにその方法
US10/344,058 US7094469B2 (en) 2001-08-28 2001-08-28 Porous or non-porous substrate coated with an immobilized polymeric composition having sulfonyl groups and hydrophilic functional groups and process

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US22942100P 2000-08-31 2000-08-31
US60/229,421 2000-08-31

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7094469B2 (en) 2001-08-28 2006-08-22 Mykrolis Corporation Porous or non-porous substrate coated with an immobilized polymeric composition having sulfonyl groups and hydrophilic functional groups and process

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Publication number Priority date Publication date Assignee Title
PL2145917T3 (pl) * 2008-07-17 2012-11-30 Gore W L & Ass Gmbh Powłoka polimerowa zawierająca kompleks jonowego fluoropolieteru oraz środka przeciwjonowego

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4851121A (en) * 1987-10-19 1989-07-25 Fuji Photo Film Co., Ltd. Process for rendering porous membrane hydrophilic
US5463005A (en) * 1992-01-03 1995-10-31 Gas Research Institute Copolymers of tetrafluoroethylene and perfluorinated sulfonyl monomers and membranes made therefrom
WO1999038842A1 (fr) * 1998-01-30 1999-08-05 Hydro-Quebec Derives bis-sulfonyles polymerisables et leur utilisation dans la preparation de membranes echangeuses d'ions

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4851121A (en) * 1987-10-19 1989-07-25 Fuji Photo Film Co., Ltd. Process for rendering porous membrane hydrophilic
US5463005A (en) * 1992-01-03 1995-10-31 Gas Research Institute Copolymers of tetrafluoroethylene and perfluorinated sulfonyl monomers and membranes made therefrom
WO1999038842A1 (fr) * 1998-01-30 1999-08-05 Hydro-Quebec Derives bis-sulfonyles polymerisables et leur utilisation dans la preparation de membranes echangeuses d'ions

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7094469B2 (en) 2001-08-28 2006-08-22 Mykrolis Corporation Porous or non-porous substrate coated with an immobilized polymeric composition having sulfonyl groups and hydrophilic functional groups and process

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