Compositions and polymer films

A novel composition and curing process for ion exchange membranes addresses the limitations of traditional bipolar membranes by producing films with high ion exchange capacity and low resistance, facilitating efficient acid and base production.

JP7802778B2Active Publication Date: 2026-01-20FUJIFILM MANUFACTURING EUROPE BV +1
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Patent Information

Application Number
JP2023519625
Authority / Receiving Office
JP · JP
Patent Type
Patents
Current Assignee / Owner
Priority Date
2020-09-30
Filing Date
2021-09-27
Publication Date
2026-01-20
Estimated Expiration
2041-09-27

AI Technical Summary

Technical Problem

Bipolar membranes formed by fusing cation and anion exchange films suffer from high electrical resistance, bubble formation, and short operational lifespan, making them unsuitable for commercial electrodialysis operations.

Method used

A composition comprising specific monomers with polymerizable groups, solvents, and optional initiators is used to create polymer films with improved ion exchange membranes, which are cured to form cation and anion exchange layers, enhancing mechanical strength and reducing electrical resistance.

Benefits of technology

The resulting polymer films exhibit high ion exchange capacity, low electrical resistance, and improved pH stability, enabling efficient production of acids and bases with low energy costs and high productivity.

✦ Generated by Eureka AI based on patent content.

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Abstract

(a) Formula (I): TIFF2023544993000037.tif2074 (where R is C 1~4 -Alkyl, NH2, or C 6~12 -aryl, and M + is a cation), (b) a monomer comprising at least two polymerizable groups, and (c) a solvent. Further claimed are compositions and processes for making the polymer film.
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Description

[Technical Field]

[0001] The present invention relates to compositions suitable for making polymeric films, polymeric films, cation exchange membranes, bipolar membranes, and their preparation and use. [Background technology]

[0002] Ion exchange membranes are used in electrodialysis, electrodialysis reversal, electrolysis, diffusion dialysis, and several other processes. Typically, the transport of ions through the membrane occurs under the influence of a driving force such as an ion concentration gradient or, alternatively, an electric potential gradient.

[0003] Ion exchange membranes are generally classified as cation exchange membranes or anion exchange membranes depending on their predominant charge. Cation exchange membranes contain negatively charged groups that allow cations to pass but reject anions, while anion exchange membranes contain positively charged groups that allow anions to pass but reject cations. Bipolar membranes have both cation and anion layers.

[0004] Some ion exchange and bipolar membranes contain a porous support that provides mechanical strength. Such membranes are often called "composite membranes" due to the presence of both an ionically charged polymer that discriminates between oppositely charged ions and a porous support that provides mechanical strength.

[0005] Cation exchange membranes may be used for the treatment of aqueous solutions and other polar liquids and for the generation of electricity. Bipolar membranes may be used to produce acids and bases from salt solutions, for example, for the recovery of hydrofluoric acid and nitric acid, for the separation and processing of organic acids such as lactic acid and citric acid, and for the production of amino acids.

[0006] Electricity can be generated using reverse electrodialysis (RED), where process-standard ion-exchange or bipolar membranes can be used. Cation-exchange membranes may also be used for hydrogen production in, for example, fuel cells and batteries.

[0007] Bipolar membranes can be prepared by many different methods. In U.S. Patent Nos. 4,024,043 and 4,057,481 (both to Dege et al.), single-film bipolar membranes are prepared from pre-swollen films containing relatively large amounts of insoluble cross-linked aromatic polymers, in which highly dissociative cation exchange groups are chemically bonded to aromatic nuclei from only one side of the film to a desired depth, and subsequently highly dissociative anion exchange groups are chemically bonded to unreacted aromatic nuclei on the other side of the film.

[0008] In Japanese Patent Publication Nos. 78-158638 and 79-7196 (both Tokuyama Soda Co. Ltd.), bipolar membranes are prepared by partially covering a membrane with a covering film, sulfonating the surface of the membrane not in contact with the covering film to introduce cation exchange groups, peeling off the covering film, and introducing anion exchange groups onto the peeled surface.

[0009] Bipolar membranes can also be prepared by joining an anion exchange film or membrane with a cation exchange film or membrane. A bipolar membrane can be formed by fusing two monopolar membranes of opposite selectivity together using heat and pressure. See, for example, U.S. Patent No. 3,372,101 to Kollsman, which uses a hydraulic press to join separate cation and anion membranes at 400 lb / sq. inch (2,758 kPa) pressure at 150°C to form a two-ply bipolar membrane structure.

[0010] However, bipolar membranes formed in this manner suffer from the drawback of high electrical resistance created by their fusion. Furthermore, these membranes are prone to bubble or blister formation and can only operate for short periods of time at relatively low current densities. [Prior art documents] [Patent documents]

[0011] [Patent Document 1] U.S. Patent No. 4,024,043 [Patent Document 2] U.S. Patent No. 4,057,481 [Patent Document 3] Japanese Patent Application Publication No. 55-86821 [Patent Document 4] Japanese Patent Application Publication No. 55-99927 [Patent Document 5] U.S. Patent No. 3,372,101 Summary of the Invention [Problem to be solved by the invention]

[0012] The above-mentioned drawbacks make known bipolar membranes unattractive for commercial electrodialysis operations. According to a first aspect of the present invention, (a) Formula (I):

[0013] [ka]

[0014] (In the formula, R is C 1~4 -Alkyl, NH2, or C 6~12 -aryl, M + is a cation), (b) a monomer comprising at least two polymerizable groups; (c) a solvent; optionally, (d) a radical initiator; and A composition comprising:

[0015] Preferably, the composition according to the first aspect of the present invention comprises: (a) 5 to 60 wt% of component (a); (b) 10 to 70 wt% of component (b); (c) 10 to 50 wt% of component (c); (d) 0 to 10 wt% of component (d) Includes:

[0016] In a preferred embodiment, M + is H + , Li + , Na + , K. + or the formula NL4 + wherein each L is independently H or C 1~3 It is often used as a cation because it has better solubility in aqueous liquids compared to many other cations. + Li + It is particularly preferred that:

[0017] Compounds of formula (I) may be obtained by methods analogous to those illustrated in the examples, or they may be obtained from commercial sources or by known methods. Examples of compounds of formula (I) that can be used as component (a) include compounds of formula MM-A, formula MM-P, and formula MM-M, shown below.

[0018] Preferably, the composition comprises 5 to 60 wt%, more preferably 5 to 50 wt%, most preferably 5 to 40 wt% of component (a). Preferred polymerizable groups which may be present in component (b) include ethylenically unsaturated groups, especially (Meth)acrylic group , and / or vinyl groups (for example, vinyl ether groups, aromatic vinyl compounds, N-vinyl compounds, and allyl groups).

[0019] Suitable (Meth)acrylic groupExamples include acrylate (HC=CHCO-), acrylamide (HC=CHCONH-), methacrylate (HC=C(CH3)CO-), and methacrylamide (HC=C(CH3)CONH-) groups. acrylic group is more reactive, so acrylic group teeth Methacrylic group is preferable to.

[0020] Preferred ethylenically unsaturated groups do not contain ester groups, as this can improve the stability and pH tolerance of the resulting composition. Preferred ethylenically unsaturated groups that do not contain ester groups include vinyl groups.

[0021] Preferred examples of the polymerizable group include those of the following formula:

[0022] [ka]

[0023] The mentioned groups are possible. Optionally, component (b) further comprises anionic groups. Preferably, in some embodiments, the composition comprises 10 to 70 wt %, more preferably 20 to 70 wt %, and most preferably 30 to 60 wt % of component (b).

[0024] Examples of monomers comprising at least two polymerizable groups that may be used as component (b) and further comprise an anionic group include compounds of the following formula (MA), formula (C), formula (ACL-A), formula (ACL-B), formula (ACL-C), and / or formula (II):

[0025] [ka]

[0026] (In formula (MA), Each R A1 each independently represents a hydrogen atom or an alkyl group; each Z1 each independently represents -O- or -NRa-, Ra represents a hydrogen atom or an alkyl group, Each M + are independently as defined above).

[0027] In formula (MA), each M + Preferred embodiments for each M are independently as defined above. + are independently an organic or inorganic cation, preferably H + , or an alkali metal ion.

[0028] Examples of component (b) of formula (MA) include:

[0029] [ka]

[0030] and salts thereof. Synthetic methods can be found, for example, in US2015 / 0353696 and US2016 / 0369017.

[0031] [ka]

[0032] (In formula (C): Each L 1 each independently represents an alkylene group or an aralkylene group; n is 2 or 3, preferably 2; each m is independently 1 or 2; L 2 represents an n-valent linking group, Each R 1 each independently represents a hydrogen atom or an alkyl group; Each R 2 are independently -SO3 - M + or -SO3 - R 3 represents Each M + are independently as defined above; R 3 represents an alkyl group or an aryl group).

[0033] In one embodiment of Formula (C), M + is H + , inorganic ions, or organic ions. Examples of component (b) of formula (C) include:

[0034] [ka]

[0035] and alternative salts thereof. Synthetic methods can be found in EP3187516.

[0036] [ka]

[0037] (In formula (ACL-A), formula (ACL-B), and formula (ACL-C), R and R' each independently represent a hydrogen atom or an alkyl group; LL represents a single bond or a divalent linking group; LL 1 , L.L. 1 ',LL 2 , and L.L. 2 each independently represents a single bond or a divalent linking atom or group; each of A and A' independently represents a methyl group or a sulfo group in the free acid or salt form of the group; (m represents 1 or 2).

[0038] Examples of component (b) of formula (ACL-A), (ACL-B), or (ACL-C) include the following:

[0039] [ka]

[0040] and alternative salts thereof. Synthesis methods can be found in US2016 / 0362526.

[0041] [ka]

[0042] (In the formula, R' is vinyl (C2H3), epoxy (C2H3O), or C 1~3 -Alkylenethiol (C 1~3 -alkylene-SH), n is 1 or 2, m has a value of 1, 2, or 3; M' + is H + , Li + , Na + , K. + , or NL4 + and each L is independently H or C 1~3 -alkyl, (a) When m and n both have a value of 1, X is vinylphenyl, or a group of formula (III):

[0043] [ka]

[0044] (In formula (III), R" can be vinyl (C2H3), epoxy (C2H3O), or C 1~3 -Alkylenethiol (C 1~3 -alkylene-SH), M” + is H + , Li + , Na + , K. + , or NL4 +and each L is independently H or C 1~3 -alkyl), (b) If m and n do not both have the value 1, then X is C 1~6 -Alkylene, C 6~18 -Arylene, or NR''' (3-m) and each R''' is independently H or C1-C4 alkyl; (c) When m has a value of 1 and n shown in formula (II) has a value of 2, X is of formula (III) (as defined above) or C 1~6 -Alkyl, C 6~18 -aryl, or N(R''')2, where each R''' is independently H or C 1~4 (It is alkyl).

[0045] Examples of component (b) of formula (II) include:

[0046] [ka]

[0047] and alternative salts thereof. Synthesis methods can be found, for example, in JP2018043936. Other examples of component (b) include compounds M-23 to M-34 shown below, and salts thereof.

[0048] [ka]

[0049] Preferably, component (b) is selected from compounds according to formula (ACL-B), formula (ACL-C), and salts thereof, and / or formula (II), as this results in a polymer film with good pH stability. Preferably, the composition comprises at least 10 wt %, more preferably at least 20 wt %, of component (b) selected from compounds according to formula (ACL-B), formula (ACL-C), and salts thereof, and / or formula (II).

[0050] Preferably, component (c) is an inert solvent. In other words, component (c) preferably does not react with any of the other components of the curable composition. In one embodiment, the solvent preferably comprises water and optionally an organic solvent, particularly one in which some or all of the organic solvent is water-miscible. Water is useful for dissolving component (a) and optionally also component (b), and the organic solvent is useful for dissolving any other organic components present in the composition.

[0051] Component (c) is useful for reducing the viscosity and / or surface tension of the composition. In some embodiments, the composition comprises 10 to 50 wt %, more preferably 10 to 40 wt %, especially 16 to 40 wt %, for example 23 to 38 wt % of component (c).

[0052] Examples of inert solvents that may be used as component (c) include water, alcoholic solvents, etheric solvents, amide solvents, ketone solvents, sulfoxide solvents, sulfone solvents, nitrile solvents, and organic phosphorus solvents. Examples of alcoholic solvents that may be used as component (c) or in component (c) (especially in combination with water) include methanol, ethanol, isopropanol, n-butanol, ethylene glycol, propylene glycol, diethylene glycol, dipropylene glycol, and mixtures containing two or more thereof. In addition, preferred inert organic solvents that may be used in component (c) include dimethyl sulfoxide, dimethylimidazolidinone, sulfolane, N-methylpyrrolidone, dimethylformamide, acetonitrile, acetone, 1,4-dioxane, 1,3-dioxolane, tetramethylurea, hexamethylphosphoramide, hexamethylphosphorotriamide, pyridine, propionitrile, butanone, cyclohexanone, tetrahydrofuran, tetrahydropyran, 2-methyltetrahydrofuran, ethylene glycol diacetate, cyclopentyl methyl ether, methyl ethyl ketone, ethyl acetate, y-butyrolactone, and mixtures containing two or more thereof. Dimethyl sulfoxide, N-methylpyrrolidone, dimethylformamide, dimethylimidazolidinone, sulfolane, acetone, cyclopentyl methyl ether, methyl ethyl ketone, acetonitrile, tetrahydrofuran, 2-methyltetrahydrofuran, and mixtures containing two or more thereof are preferred.

[0053] The composition preferably comprises 0 to 2 wt% of component (d). If the composition is intended to be cured thermally or with light (e.g., UV or visible light), the composition preferably comprises 0.001 to 2 wt%, in particular 0.005 to 0.9 wt%, of component (d).

[0054] Examples of suitable thermal initiators that may be used as component (d) include 2,2'-azobis(2-methylpropionitrile) (AIBN), 4,4'-azobis(4-cyanovaleric acid), 2,2'-azobis(2,4-dimethylvaleronitrile), 2,2'-azobis(2-methylbutyronitrile), 1,1'-azobis(cyclohexane-1-carbonitrile), 2,2'-azobis(4-methoxy-2,4-dimethylvaleronitrile), 1,1'-azobis(cyclohexane-1-carbonitrile), 2,2'-azobis(4-methyl ... nitrile), dimethyl 2,2'-azobis(2-methylpropionate), 2,2'-azobis[N-(2-propenyl)-2-methylpropionamide, 1-[(1-cyano-1-methylethyl)azo]formamide, 2,2'-azobis(N-butyl-2-methylpropionamide), 2,2'-azobis(N-cyclohexyl-2-methylpropionamide), 2,2'-azobis(2-methylpropionamidi 2,2'-Azobis[2-(2-imidazolin-2-yl)propane]dihydrochloride, 2,2'-Azobis[2-(2-imidazolin-2-yl)propane]dihydrochloride, 2,2'-Azobis[2-(2-imidazolin-2-yl)propane]disulfate dihydrate, 2,2'-Azobis[N-(2-carboxyethyl)-2-methylpropionamidine]hydrate, 2,2'-Azobis{2-[1-(2-hydroxyethyl)-2-imidazolin-2-yl]propane}dihydrate Examples of suitable azobis include 2,2'-azobis[2-(2-imidazolin-2-yl)propane], 2,2'-azobis(1-imino-1-pyrrolidino-2-ethylpropane) dihydrochloride, 2,2'-azobis{2-methyl-N-[1,1-bis(hydroxymethyl)-2-hydroxyethyl]propionamide}, and 2,2'-azobis[2-methyl-N-(2-hydroxyethyl)propionamide].

[0055] Examples of suitable photoinitiators that may be included in the composition as component (d) include aromatic ketones, acylphosphine compounds, aromatic onium salt compounds, organic peroxides, thio compounds, hexa-arylbiimidazole compounds, ketoxime ester compounds, borate compounds, azinium compounds, metallocene compounds, active ester compounds, compounds having a carbon-halogen bond, and alkylamine compounds. Preferred examples of aromatic ketones, acylphosphine oxide compounds, and thio compounds include compounds having a benzophenone skeleton or a thioxanthone skeleton, as described in "RADIATION CURING IN POLYMER SCIENCE AND TECHNOLOGY," pp. 77-117 (1993).More preferred examples thereof include alpha-thiobenzophenone compounds described in JP1972-6416B (JP-S47-6416B), benzoin ether compounds described in JP1972-3981B (JP-S47-3981B), alpha-substituted benzoin compounds described in JP1972-22326B (JP-S47-22326B), and alpha-substituted benzoin compounds described in JP1972-23664B (JP-S47-23664B). benzoin derivatives described in JP1982-30704A (JP-S57-30704A), aroylphosphonic acid esters described in JP1985-26483B (JP-S60-26483B), dialkoxybenzophenones described in JP1985-26403B (JP-S60-26403B) and JP1987-81345A (JPS62-81345A), benzoin ethers described in JP1989-34242B (JP alpha-aminobenzophenones described in JP 1990-211452A (JP-H02-211452A), U.S. Pat. No. 4,318,791A, and EP 0284561A1, p-di(dimethylaminobenzoyl)benzene described in JP 1990-211452A (JP-H02-211452A), thio-substituted aromatic ketones described in JP 1986-194062A (JPS61-194062A), acylphosphine sulfides described in JP 1990-9597B (JP-H02-9597B), acylphosphines described in JP 1990-9596B (JP-H02-9596B), thioxanthones described in JP 1988-61950B (JP-S63-61950B), and coumarins described in JP 1984-42864B (JP-S59-42864B). In addition, the photoinitiators described in JP2008-105379A and JP2009-114290A are also preferred. In addition, the photoinitiators described in Kato Kiyomi, "Ultraviolet Curing System," pages 65-148 (Research Center Co., Ltd., 1989) may also be used.

[0056] Particularly preferred photoinitiators include Norrish Type II photoinitiators that have an absorption maximum at wavelengths greater than 380 nm when measured in one or more of the following solvents: water, ethanol, and toluene at a temperature of 23° C. Examples include xanthene, flavin, curcumin, porphyrin, anthraquinone, phenoxazine, camphorquinone, phenazine, acridine, phenothiazine, xanthone, thioxanthone, thioxanthene, acridone, flavone, coumarin, fluorenone, quinoline, quinolone, naphthaquinone, quinolinone, arylmethane, azo, benzophenone, carotenoid, cyanine, phthalocyanine, dipyrrin, squarine, stilbene, styryl, triazine, or anthocyanin-derivatized photoinitiators.

[0057] According to a second aspect of the present invention, there is provided a method for preparing a polymer film comprising polymerizing a composition comprising a compound of formula (I), wherein the compound of formula (I) is as defined above.

[0058] In the second aspect of the invention, the preferred embodiments for compounds of formula (I) are as defined herein in relation to the first aspect of the invention. In the second aspect of the invention, the composition is preferably as defined in relation to the first aspect of the invention. Preferred embodiments for the composition used in the method of the second aspect of the invention are as described herein in relation to the first aspect of the invention.

[0059] The composition may be cured to prepare a film according to the second aspect of the present invention by any suitable process, including thermal curing, photocuring, electron beam (EB) irradiation, gamma irradiation, and combinations of the foregoing. Optionally, a dual-cure method, defined as a combination of two of the above-mentioned curing techniques, may be used. However, the composition is preferably cured by photocuring, e.g., by irradiating the composition with visible or ultraviolet light, thereby polymerizing the curable components present in the composition.

[0060] Preferably, the polymerization is carried out in the presence of a porous support. For example, the compound of formula (I) / composition according to the first aspect of the present invention is present in and / or on a porous support. The porous support provides mechanical strength to the polymer film resulting from the polymerization, which is particularly useful when the polymer film is intended to be used as a cation exchange membrane (CEM) or bipolar membrane (BPM).

[0061] Examples of porous supports that can be used include synthetic woven and nonwoven fabrics and extruded films. Examples include wet-laid and dry-laid nonwoven materials, spunbond fabrics, meltblown fabrics, and nanofiber webs made from polyethylene, polypropylene, polyacrylonitrile, polyvinyl chloride, polyphenylene sulfide, polyester, polyamide, polyaryletherketones such as polyetheretherketone, and copolymers thereof. The porous support can also be a porous membrane, such as a polysulfone membrane, a polyethersulfone membrane, a polyphenylene sulfone membrane, a polyphenylene sulfide membrane, a polyimide membrane, a polyetherimide membrane, a polyamide membrane, a polyamideimide membrane, a polyacrylonitrile membrane, a polycarbonate membrane, a polyacrylate membrane, a cellulose acetate membrane, a polypropylene membrane, a poly(4-methyl-1-pentene) membrane, a polyylidene fluoride membrane, a polytetrafluoroethylene membrane, a polyhexafluoropropylene membrane, and a polychlorotrifluoroethylene membrane, and derivatives thereof.

[0062] The porous support preferably has an average thickness of between 10 and 800 μm, more preferably between 15 and 300 μm, especially between 20 and 150 μm. Preferably, the porous support has a porosity between 30 and 95%. The porosity of the support may be determined by a porometer, for example a Porolux™ 1000 from IB-FT GmbH, Germany.

[0063] If present, the porous support may be treated to modify its surface energy, for example to a value greater than 45 mN / m, preferably greater than 55 mN / m. Suitable treatments include, for example, corona discharge treatment, plasma glow discharge treatment, flame treatment, ultraviolet radiation treatment, or chemical treatment to improve the wettability and adhesion of the porous support to polymer films.

[0064] Commercially available porous supports are available from several sources, such as Freudenberg Filtration Technologies (Novatexx materials), Lydall Performance Materials, Celgard LLC, APorous Inc., SWM (Conwed Plastics, DelStar Technologies), Teijin, Hirose, Mitsubishi Paper Mills Ltd, and Sefar AG.

[0065] Preferably, the support is a polymeric support. Preferably, the support comprises a synthetic woven or nonwoven fabric or extruded film that does not have covalently attached ionic groups. According to a third aspect of the present invention there is provided a polymer film obtainable by the process of the second aspect of the present invention.

[0066] Preferably, the polymer film is a cation exchange membrane (CEM) or a bipolar membrane (BPM) comprising a cation exchange layer (CEL) obtained from polymerizing a composition according to the first aspect of the invention and / or a cation exchange layer (CEL) obtained by a process according to the second aspect of the invention. Preferably, the BPM further comprises an anion exchange layer (AEL).

[0067] Preferably, the polymer film obtained by the process according to the second aspect of the present invention has the formula (A):

[0068] [ka]

[0069] (In the formula, M + is preferably a cation as defined above). In formula (A), the asterisk indicates the point where the structural group is covalently attached to another structural element of the polymer film.

[0070] In a process according to the second aspect of the present invention which is preferred, the curable composition according to the first aspect of the present invention is applied continuously to a moving (porous) support, preferably by a manufacturing section which includes a curable composition application station, one or more irradiation sources for curing the composition, a membrane collection station, and means for moving the support from the curable composition application station to the irradiation sources and to the membrane collection station.

[0071] The curable composition application station may be located upstream relative to the irradiation source, and the irradiation source may be located upstream relative to the film recovery station. Examples of suitable coating techniques for applying the curable composition according to the first aspect of the present invention to a porous support include slot die coating, slide coating, air knife coating, roller coating, screen printing, and dipping. Depending on the technique used and the desired final specifications, it may be desirable to remove excess coating from the substrate, for example, by roll-to-roll squeeze, roll-to-blade or blade-to-roll squeeze, blade-to-blade squeeze, or removal using a coating bar. Light curing is preferably performed at a dose of 40 to 1500 mJ / cm. -2 The process is carried out at wavelengths between 400 nm and 800 nm, using a dose between 100 and 1500 nm. In some cases, additional drying may be required, at which temperatures between 40°C and 200°C may be employed.

[0072] Using the process according to the second aspect of the present invention, polymer films (e.g., CEM and BPM) according to the third aspect of the present invention may be prepared in several ways, including multi-pass and single-pass processes. For example, in a two-pass process, each of the layers of the BPM (e.g., CEL and AEL) may be produced in a separate step. In the first step to produce the first layer, an optionally pretreated porous support may be impregnated with a first curable composition. To ensure a thin, pinhole-free film, the coating step is preferably followed by squeezing. The impregnated support may then be cured to provide a layer that is sufficiently rigid for handling in a coating machine but still contains enough unreacted polymerizable groups to ensure good adhesion to the second layer. In the second step, a process very similar to that for the first layer may be used, in which an optionally pretreated porous support is impregnated with a second curable composition and laminated to the first layer, followed by squeezing out the excess composition and curing.

[0073] In an alternative method for making a BPM, a second layer is coated onto the first layer, followed by laminating an optionally pretreated porous support on the side of the second curable composition, whereby the second curable composition penetrates the porous support. The resulting laminate may be compressed and cured to yield a composite membrane.

[0074] In the two-pass process described above, preferably either the first or second curable composition is as defined in the first aspect of the present invention. In a more preferred single-pass process for preparing a BPM, two optionally pretreated porous supports are unrolled and each is impregnated (e.g., simultaneously or sequentially) with a curable composition, one of which is as defined in the first aspect of the invention as providing a CEL and the other curable composition comprises at least one cationic curable monomer to provide an AEL. The two layers (the CEL from the composition according to the first aspect of the invention, and the AEL from the other curable composition) are then laminated together and squeezed, and the resulting laminate is subsequently cured to provide the final BPM.

[0075] The efficiency of the BPM according to the third aspect of the invention may be increased by increasing the surface area between the AEL and CEL, for example by physical treatment (roughening) or by other means.

[0076] In one embodiment, the BPM according to the third aspect of the invention optionally comprises a catalyst, such as a metal salt, metal oxide, organometallic compound, monomer, polymer, or copolymer, or salt, preferably at the interface between the CEL and AEL of the BPM.

[0077] Suitable inorganic compounds or salts that may be used as catalysts include, for example, cations selected from Groups 1a to 4a (inclusive), along with the lanthanide and actinide series elements of the Periodic Table of the Elements, such as thorium, zirconium, iron, lanthanum, cobalt, cadmium, manganese, cerium, molybdenum, nickel, copper, chromium, ruthenium, rhodium, tin, titanium, and indium, and combinations comprising two or more of the foregoing. Suitable salts that may be used as catalysts include anions such as tetraborate, metaborate, silicate, metasilicate, tungstate, chlorate, phosphate, sulfate, chromate, hydroxyl, carbonate, molybdate, chloroplatinate, chloropalladite, orthobanate, tellurite, and others, and combinations comprising two or more of the foregoing.

[0078] Other examples of inorganic compounds or salts that may be used as catalysts include, but are not limited to, FeCl3, FeCl2, AlCl3, MgCl2, RuCl3, CrCl3, Fe(OH)3, Al2O3, NiO, Zr(HPO4)2, MoS2, graphene oxide, Fe-polyvinyl alcohol complexes, polyvinyl alcohol (PVA), polyethylene glycol (PEG), polyethyleneimine (PEI), polyacrylic acid (PAA), copolymers of acrylic acid and maleic anhydride (PAAMA), and hyperbranched aliphatic polyesters, and combinations comprising two or more of the foregoing.

[0079] As a result of preparing a CEM from a composition according to the first aspect of the present invention having a low amount of component (c), for example, 10 to 40 wt %, the CEM (which is a polymer film) according to the third aspect of the present invention preferably has a very high density. Thus, the present invention enables the production of polymer films (e.g., CEMs and BPMs) having very high ion exchange capacity, and consequently, high selectivity and low electrical resistance (ER).

[0080] Preferably, the ER (for 0.5M NaCl) is 5 ohm.cm 2 Lower, preferably 2.5 ohm.cm 2 Lower. Component (b) of the composition preferably comprises a compound of formula (ACL-B), formula (ACL-C), and / or formula (II) (including the salts described above) because this can result in polymer films (e.g., CEM and BPM) with excellent pH stability in the range of 0 to 14.

[0081] Furthermore, the CEM according to the present invention and the BPM containing a cation exchange layer (CEL) have low electrical resistance. As a result, the CEM and BPM according to the present invention can be used in bipolar electrodialysis to provide high voltage at low current density. Therefore, when the BPM according to the present invention is used in a bipolar electrodialysis process for producing acids and bases, the BPM can provide low energy costs and / or high productivity.

[0082] In one embodiment, the polymer film according to the third aspect of the invention is preferably a bipolar membrane or a membrane that can be converted into a bipolar membrane by hydrolysis. The anion exchange layer (AEL) of the bipolar membrane is preferably obtained by curing a composition containing a curable cationic compound (i.e., an AEL composition). Accordingly, the AEL composition preferably contains a curable cationic compound.

[0083] Preferred curable cationic compounds contain at least two ethylenically unsaturated groups, such as those represented by formula (IV):

[0084] [ka]

[0085] (In the formula, L 1 is an alkylene or alkenylene group, R a , R b , R c , and R d are each independently an alkyl group or an aryl group; or R a and R b , and / or R c and R d may form a ring together with the atoms to which they are attached, n1 and n2 each independently represent an integer having a value of 1 to 10, X1 -and X2 - each independently represents an anion).

[0086] L 1 is preferably ethylene (CH2CH2), propylene (CH2CH2CH2), hexylene (CH2CH2CH2CH2CH2CH2CH2), or vinylene (CH=CH).

[0087] R a , R b , R c , and R d If any of the is an alkyl group, it is preferably C 1~4 alkyl groups, in particular methyl. R a , R b , R c , and R d When any of is an aryl group, it is preferably C 6~10 - an aryl group, in particular phenyl.

[0088] R a and R b , and / or R c and R d When they form a ring together with the atoms to which they are attached, the ring is preferably a five- or six-membered ring. X1 - and X2 - are preferably each independently halo, especially Cl - is.

[0089] Thus, the AEL composition preferably comprises the following ingredients: (a2) a curable cationic compound containing at least two ethylenically unsaturated groups; and optionally (b2) a compound containing one and only one ethylenically unsaturated group; optionally (c2) a solvent; optionally (d2) a radical initiator; Includes:

[0090] Preferably, the AEL composition comprises at least one, more preferably at least two, especially all three of component (b2), component (c2), and component (d2). Examples of compounds of formula (IV) include:

[0091] [ka]

[0092] Examples include: Synthetic methods can be found, for example, in EP3184558 and US2016 / 0001238.

[0093] The AEL composition preferably comprises 30-80 wt% of component (a2), more preferably between 40-70 wt% of component (a2). Preferably, the AEL composition comprises: (i) 30 to 80 wt% of component (a2); (ii) 0 to 40 wt% of component (b2); (iii) 10 to 40 wt% of component (c2) Includes:

[0094] Component (b2) preferably contains an aromatic group. Component (b2) preferably contains cationic groups. Examples of compounds that may be used as component (b2) of the AEL composition include the following:

[0095] [ka]

[0096] Examples include: The above compounds may be prepared, for example, as described in US2016177006.

[0097] Preferably, the molar ratio of component (a2) to component (b2) is 9:1 to 1:4. The AEL composition comprises 0 to 60 wt %, more preferably 5 to 45 wt %, and most preferably 10 to 40 wt % of component (b2).

[0098] Component (c2) of the AEL composition preferably comprises water and, optionally, an organic solvent, particularly where some or all of the organic solvent is water-miscible. The water is useful for dissolving the compound of formula (IV) and, if present, component (c2). The solvent is useful for reducing the viscosity and / or surface tension of the composition.

[0099] Examples of suitable solvents that may be used as component (c2) of the AEL composition include water, alcoholic solvents, etheric solvents, amide-based solvents, ketone-based solvents, sulfoxide-based solvents, sulfone-based solvents, nitrile-based solvents, organic phosphorus-based solvents, and mixtures comprising two or more thereof. Examples of alcoholic solvents that may be used as component (c2) or in component (c2) (especially in combination with water) include methanol, ethanol, isopropanol, n-butanol, ethylene glycol, propylene glycol, diethylene glycol, dipropylene glycol, and mixtures comprising two or more thereof. In addition, preferred inert organic solvents that may be used in component (c2) include dimethyl sulfoxide, dimethylimidazolidinone, sulfolane, N-methylpyrrolidone, dimethylformamide, acetonitrile, acetone, 1,4-dioxane, 1,3-dioxolane, tetramethylurea, hexamethylphosphoramide, hexamethylphosphorotriamide, pyridine, propionitrile, butanone, cyclohexanone, tetrahydrofuran, tetrahydropyran, 2-methyltetrahydrofuran, ethylene glycol diacetate, cyclopentyl methyl ether, methyl ethyl ketone, ethyl acetate, y-butyrolactone, and mixtures containing two or more thereof. Dimethyl sulfoxide, N-methylpyrrolidone, dimethylformamide, dimethylimidazolidinone, sulfolane, acetone, cyclopentyl methyl ether, methyl ethyl ketone, acetonitrile, tetrahydrofuran, 2-methyltetrahydrofuran, and mixtures containing two or more thereof are preferred.

[0100] In some embodiments, the AEL composition comprises 10 to 40 wt %, more preferably 10 to 35 wt %, and most preferably 15 to 30 wt % of component (c2). Examples of components (c2)-(d2) that may be included in the AEL composition used to form the AEL are as described above for the composition used for the CEL as components (c) and (d), respectively. However, component (c2) of the AEL composition is preferably aqueous.

[0101] Component (d2) preferably is or comprises a thermal initiator, a photoinitiator, or a combination thereof. Most preferably, component (d) is or comprises a photoinitiator.

[0102] Examples of suitable photoinitiators that may be used as component (d2) of the AEL composition include those described above in relation to the composition according to the first aspect of the invention. The AEL composition preferably contains 0.001 to 2 wt % of component (d2), more preferably 0.005 to 0.9 wt %.

[0103] The AEL composition and the CEL composition optionally each independently further comprise a polymerization inhibitor, which can be useful in making the compositions stable during storage and use.

[0104] As the polymerization inhibitor, well-known polymerization inhibitors can be used, examples of which include phenol compounds, hydroquinone compounds, certain amine compounds, mercapto compounds, and nitroxyl radical compounds.

[0105] Examples of phenolic compounds include hindered phenols (phenols having a t-butyl group at the ortho position, typically 2,6-di-t-butyl-4-methylphenol) and bisphenols. Specific examples of hydroquinone compounds include monomethyl ether hydroquinone. Specific examples of amine compounds include N-nitroso-N-phenylhydroxylamine and N,N-diethylhydroxylamine. Specific examples of nitroxyl radical compounds include 4-hydroxyTEMPO (4-hydroxy-2,2,6,6-tetramethylpiperidine-1-oxyl free radical).

[0106] The AEL and CEL compositions optionally each independently further comprise two or more polymerization inhibitors. When the composition used to form the AEL or CEL contains a polymerization inhibitor, the content is preferably 0.01 to 5 wt %, more preferably 0.01 to 1 wt %, and even more preferably 0.01 to 0.5 wt %, relative to the total weight of the composition.

[0107] The AEL composition and the CEL composition optionally each independently further comprise a surfactant, a polymeric dispersant, and / or an anti-crater agent. Various polymer compounds may be included in the AEL and / or CEL composition films to adjust their physical properties. Suitable polymer compounds include acrylic polymers, polyurethane resins, polyamide resins, polyester resins, epoxy resins, phenolic resins, polycarbonate resins, polyvinyl butyral resins, polyvinyl formal resins, shellac, vinyl resins, acrylic resins, rubber resins, waxes, and natural resins, as well as combinations of two or more of the foregoing.

[0108] The AEL composition and the CEL composition may each independently further comprise a surfactant, such as a nonionic surfactant, a cationic surfactant, or an organic fluorosurfactant. Specific examples of surfactants include anionic surfactants (e.g., alkylbenzenesulfonates, alkylnaphthalenesulfonates, higher fatty acid salts, sulfonates of higher fatty acid esters, sulfate ester salts of higher alcohol ethers, sulfonates of higher alcohol ethers, alkyl carboxylate salts of higher alkylsulfonamides, and alkyl phosphate salts), and nonionic surfactants (e.g., poly(oxyethylene) alkyl ethers, poly(oxyethylene) alkylphenyl ethers, poly(oxyethylene) fatty acid esters, sorbitan fatty acid esters, ethylene oxide adducts of acetylene glycol, ethylene oxide adducts of glycerin, and polyoxyethylene sorbitan fatty acid esters). Other examples of suitable surfactants include amphoteric surfactants (e.g., alkylbetaines and amidobetaines), silicone surfactants, and fluorosurfactants. The surfactant may be suitably selected from surfactants known in the art or their derivatives.

[0109] The AEL composition and the CEL composition optionally each independently further comprise a polymeric dispersant. Specific examples of polymer dispersants include polyvinylpyrrolidone, polyvinyl alcohol, polyvinyl methyl ether, polyethylene oxide, polyethylene glycol, polypropylene glycol, and polyacrylamide. Among these, polyvinylpyrrolidone is preferably used.

[0110] The AEL and CEL compositions optionally each independently further comprise an anti-crater agent (sometimes called a surface conditioner), a leveling or slip agent to prevent unevenness on the CEL or AEL surface, examples of which include organo-modified polysiloxanes (mixtures of polyether siloxanes and polyethers), polyether-modified polysiloxane copolymers, and silicone-modified copolymers.

[0111] Examples of commercially available surfactants that may be included in the compositions used to form the AEL and / or CEL include Tego Glide™ 432, Tego Glide™ 110, Tego Glide™ 130, Tego Glide™ 406, Tego Glide™ 410, Tego Glide™ 411, Tego Glide™ 415, Tego Glide™ 420, Tego Glide™ 435, Tego Glide™ 440, Tego Glide™ 450, Tego Glide™ 482, Tego Glide™ A115, Tego Glide™ B1484, and Tego Glide™ ZG400 (all trade names) manufactured by Evonik Industries GmbH.

[0112] The AEL and CEL compositions preferably each independently comprise 0 to 10 wt%, more preferably 0 to 5 wt%, especially 1 to 2 wt% of anti-crater agent (based on the total weight of the relevant composition).

[0113] In a preferred embodiment, the bipolar membrane includes a catalyst. The catalyst may be included in the AEL composition and / or the CEL composition curable composition. For example, the catalyst can be applied to the AEL (as a post-treatment step) (e.g., before applying the CEL composition thereto) using, but not limited to, dipping, air knife coating, micro-roller coating, spraying, chemical (vapor deposition) deposition, or physical (vapor deposition) deposition.

[0114] Examples of suitable catalysts are described above. When the AEL or CEL composition includes a catalyst, the amount of catalyst is preferably up to 5 wt %, for example 0.001 wt % to 1 wt %, based on the weight of the relevant composition.

[0115] The bipolar membrane is (i) applying an AEL composition to a substrate; (ii) at least partially curing the AEL composition, thereby forming an anion exchange layer (AEL); (iii) applying a CEL composition to the AEL; (iv) curing the CEL composition, thereby forming a cation exchange layer (CEL) on the AEL; It may be prepared by a method comprising:

[0116] In step (ii), the AEL composition is preferably photocured, for example using ultraviolet light. Thus, preferably, component (d2) of the AEL composition is or comprises a photoinitiator.

[0117] In step (ii), the AEL composition is preferably cured to an extent such that the resulting AEL can be processed in a curable composition application station while still containing unreacted ethylenically unsaturated groups available for crosslinking to the monomers of the CEL composition.

[0118] In step (iv), the CEL composition is preferably thermally cured, and therefore preferably, component (d) of the CEL composition is or comprises a thermal initiator. The temperature suitable for curing the CEL composition is 50 to 120°C, more preferably 50 to 100°C, and particularly 60 to 85°C.

[0119] Thermal curing of the CEL composition typically takes from one minute or more to several hours. Optionally, the CEL composition is sandwiched between polymer films to prevent evaporation of component (c), if present, and then cured.

[0120] The composition is preferably applied sequentially in step (i) and step (iii), preferably by a manufacturing unit including a composition application station, one or more curing stations equipped with a radiation source if the composition is photocurable, one or more curing stations equipped with one or more heat sources if the composition is heat curable, a bipolar membrane collection station, and means for moving the support from the composition application station to the curing station and to the bipolar membrane collection station.

[0121] The composition application station may be located upstream relative to the curing station, which may be located upstream relative to the bipolar membrane collection station. Examples of application techniques include slot die coating, slide coating, air knife coating, roller coating, screen printing, and dipping. Depending on the technique used and the desired final specifications, it may be necessary to remove excess composition from the substrate, for example, by roll-to-roll squeeze, roll-to-blade or blade-to-roll squeeze, blade-to-blade squeeze, or removal using a coating bar.

[0122] Photocuring with ultraviolet or visible light is preferred, typically at 40-1500 mJ / cm 2 The thermal curing is preferably carried out at a temperature between 20°C and 100°C for a period of, for example, 0.01 hours to 24 hours.

[0123] The performance of a bipolar membrane is characterized by a plot of strength versus voltage. To measure this plot, a six-compartment cell was used. The first electrode compartment contained a platinum plate as the cathode and was separated from the second compartment by a CEM (CMX from Astom). The electrode compartments were filled with 0.5 M Na2SO4. A reference BPM (from Fumatech) was located between the second and third compartments. Both compartments contained 0.5 M NaCl solution. The BPM to be analyzed was placed between the third and fourth compartments. The same reference BPM (from Fumatech) was located between the fourth and fifth compartments, and a CEM (CMX from Astom) was located between the fifth and sixth compartments. The fourth and fifth compartments were also filled with 0.5 M NaCl solution. The sixth compartment, containing a platinum plate as the anode, was the electrode compartment and contained 0.5 M Na2SO4.

[0124] Using the cell described above, the solution was measured at a temperature of 25°C and had a current of 600 A / m 2 A current density was applied and pumped through the chamber, and the bipolar voltage was measured using Haber-Luggin capillaries placed on either side of the BPM to be analyzed. [Example]

[0125] [Table 1-1]

[0126] [Table 1-2]

[0127] [ka]

[0128] The lithium content of the prepared compounds of formula (I) was determined using inductively coupled plasma atomic emission spectroscopy (ICP-OES). The ICP-OES analysis was carried out using a Thermo iCAP™ PRO XP ICP-OES instrument from Thermo Fisher Scientific. A coaxial nebulizer was used in conjunction with a cyclone spray chamber. Approximately 50 mg of each compound under test was sprayed onto a 50 cm 3 The compounds were dissolved in Milli-Q water. The dissolved compounds were diluted 100 times and acidified with 0.5% concentrated nitric acid containing yttrium as an internal standard. All samples were prepared and measured in duplicate. Results were expressed as g of Li per kg of monomer.

[0129] A Magritek Spincolve 60 Carbon (60 MHz, 4 scans) NMR spectrometer was used. 1 The structure of the compound of formula (I) was confirmed by H-NMR. Samples for analysis were prepared by dissolving 5 wt % of each compound of formula (I) in DMSO-d6.

[0130] The purity of the compound of formula (I) was determined by HPLC-MS. A Waters ACQUITY UPLC System with 2D Technology was used. The UPLC was equipped with two pumps (BSM and QSM), an FTN sample manager, a column manager, and a PDA detector (192 to 400 nm). The HPLC was equipped with a Waters Xbridge C8 5 μm 2.1 × 150 mm column using an operating temperature of 45°C. Additionally, the instrument was equipped with a Waters Q-TOF premier mass spectrometer with ESI and ESCi ionization options. Chromatograms were collected using dual detection mode. The PDA detector collected the signal at 245 nm. The mass detector was set to negative mode to detect anionic molecules. A sample containing the compound of formula (I) was prepared as follows: 5 mg of the compound of formula (I) was dissolved in 50 ml of Milli-Q water. The resulting solution was diluted 10 times with Milli-Q water and a volume of 10 μl was injected into the HPLC-MS instrument described above for analysis.

[0131] Table 2 shows a typical method employed to elute samples of compounds of formula (I) represented in Table 3. In Table 3, a summary of the retention times and molecular weights recorded for identification of the substances is provided.

[0132] [Table 2]

[0133] [Table 3]

[0134] The solubility of the compounds of formula (I) was determined visually or by UV spectroscopy. For each compound of formula (I), three solutions containing a 1:1 molar ratio of the compound of formula (I) to the crosslinker Li-BVBSI were prepared: one solution at 30 wt%, one solution at 60 wt%, and one solution at 70 wt%. 500 ppm of 4OH-TEMPO was included in all three solutions to prevent premature polymerization. The solutions were kept in a 40°C water bath overnight and centrifuged prior to investigation. UV spectra were recorded using a 1 mm pathlength quartz cuvette on an Agilent Technologies Cary™ 100 UV-visible spectrophotometer.

[0135] [ka]

[0136] [Table 4]

[0137] In a separate, comparative experiment from that shown in Table 4, the highest solubility achieved by mixing lithium styrene sulfonate (LiSS) and DVBS-Na was found to be 55 wt%. Furthermore, when a compound of formula (I) shown in Table 2 (where M is Li) was combined with DVBS-Na, the solubility achieved was at least 60 wt% in all cases. When a compound of formula (I) shown in Table 4 (where M is Li) was combined with a crosslinker from the bis-sulfonamide family (e.g., of formula (II)), the highest solubility achieved reached a solids content of over 70 wt%.

[0138] The ER (ohm.cm) of the polymer films prepared in the examples was determined by the method described by Dlugolecki et al., J. of Membrane Science, 319 (2008), pp. 217-218, with the following modifications: 2 ) was measured.

[0139] The auxiliary membranes were CMX and AMX from Tokuyama Soda, Japan. The capillary and Ag / AgCl reference electrode (Metrohm type 6.0750.100) contained 3M KCl. The calibration solution and the liquid in chambers 2, 3, 4 and 5 were 0.5M NaCl solutions at 25°C. The effective membrane area is 9.62cm 2 was, The distance between the capillaries was 5.0 mm. The measurement temperature was 25°C. Cole Parmer Masterflex console drives (77521-47) with Easyload II model 77200-62 gear pumps were used for all chambers. The flow rate of each stream was 475 ml / min, controlled by a Porter Instrument flow meter (model 150AV-B250-4RVS) and a Cole Parmer flow meter (model G-30217-90); and Prior to measurements, samples were equilibrated in a 0.5 M solution of NaCl for at least 1 hour at room temperature.

[0140] Preferably, the ER (for 0.5M NaCl) is 5 ohm.cm 2 Lower, preferably 2.5 ohm.cm 2 Lower. Permselectivity (PS) measurement The permselectivity PS (%), which is the selectivity for the passage of ions of opposite charge to the charge of the cationically charged membranes prepared in the examples, was measured as follows: The membrane to be analyzed was placed in a two-chamber system: one chamber was filled with a 0.05 M solution of NaOH and the other with a 0.5 M solution of NaOH.

[0141] setting: The capillary and Ag / AgCl reference electrode (Metrohm type 6.0750.100) contained 3M KCl. The effective membrane area is 9.62cm2 was, The distance between the capillaries was approximately 15 mm. The measured temperature was 21.0±0.2℃. A Cole Parmer Masterflex console drive (77521-47) with an EasyLoad II model 77200-62 gear pump was used for two chambers. Flow was controlled at a constant 500 ml / min using a Porter Instrument flow meter (model 150AV-B250-4RVS) and a Cole Parmer flow meter (model G-30217-90). Prior to measurements, the samples were equilibrated in 0.5M NaOH solution for 1 hour. After 20 minutes, voltage readings were taken from a standard VOM (multimeter).

[0142] Preferably, the PS with respect to NaOH was at least 50%. pH stability To broaden the range of applications in which a CEM can be used, it is preferable that it be stable in acidic and / or alkaline conditions. Stability is typically tested by immersing a sample in 4M HCl or NaOH at 80°C for 7 days. After this treatment, the selectivity should be at least 80% of the original selectivity to be considered stable. Preparation of compounds of formula (I) and comparative compounds MM-Tf, MM-A, MM-P, and MM-M (mentioned above) had the structures shown below.

[0143] [ka]

[0144] Compounds MM-Tf, MM-A, MM-P, and MM-M were synthesized according to the following general scheme and procedures.

[0145] [ka]

[0146] General Procedure Prior to synthesis, the corresponding sulfamide was dried overnight in a vacuum oven at 30°C. To a solution of the dried sulfamide (0.100 mol, 1 mol eq) and 4OH-TEMPO (30 mg, 500 ppm) in THF (100 mL) was added LiH (0.300 mol, 3 mol eq) as a solid in one portion. The reaction mixture was stirred for 30 min at room temperature. Then, a solution of vinylbenzylsulfonyl chloride (0.100 mol, 1 mol eq) in THF (50 mL) was added, and the reaction mixture was heated to 60°C (water bath temperature) for 16 h. The resulting solution was filtered through Celite, and the resulting foam was dissolved in 500 mL of ethyl acetate. Celite was added, and the resulting slurry was stirred for 5 min. The Celite was then filtered off and washed with 100 mL of ethyl acetate. The solvent was then evaporated in vacuo, and the resulting white foam was triturated with 500 mL of diethyl ether overnight. The resulting compound of formula (i) was recovered by filtration and isolated as a white, hygroscopic powder. Yield and purity data are shown in Table 5 below.

[0147] [Table 5]

[0148] Composition Examples 1 to 10, Comparative Examples CEx1 to CEx4, and Polymer Films Table 6 below sets forth the compositions of Examples 1-10 according to the first aspect of the present invention and Comparative Examples CEx1-CEx4. Each of the compositions was polymerized and coated onto a polypropylene / polyethylene porous substrate using a 100 μm Meyer bar for reinforcement to form a 100 μm thick polymer film. The electrical resistance (ER) of the resulting polymer films was measured using 0.5 N NaCl, and the permselectivity (PS) was measured as described above, with the results shown in the last column of Table 6.

[0149] [Table 6]

[0150] [Table 7]

[0151] Infrared analysis ATR-FTIR spectra were recorded on the polymer films using a PerkinElmer Frontier FT-IR Spectrometer using a Universal ATR Sampling Accessory equipped with a diamond top plate. -1 with a spectral resolution of 4000-580 cm -1 Spectra were recorded in the range of 10 s and averaged over the 10 recorded spectra. For optimal peak resolution, the polymer film sample was pressed against an ATR diamond with a conical tip (force gauge, 75). The results for Example 7 and Comparative Example CEx2 are shown in Table 8 below.

[0152] [Table 8]

[0153] From Table 8, the strong IR peaks at 1262, 1151, 1076, and 1048 can be used to distinguish the bisulfonimide functional groups from the sulfonic acid functional groups in the polymer film samples. extraction analysis To analyze the degree of polymerization of the polymer film and to demonstrate the presence of the claimed substance in the polymer film, a sample of the polymer film was dissolved in purified water (10 cm in 50 mL of purified water). 2 ) was extracted and the extract was then analyzed by the HPLC-MS method described above.

[0154] [Table 9]

[0155] Preparation of AEL An AEL composition was prepared containing 58 wt% 1,4-diazoniabicyclo[2.2.2]octane, 1,4-bis[(4-ethenylphenyl)methyl]-, chloride, 19 wt% water, 6 wt% IPA, 1 wt% Omnirad™ TPO-L, and 1 wt% Omnirad™ 1173. The AEL composition was coated onto a polyethylene nonwoven fabric and cured by UV. Preparation of CEL for producing BPM and its application to AEL The CEL compositions were prepared according to Table 7 (Example 9 and Comparative Example CEx4). The CEL compositions were coated onto the AEL prepared as described above, and then a second polyethylene nonwoven fabric was placed on the layer of CEL composition, the excess CEL composition was wiped off, and the CEL composition was cured using UV light.

[0156] The electrochemical and bipolar characteristics of this bipolar membrane were compared with a reference membrane using the so-called current-voltage characteristic (IU curve), in which the current density was measured as a function of the applied voltage. Typically, at a given current density, i.e., 600 mA / cm 2 The lower the voltage (U) required to generate , the lower the ionic resistance of one or both of the ion exchange layers specifically, and of the bipolar membrane in general. A lower ionic resistance, in this case of the cation exchange layer, results in a more energy efficient membrane.

[0157] [Table 10]

Claims

1. (a) Formula (I): 【Chemistry 1】 (In the formula, R is methyl, phenyl, NH 2 , or benzyl, M + is a cation; (b) a monomer comprising at least two polymerizable groups each independently selected from a (meth)acrylic group and a vinyl group; (c) a solvent; A polymer film obtained by polymerizing a composition comprising:

2. The composition comprises: (a) 5 to 60 wt % of component (a); (b) 10 to 70 wt % of component (b); (c) 10 to 50 wt % of component (c); The polymer film of claim 1 , comprising:

3. 3. The polymer film according to claim 1, wherein component (b) further comprises a sulfo group or a bissulfonylimide group.

4. 4. The polymer film according to claim 1, wherein component (a) does not contain fluorine atoms.

5. The polymer film of claim 1 which is a cation exchange membrane.

6. A bipolar membrane comprising the polymer film of any one of claims 1 to 4.

7. Formula (IV): 【Chemistry 2】 (In the formula, L 1 is an alkylene or alkenylene group, R a , R b , R c , and R d are each independently an alkyl group or an aryl group, or R a and R b , and / or R c and R d form a ring together with the atoms to which they are attached, n1 and n2 each independently represent an integer having a value of 1 to 10; X 1 - and X 2 - each independently represents an anion) 7. The bipolar membrane of claim 6, further comprising an anion exchange layer (AEL) obtained by curing a composition comprising the compound of formula (I).

8. (a) Formula (I); 【Transformation 3】 (In the formula, R is methyl, phenyl, NH 2 , or benzyl, M + is a cation; (b) a monomer comprising at least two polymerizable groups each independently selected from a (meth)acrylic group and a vinyl group; (c) a solvent.

9. (a) Formula (I); 【Chemistry 4】 (In the formula, R is methyl, phenyl, NH 2 , or benzyl, M + is a cation; (b) a monomer comprising at least two polymerizable groups each independently selected from a (meth)acrylic group and a vinyl group; (c) a solvent; A composition comprising:

10. (a) 5 to 60 wt % of component (a); (b) 10 to 70 wt % of component (b); (c) 10 to 50 wt % of component (c); (d) 0 to 10 wt % of an initiator as component (d); 10. The composition of claim 9, comprising:

11. 6. Use of a cation exchange membrane according to claim 5 for the treatment of polar liquids, for the production of hydrogen or for the generation of electricity.

12. 7. Use of the bipolar membrane according to claim 6 for the production of acids and bases, for the separation or treatment of organic acids, for the production of amino acids or for the generation of electricity.

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