WO2013103257A1 - 내오염성이 우수한 역삼투막 및 그 제조방법 - Google Patents
내오염성이 우수한 역삼투막 및 그 제조방법 Download PDFInfo
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- WO2013103257A1 WO2013103257A1 PCT/KR2013/000048 KR2013000048W WO2013103257A1 WO 2013103257 A1 WO2013103257 A1 WO 2013103257A1 KR 2013000048 W KR2013000048 W KR 2013000048W WO 2013103257 A1 WO2013103257 A1 WO 2013103257A1
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- trimethylammonio
- dimethyl
- phosphate
- ammonium hydroxide
- butyl
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
- B01D71/06—Organic material
- B01D71/76—Macromolecular material not specifically provided for in a single one of groups B01D71/08 - B01D71/74
- B01D71/82—Macromolecular material not specifically provided for in a single one of groups B01D71/08 - B01D71/74 characterised by the presence of specified groups, e.g. introduced by chemical after-treatment
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D65/00—Accessories or auxiliary operations, in general, for separation processes or apparatus using semi-permeable membranes
- B01D65/08—Prevention of membrane fouling or of concentration polarisation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
- B01D67/0002—Organic membrane manufacture
- B01D67/0006—Organic membrane manufacture by chemical reactions
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
- B01D67/0081—After-treatment of organic or inorganic membranes
- B01D67/0093—Chemical modification
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/02—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor characterised by their properties
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/12—Composite membranes; Ultra-thin membranes
- B01D69/1213—Laminated layers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/12—Composite membranes; Ultra-thin membranes
- B01D69/125—In situ manufacturing by polymerisation, polycondensation, cross-linking or chemical reaction
- B01D69/1251—In situ manufacturing by polymerisation, polycondensation, cross-linking or chemical reaction by interfacial polymerisation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
- B01D71/06—Organic material
- B01D71/40—Polymers of unsaturated acids or derivatives thereof, e.g. salts, amides, imides, nitriles, anhydrides, esters
- B01D71/401—Polymers based on the polymerisation of acrylic acid, e.g. polyacrylate
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
- B01D71/06—Organic material
- B01D71/56—Polyamides, e.g. polyester-amides
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
- B01D71/06—Organic material
- B01D71/76—Macromolecular material not specifically provided for in a single one of groups B01D71/08 - B01D71/74
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2323/00—Details relating to membrane preparation
- B01D2323/40—Details relating to membrane preparation in-situ membrane formation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2325/00—Details relating to properties of membranes
- B01D2325/18—Membrane materials having mixed charged functional groups
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/02—Reverse osmosis; Hyperfiltration ; Nanofiltration
- B01D61/025—Reverse osmosis; Hyperfiltration
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- 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
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
- Y02A20/131—Reverse-osmosis
Definitions
- the present invention relates to a reverse osmosis membrane and a method for manufacturing the same, and more particularly, a coating layer comprising a copolymer of an amphoteric ionic compound and glycidyl methacrylate is formed on the surface thereof, and thus, a reverse osmosis membrane having excellent stain resistance and its preparation It is about a method.
- Osmotic phenomenon in which a solvent moves from a solution having a low solute concentration toward a high solution between two solutions separated by a semipermeable membrane is called an osmotic phenomenon.
- applying an external pressure higher than osmotic pressure causes the solvent to move toward a solution with a low concentration of solute.
- This phenomenon is called reverse osmosis.
- a pressure gradient can be used as a driving force to separate various salts or organic substances through the semipermeable membrane.
- Reverse osmosis membrane using the reverse osmosis phenomenon is used to separate the material of the molecular level, remove the salt from the brine or sea water to supply the domestic, construction, industrial water.
- reverse osmosis membranes include polyamide reverse osmosis membranes, and polyamide reverse osmosis membranes are manufactured by forming a polyamide active layer on a microporous layer support, and more specifically, A polysulfone layer was formed on the nonwoven fabric to form a microporous support, and the microporous support was immersed in an aqueous solution of m-phenylene diamine (mPD) to form an mPD layer.
- mPD m-phenylene diamine
- TMC TriMesoyl Chloride
- TMC TriMesoyl Chloride
- the present invention is to solve the above problems, to provide a reverse osmosis membrane that can be implemented in a thin, having excellent fouling resistance without deteriorating water purification performance such as salt removal rate, permeate flow rate.
- the present invention is a porous support; A polyamide active layer formed on the porous support; And a copolymer comprising an amphoteric ionic compound and glycidyl (meth) acrylate, and providing a reverse osmosis membrane comprising a coating layer chemically bonded to the polyamide active layer.
- the zwitterionic compound may be a compound represented by the following [Formula 1] or a compound represented by the [Formula 2].
- R 1 is H or a C 1-10 alkyl group, preferably H or a methyl group,
- R 2 is O, NH, S, or PH
- R 3 , R 4 , R 5 , R 6 and R 7 are each independently hydrogen or a C 1-5 alkyl group, preferably a C 1-3 alkyl group, most preferably a methyl group,
- n1 is 1 to 8, preferably 2 to 8,
- n2 is 1-4, preferably 2-4.
- the coating layer may preferably include a copolymer including the zwitterionic compound, glycidyl (meth) acrylate, poly (ethylene glycol) methacrylate, and poly (ethylene glycol) dimethylacrylate. .
- the present invention provides a method for producing a reverse osmosis membrane, comprising treating a porous support on which a polyamide active layer is formed with an aqueous solution containing a copolymer including an amphoteric ionic compound and glycidyl (meth) acrylate.
- the aqueous solution preferably comprises a copolymer in an amount of 0.0001% by weight to 10% by weight, and the treatment may be performed by an immersion method.
- the reverse osmosis membrane of the present invention is equivalent to the conventional reverse osmosis membrane, has excellent water purification function, and has excellent stain resistance.
- the coating layer of the present invention has a chemical bond with the polyamide membrane on the reverse osmosis membrane surface, it is not easily peeled off and is excellent in durability.
- the present inventors have conducted research to develop reverse osmosis membranes excellent in fouling resistance and durability without degrading water purification performance, and as a result, a coating layer containing an amphoteric ionic compound and glycidyl (meth) acrylate on a polyamide active layer
- a coating layer containing an amphoteric ionic compound and glycidyl (meth) acrylate on a polyamide active layer By forming the present invention, it was found that the above object can be achieved, and the present invention was completed.
- the reverse osmosis membrane of the present invention includes (1) a porous support (2) a polyamide active layer and (3) a coating layer.
- polysulfone polysulfone, polyether sulfone, polycarbonate, polyethylene oxide, polyimide, poly Etherimide, polyetheretherketone, polypropylene, polymethylpentene, polymethylchloride and polyvinylidene fluoride may be used, but are not necessarily limited thereto.
- polysulfone is particularly preferable.
- the (2) polyamide active layer may be formed by an interfacial polymer of an amine compound and an acyl halide compound, wherein the amine compound is not limited thereto, for example, m-phenylenediamine, p-phenyl Rendiamine, 1,3,6-benzenetriamine, 4-chloro-1,3-phenylenediamine, 6-chloro-1,3-phenylenediamine, 3-chloro-1,4-phenylene diamine or these It is preferably a mixture of.
- the acyl halide compound is not limited thereto, but is preferably, for example, trimezoyl chloride, isophthaloyl chloride, terephthaloyl chloride or a mixture thereof.
- the (3) coating layer is characterized in that it comprises an amphoteric ionic compound and glycidyl (meth) acrylate.
- the zwitterionic compound is electrically neutral, but includes a cationic charge and an anionic charge in the molecule, to improve the hydrophilicity of the reverse osmosis membrane surface.
- the charge energy present in the zwitterionic compound molecule increases the surface energy of the reverse osmosis membrane, thereby improving hydrophilicity. Since the increased hydrophilicity of the amphoteric ionic compound is significantly higher than that of the polyamide active layer itself, the water permeability of the reverse osmosis membrane is improved, and the adsorption of contaminants, especially organic biomaterials, on the surface of the reverse osmosis membrane is prevented. It has the effect of improving pollution resistance.
- the amphoteric ionic compound usable in the present invention is not particularly limited and may be used without limitation as long as it is a compound containing a cationic charge and an anionic charge in the molecule.
- the cationic charge may include an ammonium group, a phosphonium group, and the like
- the anion charge may include a sulfonic acid group, a phosphate group, an acetate group, and the like.
- amphoteric ionic compound of the present invention may be a compound represented by the following [Formula 1] or a compound represented by [Formula 2].
- R 1 is H or a C 1-10 alkyl group, preferably H or a methyl group,
- R 2 is O, NH, S, or PH
- R 3 , R 4 , R 5 , R 6 and R 7 are each independently hydrogen or a C 1-5 alkyl group, preferably a C 1-3 alkyl group, most preferably a methyl group,
- n1 is 1 to 8, preferably 2 to 8,
- n2 is 1-4, preferably 2-4.
- the zwitterionic compound is not limited thereto, but is not limited thereto, but is [2- (methacryloyloxy) ethyl] -dimethyl- (2-sulfoethyl) -ammonium hydroxide, [2- (meth) Chryloyloxy) ethyl] -dimethyl- (3-sulfopropyl) -ammonium hydroxide, [2- (methacryloyloxy) ethyl] -dimethyl- (4-sulfobutyl) -ammonium hydroxide, [ 2- (methacryloyloxy) ethyl] -dimethyl- (5-sulfopentyl) -ammonium hydroxide, [2- (acryloyloxy) ethyl] -dimethyl- (2-sulfoethyl) -ammonium hydroxide Said, [2- (acryloyloxy) ethyl] -d
- the glycidyl (meth) acrylate is for chemically bonding the polyamide active layer and the coating layer, and may be glycidyl methacrylate or glycidyl acrylate, and more preferably glycidyl methacrylate. desirable.
- the zwitterionic compound and glycidyl (meth) acrylate is preferably included in the form of a copolymer, wherein the copolymer is an initiator containing the zwitterionic compound monomer and glycidyl (meth) acrylate monomer It can form by polymerizing in presence.
- the amphoteric ionic compound and glycidyl (meth) acrylate is preferably reacted in an equivalent ratio of 0.01 to 7: 0.05 to 3.
- the copolymer of the present invention may further include a poly (ethylene glycol) (meth) acrylate compound with the zwitterionic compound and glycidyl (meth) acrylate, the poly (ethylene glycol)
- a poly (ethylene glycol) (meth) acrylate compound with the zwitterionic compound and glycidyl (meth) acrylate the poly (ethylene glycol)
- Poly (ethylene glycol) methyl whose poly (ethylene glycol) methacrylate, poly (ethylene glycol) dimethacrylate, and the number of chains of ethylene glycol are 3-200 Methacrylates and combinations thereof can be used. It is more preferable to use poly (ethylene glycol) methacrylate and poly (ethylene glycol) dimethacrylate together.
- fouling resistance properties can be maximized.
- the coating layer of the present invention will comprise a copolymer comprising an amphoteric ionic compound, glycidyl (meth) acrylate, poly (ethylene glycol) methacrylate, and poly (ethylene glycol) dimethylacrylate.
- an amphoteric ionic compound glycidyl (meth) acrylate, poly (ethylene glycol) methacrylate, and poly (ethylene glycol) dimethylacrylate.
- the copolymer is an amphoteric ionic compound, glycidyl (meth) acrylate, poly (ethylene glycol) methacrylate, and poly (ethylene glycol) dimethyl acrylate 0.1 to 7.5: 0.01 to 5: 0.1 to 5: It is preferable to make it by making it react by the equivalent ratio of 0.01-1.
- the reverse osmosis membrane of the present invention is excellent in preventing bio fouling (bio-fouling) by the organic material.
- the initial salt removal rate is 97% or more, and the initial The flow rate is 25 gallon / ft 2 ⁇ day or more and has the same or superior performance as the conventional reverse osmosis membrane, and the salt removal rate is 97% or more and the flow rate is 23 to 35 gallon / ft 2 It was found that the water purification function did not drop much. That is, the reverse osmosis membrane of the present invention is very excellent in fouling resistance compared to the conventional reverse osmosis membrane.
- the reverse osmosis membrane of the present invention may be prepared by treating a porous support on which a polyamide active layer is formed with an aqueous solution containing a copolymer containing an amphoteric ionic compound and glycidyl (meth) acrylate to form a coating layer. .
- the method of forming the polyamide active layer on the porous support is not particularly limited, and may be performed by a method for preparing a reverse osmosis membrane well known in the art.
- the porous support is immersed in an m-phenylene diamine (mPD) aqueous solution to form an mPD layer, which is then immersed in an organic solvent of trimesoyl chloride (TMC) to form an mPD layer.
- mPD m-phenylene diamine
- TMC trimesoyl chloride
- the polyamide active layer can be formed by interfacial polymerization by contacting with TMC.
- the polyamide active layer may be formed by spraying or coating instead of dipping.
- the step of treating the porous support on which the polyamide active layer is formed with an aqueous solution containing a copolymer containing the zwitterionic compound and glycidyl (meth) acrylate, for example, the porous on which the polyamide active layer is formed It can be carried out by a method of immersing the support in an aqueous solution containing the copolymer.
- the aqueous solution is preferably contained in an amount of 0.0001 to 10% by weight, preferably 0.01 to 5% by weight, most preferably 0.5 to 3% by weight of the copolymer. This is because when the copolymer content in the aqueous solution satisfies the above range, both pollution resistance and water purification performance are excellent.
- the immersion time may be about 1 minute to 5 hours, more preferably about 1 minute to 3 hours. If the immersion time is less than 1 minute, the coating layer is not formed sufficiently, if the immersion time exceeds 5 hours, the coating layer thickness is too thick, there is a negative effect that the permeate flow rate of the reverse osmosis membrane is reduced.
- the coating layer is formed on the polyamide active layer through the immersion treatment, it is preferable to perform a step of drying for about 1 to 30 minutes at about 25 to 65 °C to improve the adhesion between the coating layer and the polyamide active layer.
- amphoteric ionic compound usable in the present invention is not particularly limited, but preferably, may be a compound represented by the following [Formula 1] or a compound represented by [Formula 2].
- R 1 is H or a C 1-10 alkyl group, preferably H or a methyl group,
- R 2 is O, NH, S, or PH
- R 3 , R 4 , R 5 , R 6 and R 7 are each independently hydrogen or a C 1-5 alkyl group, preferably a C 1-3 alkyl group, most preferably a methyl group,
- n1 is 1 to 8, preferably 2 to 8,
- n2 is 1-4, preferably 2-4.
- the zwitterionic compounds include, but are not limited to, [2- (methacryloyloxy) ethyl] -dimethyl- (2-sulfoethyl) -ammonium hydroxide, [2- (methacryloyl jade) Ethyl] -dimethyl- (3-sulfopropyl) -ammonium hydroxide, [2- (methacryloyloxy) ethyl] -dimethyl- (4-sulfobutyl) -ammonium hydroxide, [2- ( Methacryloyloxy) ethyl] -dimethyl- (5-sulfopentyl) -ammonium hydroxide, [2- (acryloyloxy) ethyl] -dimethyl- (2-sulfoethyl) -ammonium hydroxide, [ 2- (acryloyloxy) ethyl] -dimethyl- (3-sulfo)
- the copolymer of the amphoteric ionic compound and glycidyl (meth) acrylate can be formed by polymerizing the amphoteric ionic compound monomer and glycidyl (meth) acrylate monomer in the presence of an initiator, In this case, the amphoteric ionic compound and glycidyl (meth) acrylate may be reacted in an equivalent ratio of 0.01 to 7: 0.05 to 3.
- the copolymer may further include a poly (ethylene glycol) (meth) acrylate-based compound together with the zwitterionic compound and glycidyl (meth) acrylate, and the poly (ethylene glycol) (meth)
- the acrylate compound poly (ethylene glycol) methacrylate, poly (ethylene glycol) dimethacrylate, poly (ethylene glycol) methyl ether methacrylate and combinations thereof may be used, but not limited thereto. It is more preferable to use poly (ethylene glycol) methacrylate and poly (ethylene glycol) dimethacrylate together.
- fouling resistance properties can be maximized.
- the copolymer comprises the zwitterionic compound, glycidyl (meth) acrylate, poly (ethylene glycol) methacrylate, and poly (ethylene glycol) dimethylacrylate.
- the amphoteric ionic compound, glycidyl (meth) acrylate, poly (ethylene glycol) methacrylate, and poly (ethylene glycol) dimethyl acrylate are equivalent ratios of 0.1 to 7.5: 0.01 to 5: 0.1 to 5: 0.01 to 1, and may further include a step of preparing a copolymer by a polymerization reaction.
- the polymerization reaction is preferably performed for 0.1 to 10 hours at 40 ⁇ 80 °C.
- the type of the polymerization reaction is not particularly limited, and may be, for example, radical polymerization.
- the copolymer formed as a result of the polymerization reaction is a random copolymer, and after manufacture, the copolymer is preferably stored at a temperature of 0 ° C. or lower, and in use, it is preferable to use it immediately after thawing at room temperature. This is to suppress the reactivity of the glycidyl functional group included in the copolymer, and when the copolymer is stored at room temperature, the glycidyl reactor is easily hydrolyzed by moisture, and in this case, chemical bondability with the polyamide active layer This can fall.
- porous polysulfone support prepared by the above method was soaked for 2 minutes in an aqueous solution containing 2% by weight of metaphenylenediamine, and then the excess aqueous solution on the support was removed using a 25 psi roller and dried at room temperature for 1 minute. .
- the support was immersed in an organic solution of 0.1% by weight of trimezoyl chloride using ISOL-C (SK Chem) solvent for 1 minute, then taken out, and dried in an oven at 60 ° C for 10 minutes. Then, after washing with 0.2% by weight aqueous solution of sodium carbonate at room temperature for 2 hours or more, washed with distilled water to prepare a porous support having a polyamide active layer of 200nm thickness.
- ISOL-C SK Chem
- PGMA is polyglycidyl methacrylate
- PMPDSAH is poly ((3-methacryloylamino) propyl) -dimethyl (3-sulfopropyl) -ammonium hydroxide
- PEGMA is poly (ethylene glycol)
- PEGDMA means poly (ethylene glycol) dimethylacrylate
- the copolymer was prepared by reacting PMPDSAH: PGMA: PEGMA: PEGDMA in an equivalent ratio of 5: 2: 3.9: 0.1.
- a coating layer was formed in the same manner as in Example 1 except that the copolymer content in the aqueous solution was 0.5% by weight.
- a coating layer was formed in the same manner as in Example 1 except that the content of the copolymer in the aqueous solution was 1% by weight.
- a coating layer was formed in the same manner as in Example 1 except that the copolymer content in the aqueous solution was 3% by weight.
- porous support having the polyamide active layer prepared in Preparation Example 1 was washed with distilled water and then used as it was without any surface treatment.
- PGMA is polyglycidyl methacrylate
- PMPDSAH is poly ((3-methacryloylamino) propyl) -dimethyl (3-sulfopropyl) -ammonium hydroxide
- the copolymer is PMPDSAH :
- PGMA was prepared by reacting with an equivalent ratio of 7: 2.
- a coating layer was formed in the same manner as in Example 5 except that the copolymer content in the aqueous solution was 0.5% by weight.
- a coating layer was formed in the same manner as in Example 5, except that the copolymer content in the aqueous solution was 1% by weight.
- a coating layer was formed in the same manner as in Example 5, except that the copolymer content in the aqueous solution was 3% by weight.
- PGMA is polyglycidyl methacrylate
- PMPTPP is poly 3- (methacryloyloxy) propyl 3- (trimethylammonio) propyl phosphate
- PEGMA is poly (ethylene glycol) methacrylate
- PEGDMA Means poly (ethylene glycol) dimethylacrylate
- the copolymer was prepared by reacting PMPTPP: PGMA: PEGMA: PEGDMA in an equivalent ratio of 5: 2: 3.9: 0.1.
- a coating layer was formed in the same manner as in Example 9, except that the copolymer content in the aqueous solution was 0.5% by weight.
- a coating layer was formed in the same manner as in Example 9, except that the copolymer content in the aqueous solution was 1% by weight.
- a coating layer was formed in the same manner as in Example 9 except that the copolymer content in the aqueous solution was 3% by weight.
- PGMA refers to polyglycidyl methacrylate
- PMPTPP refers to poly 3- (methacryloyloxy) propyl 3- (trimethylammonio) propyl phosphate
- the copolymer refers to PMPTPP: PGMA 7: 2 It was prepared by reacting with an equivalent ratio of.
- a coating layer was formed in the same manner as in Example 13, except that the copolymer content in the aqueous solution was 0.5% by weight.
- a coating layer was formed in the same manner as in Example 13, except that the copolymer content in the aqueous solution was 1% by weight.
- a coating layer was formed in the same manner as in Example 13 except that the copolymer content in the aqueous solution was 3% by weight.
- the initial salt rejection rate and initial permeation flux of the reverse osmosis membranes prepared by Examples 1 to 16 and Comparative Examples were measured.
- the initial salt excretion rate and initial permeate flow rate were measured while supplying a 32,000 ppm sodium chloride aqueous solution at 25 ° C. at a flow rate of 1400 mL / min.
- the reverse osmosis membrane cell apparatus used for the membrane evaluation was equipped with a flat plate permeation cell, a high pressure pump, a storage tank, and a cooling device.
- the structure of the flat plate permeation cell was 140 cm 2 in a cross-flow method.
- the stain resistance of the reverse osmosis membranes prepared by Examples 1 to 16 and Comparative Examples was evaluated.
- the stain resistance was measured at a pressure of 800 psi using a 32,000 ppm NaCl aqueous solution and a 100 ppm casein mixed aqueous solution.
- 100 ppm of casein aqueous solution was added to the evaluator tank and the change in salt rejection rate and flow rate was measured immediately. Then, after 2 hours, the change in salt excretion rate and flow rate was measured.
- Casein was dissolved in an aqueous solution of pH 11 or higher. The measurement results are shown in [Table 2].
- Example 1 27.24 23.42 97.81 98.21
- Example 2 30.08 29.88 98.54 99.34
- Example 3 28.94 27.74 98.43 99.09
- Example 4 28.14 26.97 98.64 98.89
- Example 5 27.13 23.54 97.77 98.13
- Example 6 29.32 29.00 98.64 99.19
- Example 7 28.75 27.98 98.51 99.01
- Example 8 28.34 26.99 98.72 98.85
- Example 9 27.38 23.37 97.82 98.19
- Example 10 29.45 29.89 98.58 99.05
- Example 11 28.30 27.70 98.60 99.02
- Example 12 28.08 26.89 98.57 98.91
- Example 13 27.09 23.31 97.88 98.05
- Example 14 29.88 29.34 98.44 99.14
- Example 15 28.
- the fouling resistance of the reverse osmosis membrane prepared in Example 2 was measured at a pressure of 800 psi using a 32,000 ppm NaCl aqueous solution and a 300 ppm casein mixed aqueous solution. The results are shown in [Table 3].
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Abstract
Description
| 초기 염배제율(%) | 초기 투과유량(gallon/ft2·day) | |
| 실시예 1 | 97.94 | 27.94 |
| 실시예 2 | 98.78 | 29.97 |
| 실시예 3 | 98.54 | 29.63 |
| 실시예 4 | 98.23 | 29.31 |
| 실시예 5 | 97.84 | 27.99 |
| 실시예 6 | 98.59 | 29.72 |
| 실시예 7 | 98.43 | 29.21 |
| 실시예 8 | 98.31 | 29.09 |
| 실시예 9 | 97.75 | 27.98 |
| 실시예 10 | 98.17 | 29.46 |
| 실시예 11 | 98.23 | 29.32 |
| 실시예 12 | 98.31 | 29.25 |
| 실시예 13 | 97.91 | 27.99 |
| 실시예 14 | 98.23 | 29.48 |
| 실시예 15 | 98.28 | 29.17 |
| 실시예 16 | 98.32 | 28.87 |
| 비교예 | 97.79 | 27.96 |
| 카제인 투입 직후 초기유량 | 카제인 투입 2시간 후 초기 유량 | 카제인 투입 직후 염 제거율 | 카제인 투입 2시간 후 염 제거율 | |
| 실시예 1 | 27.24 | 23.42 | 97.81 | 98.21 |
| 실시예 2 | 30.08 | 29.88 | 98.54 | 99.34 |
| 실시예 3 | 28.94 | 27.74 | 98.43 | 99.09 |
| 실시예 4 | 28.14 | 26.97 | 98.64 | 98.89 |
| 실시예 5 | 27.13 | 23.54 | 97.77 | 98.13 |
| 실시예 6 | 29.32 | 29.00 | 98.64 | 99.19 |
| 실시예 7 | 28.75 | 27.98 | 98.51 | 99.01 |
| 실시예 8 | 28.34 | 26.99 | 98.72 | 98.85 |
| 실시예 9 | 27.38 | 23.37 | 97.82 | 98.19 |
| 실시예 10 | 29.45 | 29.89 | 98.58 | 99.05 |
| 실시예 11 | 28.30 | 27.70 | 98.60 | 99.02 |
| 실시예 12 | 28.08 | 26.89 | 98.57 | 98.91 |
| 실시예 13 | 27.09 | 23.31 | 97.88 | 98.05 |
| 실시예 14 | 29.88 | 29.34 | 98.44 | 99.14 |
| 실시예 15 | 28.68 | 27.44 | 98.47 | 99.04 |
| 실시예 16 | 28.11 | 26.86 | 98.60 | 98.91 |
| 비교예 | 26.98 | 22.93 | 97.41 | 98.18 |
| 카제인 투입 직후 초기유량 | 카제인 투입 2시간 후 초기 유량 | 카제인 투입 직후 염 제거율 | 카제인 투입 2시간 후 염 제거율 | |
| 실시예 2 | 31.12 | 29.12 | 98.44 | 99.28 |
| 비교예 | 26.28 | 22.03 | 97.32 | 98.07 |
Claims (16)
- 다공성 지지체;상기 다공성 지지체 상에 형성되는 폴리아미드 활성층; 및양쪽성 이온 화합물 및 글리시딜 (메트)아크릴레이트를 포함하는 공중합체를 포함하며, 상기 폴리아미드 활성층과 화학적으로 결합된 코팅층을 포함하는 역삼투막.
- 제1항에 있어서,상기 양쪽성 이온 화합물은 [2-(메타크릴로일옥시)에틸]-디메틸-(2-술포에틸)-암모늄 하이드록사이드, [2-(메타크릴로일옥시)에틸]-디메틸-(3-술포프로필)-암모늄 하이드록사이드, [2-(메타크릴로일옥시)에틸]-디메틸-(4-술포부틸)-암모늄 하이드록사이드, [2-(메타크릴로일옥시)에틸]-디메틸-(5-술포펜틸)-암모늄 하이드록사이드, [2-(아크릴로일옥시)에틸]-디메틸-(2-술포에틸)-암모늄 하이드록사이드, [2-(아크릴로일옥시)에틸]-디메틸-(3-술포프로필)-암모늄 하이드록사이드, [2-(아크릴로일옥시)에틸]-디메틸-(4-술포부틸)-암모늄 하이드록사이드, [2-(아크릴로일옥시)에틸]-디메틸-(5-술포펜틸)-암모늄 하이드록사이드, [3-(메타크릴로일옥시)프로필]-디메틸-(2-술포에틸)-암모늄 하이드록사이드, [3-(메타크릴로일옥시)프로필]-디메틸-(3-술포프로필)-암모늄 하이드록사이드, [3-(메타크릴로일옥시)프로필]-디메틸-(4-술포부틸)-암모늄 하이드록사이드, [3-(메타크릴로일옥시)프로필]-디메틸-(5-술포펜틸)-암모늄 하이드록사이드, [3-(아크릴로일옥시)프로필]-디메틸-(2-술포에틸)-암모늄 하이드록사이드, [3-(아크릴로일옥시)프로필]-디메틸-(3-술포프로필)-암모늄 하이드록사이드, [3-(아크릴로일옥시)프로필]-디메틸-(4-술포부틸)-암모늄 하이드록사이드, [3-(아크릴로일옥시)프로필]-디메틸-(5-술포펜틸)-암모늄 하이드록사이드, [4-(메타크릴로일옥시)부틸]-디메틸-(2-술포에틸)-암모늄 하이드록사이드, [4-(메타크릴로일옥시)부틸]-디메틸-(3-술포프로필)-암모늄 하이드록사이드, [4-(메타크릴로일옥시)부틸]-디메틸-(4-술포부틸)-암모늄 하이드록사이드, [4-(메타크릴로일옥시)부틸]-디메틸-(5-술포펜틸)-암모늄 하이드록사이드, [4-(메타크릴로일옥시)부틸]-디메틸-(6-술포헥실)-암모늄 하이드록사이드, [4-(아크릴로일옥시)부틸]-디메틸-(2-술포에틸)-암모늄 하이드록사이드, [4-(아크릴로일옥시)부틸]-디메틸-(3-술포프로필)-암모늄 하이드록사이드, [4-(아크릴로일옥시)부틸]-디메틸-(4-술포부틸)-암모늄 하이드록사이드, [4-(아크릴로일옥시)부틸]-디메틸-(5-술포펜틸)-암모늄 하이드록사이드, [4-(아크릴로일옥시)부틸]-디메틸-(6-술포헥실)-암모늄 하이드록사이드, [2-(메타크릴로일아미노)에틸]-디메틸-(2-술포에틸)-암모늄 하이드록사이드, [2-(메타크릴로일아미노)에틸]-디메틸-(3-술포프로필)-암모늄 하이드록사이드, [2-(메타크릴로일아미노)에틸]-디메틸-(4-술포부틸)-암모늄 하이드록사이드, [2-(메타크릴로일아미노)에틸]-디메틸-(5-술포펜틸)-암모늄 하이드록사이드, [2-(아크릴로일아미노)에틸]-디메틸-(2-술포에틸)-암모늄 하이드록사이드, [2-(아크릴로일아미노)에틸]-디메틸-(3-술포프로필)-암모늄 하이드록사이드, [2-(아크릴로일아미노)에틸]-디메틸-(4-술포부틸)-암모늄 하이드록사이드, [2-(아크릴로일아미노)에틸]-디메틸-(5-술포펜틸)-암모늄 하이드록사이드, [3-(메타크릴로일아미노)프로필]-디메틸-(2-술포에틸)-암모늄 하이드록사이드, [3-(메타크릴로일아미노)프로필]-디메틸-(3-술포프로필)-암모늄 하이드록사이드, [3-(메타크릴로일아미노)프로필]-디메틸-(4-술포부틸)-암모늄 하이드록사이드, [3-(메타크릴로일아미노)프로필]-디메틸-(5-술포펜틸)-암모늄 하이드록사이드, [3-(아크릴로일아미노)프로필]-디메틸-(2-술포에틸)-암모늄 하이드록사이드, [3-(아크릴로일아미노)프로필]-디메틸-(3-술포프로필)-암모늄 하이드록사이드, [3-(아크릴로일아미노)프로필]-디메틸-(4-술포부틸)-암모늄 하이드록사이드, [3-(아크릴로일아미노)프로필]-디메틸-(5-술포펜틸)-암모늄 하이드록사이드, [4-(메타크릴로일아미노)부틸]-디메틸-(2-술포에틸)-암모늄 하이드록사이드, [4-(메타크릴로일아미노)부틸]-디메틸-(3-술포프로필)-암모늄 하이드록사이드, [4-(메타크릴로일아미노)부틸]-디메틸-(4-술포부틸)-암모늄 하이드록사이드, [4-(메타크릴로일아미노)부틸]-디메틸-(5-술포펜틸)-암모늄 하이드록사이드, [4-(메타크릴로일아미노)부틸]-디메틸-(6-술포헥실)-암모늄 하이드록사이드, [4-(아크릴로일아미노)부틸]-디메틸-(2-술포에틸)-암모늄 하이드록사이드, [4-(아크릴로일아미노)부틸]-디메틸-(3-술포프로필)-암모늄 하이드록사이드, [4-(아크릴로일아미노)부틸]-디메틸-(4-술포부틸)-암모늄 하이드록사이드, [4-(아크릴로일아미노)부틸]-디메틸-(5-술포펜틸)-암모늄 하이드록사이드, [4-(아크릴로일아미노)부틸]-디메틸-(6-술포헥실)-암모늄 하이드록사이드, 2-(메타크릴로일옥시)에틸 2-(트리메틸암모니오)에틸 포스페이트, 3-(메타크릴로일옥시)프로필 2-(트리메틸암모니오)에틸 포스페이트, 4-(메타크릴로일옥시)부틸 2-(트리메틸암모니오)에틸 포스페이트, 5-(메타크릴로일옥시)펜틸 2-(트리메틸암모니오)에틸 포스페이트, 6-(메타크릴로일옥시)헥실 2-(트리메틸암모니오)에틸 포스페이트, 7-(메타크릴로일옥시)헵틸 2-(트리메틸암모니오)에틸 포스페이트, 8-(메타크릴로일옥시)옥틸2-(트리메틸암모니오)에틸 포스페이트, 2-(메타크릴로일아미노)에틸 2-(트리메틸암모니오)에틸 포스페이트, 3-(메타크릴로일아미노)프로필 2-(트리메틸암모니오)에틸 포스페이트, 4-(메타크릴로일아미노)부틸 2-(트리메틸암모니오)에틸 포스페이트, 5-(메타크릴로일아미노)펜틸 2-(트리메틸암모니오)에틸 포스페이트, 6-(메타크릴로일아미노)헥실 2-(트리메틸암모니오)에틸 포스페이트, 7-(메타크릴로일아미노)헵틸 2-(트리메틸암모니오)에틸 포스페이트, 8-(메타크릴로일아미노)옥틸 2-(트리메틸암모니오)에틸 포스페이트, 2-(아크릴로일옥시)에틸 2-(트리메틸암모니오)에틸 포스페이트, 3-(아크릴로일옥시)프로필 2-(트리메틸암모니오)에틸 포스페이트, 4-(아크릴로일옥시)부틸 2-(트리메틸암모니오)에틸 포스페이트, 5-(아크릴로일옥시)펜틸 2-(트리메틸암모니오)에틸 포스페이트, 6-(아크릴로일옥시)헥실 2-(트리메틸암모니오)에틸 포스페이트, 7-(아크릴로일옥시)헵틸 2-(트리메틸암모니오)에틸 포스페이트, 8-(아크릴로일옥시)옥틸 2-(트리메틸암모니오)에틸 포스페이트, 2-(메타크릴로일옥시)에틸 3-(트리메틸암모니오)프로필 포스페이트, 3-(메타크릴로일옥시)프로필 3-(트리메틸암모니오)프로필 포스페이트, 4-(메타크릴로일옥시)부틸 3-(트리메틸암모니오)프로필 포스페이트, 5-(메타크릴로일옥시)펜틸 3-(트리메틸암모니오)프로필 포스페이트, 6-(메타크릴로일옥시)헥실 3-(트리메틸암모니오)프로필 포스페이트, 7-(메타크릴로일옥시)헵틸 3-(트리메틸암모니오)프로필 포스페이트, 8-(메타크릴로일옥시)옥틸 3-(트리메틸암모니오)프로필 포스페이트, 2-(메타크릴로일아미노)에틸 3-(트리메틸암모니오)프로필 포스페이트, 3-(메타크릴로일아미노)프로필 3-(트리메틸암모니오)프로필 포스페이트, 4-(메타크릴로일아미노)부틸 3-(트리메틸암모니오)프로필 포스페이트, 5-(메타크릴로일아미노)펜틸 3-(트리메틸암모니오)프로필 포스페이트, 6-(메타크릴로일아미노)헥실 3-(트리메틸암모니오)프로필 포스페이트, 7-(메타크릴로일아미노)헵틸 3-(트리메틸암모니오)프로필 포스페이트, 8-(메타크릴로일아미노)옥틸 3-(트리메틸암모니오)프로필 포스페이트, 2-(아크릴로일옥시)에틸 3-(트리메틸암모니오)프로필 포스페이트, 3-(아크릴로일옥시)프로필 3-(트리메틸암모니오)프로필 포스페이트, 4-(아크릴로일옥시)부틸 3-(트리메틸암모니오)프로필 포스페이트, 5-(아크릴로일옥시)펜틸 3-(트리메틸암모니오)프로필 포스페이트, 6-(아크릴로일옥시)헥실 3-(트리메틸암모니오)프로필 포스페이트, 7-(아크릴로일옥시)헵틸 3-(트리메틸암모니오)프로필 포스페이트, 8-(아크릴로일옥시)옥틸 3-(트리메틸암모니오)프로필 포스페이트, 2-(메타크릴로일옥시)에틸 4-(트리메틸암모니오)부틸 포스페이트, 3-(메타크릴로일옥시)프로필 4-(트리메틸암모니오)부틸 포스페이트, 4-(메타크릴로일옥시)부틸 4-(트리메틸암모니오)부틸 포스페이트, 5-(메타크릴로일옥시)펜틸 4-(트리메틸암모니오)부틸 포스페이트, 6-(메타크릴로일옥시)헥실 4-(트리메틸암모니오)부틸 포스페이트, 7-(메타크릴로일옥시)헵틸 4-(트리메틸암모니오)부틸 포스페이트, 8-(메타크릴로일옥시)옥틸 4-(트리메틸암모니오)부틸 포스페이트, 2-(메타크릴로일아미노)에틸 4-(트리메틸암모니오)부틸 포스페이트, 3-(메타크릴로일아미노)프로필 4-(트리메틸암모니오)부틸 포스페이트, 4-(메타크릴로일아미노)부틸 4-(트리메틸암모니오)부틸 포스페이트, 5-(메타크릴로일아미노)펜틸 4-(트리메틸암모니오)부틸 포스페이트, 6-(메타크릴로일아미노)헥실 4-(트리메틸암모니오)부틸 포스페이트, 7-(메타크릴로일아미노)헵틸 4-(트리메틸암모니오)부틸 포스페이트, 8-(메타크릴로일아미노)옥틸 4-(트리메틸암모니오)부틸 포스페이트, 2-(아크릴로일옥시)에틸 4-(트리메틸암모니오)부틸 포스페이트, 3-(아크릴로일옥시)프로필 4-(트리메틸암모니오)부틸 포스페이트, 4-(아크릴로일옥시)부틸 4-(트리메틸암모니오)부틸 포스페이트, 5-(아크릴로일옥시)펜틸 4-(트리메틸암모니오)부틸 포스페이트, 6-(아크릴로일옥시)헥실 4-(트리메틸암모니오)부틸 포스페이트, 7-(아크릴로일옥시)헵틸 4-(트리메틸암모니오)부틸 포스페이트, 및 8-(아크릴로일옥시)옥틸 4-(트리메틸암모니오)부틸 포스페이트로 이루어진 군으로부터 선택되는 1종 이상을 포함하는 역삼투막.
- 제1항에 있어서,상기 공중합체는 양쪽성 이온 화합물과 글리시딜 (메트)아크릴레이트를 0.01 ~ 7 : 0.05 ~ 3 의 당량비로 반응시켜 제조된 것인 역삼투막.
- 제1항에 있어서,상기 공중합체는 에틸렌 글리콜 (메트)아크릴레이트계 화합물을 더 포함하는 것인 역삼투막.
- 제5항에 있어서,상기 에틸렌 글리콜 (메트)아크릴레이트계 화합물은 폴리에틸렌 글리콜 메타크릴레이트, 폴리에틸렌 글리콜 디메타크릴레이트 및 폴리 (에틸렌글리콜) 메틸 이써 메타크릴레이트로부터 선택된 1종 이상인 역삼투막.
- 제1항에 있어서,상기 코팅층은 양쪽성 이온 화합물, 글리시딜 (메트)아크릴레이트, 폴리(에틸렌 글리콜) 메타크릴레이트 및 폴리(에틸렌 글리콜) 디메틸아크릴레이트를 포함하는 공중합체를 포함하는 역삼투막.
- 제6항에 있어서,상기 공중합체는 양쪽성 이온 화합물, 글리시딜 (메트)아크릴레이트, 폴리(에틸렌 글리콜) 메타크릴레이트 및 폴리(에틸렌 글리콜) 디메틸아크릴레이트를 0.1~7.5 : 0.01~5 : 0.1~5 : 0.01~1의 당량비로 반응시켜 제조된 것인 역삼투막.
- 제1항 내지 제8항 중 어느 한 항에 있어서,상기 역삼투막은 카제인 투입 2시간 경과 후의 염제거율이 97% 이상이고, 투과 유량이 23 내지 35gallon/ft2·day 인 역삼투막.
- 폴리아미드 활성층이 형성된 다공성 지지체를 양쪽성 이온 화합물 및 글리시딜 (메트)아크릴레이트를 포함하는 공중합체를 함유하는 수용액으로 처리하여 코팅층을 형성하는 단계를 포함하는 역삼투막 제조 방법.
- 제10항에 있어서,상기 수용액은 상기 공중합체를 0.0001 중량% 내지 10 중량%의 함량으로 포함하는 역삼투막 제조 방법.
- 제10항에 있어서,상기 처리는 침지법에 의해 수행되는 역삼투막 제조 방법.
- 제12항에 있어서,상기 침지는 1분 내지 5시간 동안 수행되는 역삼투막 제조 방법.
- 제10항에 있어서,상기 공중합체는 폴리(에틸렌 글리콜) 메타크릴레이트 및 폴리(에틸렌 글리콜) 디메틸아크릴레이트 중 적어도 하나를 추가로 포함하는 것인 역삼투막 제조 방법.
- 제10항에 있어서,상기 양쪽성 이온 화합물, 글리시딜 (메트)아크릴레이트, 폴리(에틸렌 글리콜) 메타크릴레이트, 및 폴리(에틸렌 글리콜) 디메틸아크릴레이트를 0.1~7.5 : 0.01~ 5 : 0.1~5 : 0.01~1의 당량비로 혼합한 후 중합시켜 공중합체를 제조하는 단계를 더 포함하는 역삼투막 제조 방법.
- 제10항에 있어서,상기 코팅층을 형성하는 단계 이후에 25 내지 65℃에서 1 내지 30 분 동안 건조시키는 단계를 추가로 포함하는 역삼투막 제조 방법.
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| CN201380000815.3A CN103402616B (zh) | 2012-01-05 | 2013-01-04 | 具有良好防污性的反渗透膜及其制造方法 |
| ES13733795T ES2715317T3 (es) | 2012-01-05 | 2013-01-04 | Membrana de osmosis inversa excepcionalmente resistente a la contaminación y método para su producción |
| JP2013552482A JP5863127B2 (ja) | 2012-01-05 | 2013-01-04 | 耐汚染性に優れた逆浸透膜及びその製造方法 |
| EP13733795.2A EP2801401B1 (en) | 2012-01-05 | 2013-01-04 | Outstandingly contamination resistant reverse osmosis membrane and production method therefor |
| US13/951,239 US8646617B2 (en) | 2012-01-05 | 2013-07-25 | Reverse osmosis membrane having good antifouling properties and method of manufacturing the same |
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| KR10-2012-0001513 | 2012-01-05 | ||
| KR20120001513 | 2012-01-05 | ||
| KR1020130000696A KR101440971B1 (ko) | 2012-01-05 | 2013-01-03 | 내오염성이 우수한 역삼투막 및 그 제조방법 |
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| US13/951,239 Continuation US8646617B2 (en) | 2012-01-05 | 2013-07-25 | Reverse osmosis membrane having good antifouling properties and method of manufacturing the same |
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| US (1) | US8646617B2 (ko) |
| EP (1) | EP2801401B1 (ko) |
| JP (1) | JP5863127B2 (ko) |
| KR (1) | KR101440971B1 (ko) |
| CN (1) | CN103402616B (ko) |
| ES (1) | ES2715317T3 (ko) |
| WO (1) | WO2013103257A1 (ko) |
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| DE102014224473A1 (de) * | 2014-11-29 | 2016-06-02 | Leibniz-Institut Für Polymerforschung Dresden E.V. | Umkehrosmose- oder Nanofiltrations-Membranen und Verfahren zu ihrer Herstellung |
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| KR102537506B1 (ko) * | 2016-06-15 | 2023-05-30 | 한국과학기술원 | 이온가교된 고분자를 이용한 수처리용 분리막의 제조방법 |
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Also Published As
| Publication number | Publication date |
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| US20130306550A1 (en) | 2013-11-21 |
| KR101440971B1 (ko) | 2014-09-17 |
| JP2014510621A (ja) | 2014-05-01 |
| ES2715317T3 (es) | 2019-06-03 |
| EP2801401B1 (en) | 2018-12-12 |
| KR20130080808A (ko) | 2013-07-15 |
| EP2801401A1 (en) | 2014-11-12 |
| US8646617B2 (en) | 2014-02-11 |
| EP2801401A4 (en) | 2015-08-26 |
| CN103402616B (zh) | 2016-05-04 |
| JP5863127B2 (ja) | 2016-02-16 |
| CN103402616A (zh) | 2013-11-20 |
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