WO2010062016A2 - Membrane composite à base de polyamide résistant à l'encrassement et au chlore, et procédé de préparation associé - Google Patents

Membrane composite à base de polyamide résistant à l'encrassement et au chlore, et procédé de préparation associé Download PDF

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Publication number
WO2010062016A2
WO2010062016A2 PCT/KR2009/001762 KR2009001762W WO2010062016A2 WO 2010062016 A2 WO2010062016 A2 WO 2010062016A2 KR 2009001762 W KR2009001762 W KR 2009001762W WO 2010062016 A2 WO2010062016 A2 WO 2010062016A2
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Prior art keywords
silane
epoxypropoxy
polyamide
composite membrane
membrane
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PCT/KR2009/001762
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English (en)
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WO2010062016A3 (fr
Inventor
Yong Taek Lee
No Won Kim
Dong Ho Shin
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University-Industry Cooperation Group Of Kyung Hee University
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Publication of WO2010062016A2 publication Critical patent/WO2010062016A2/fr
Publication of WO2010062016A3 publication Critical patent/WO2010062016A3/fr

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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
    • 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
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
    • B01D67/0081—After-treatment of organic or inorganic membranes
    • B01D67/0088—Physical treatment with compounds, e.g. swelling, coating or impregnation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
    • B01D69/02—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
    • B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • 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
    • B01D2323/00—Details relating to membrane preparation
    • B01D2323/30—Cross-linking
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2325/00—Details relating to properties of membranes
    • B01D2325/30—Chemical resistance

Definitions

  • the present invention relates to a polyamide composite membrane and a method for preparing the same. Specifically, the present invention relates to a polyamide composite membrane having both fouling resistance and chlorine resistance at the same time, and a method for preparing the same.
  • dissolved substances can be separated from their solvents by use of selective membranes.
  • membranes such as microfiltration membranes, ultrafiltration membranes, nanofiltration membranes, reverse osmosis membranes and the like.
  • the reverse osmosis membranes are particularly useful in the desalination of brackish water or sea water.
  • the desalination process of brackish water or sea water using reverse osmosis membranes involves a filtration process for separation by applying pressure to the feed water and forcing the water through the membrane, so that purified water passes through the membrane and the salts or other dissolved substances or molecules are filtered out.
  • osmotic pressure naturally occurs, and the more concentrated the feed water, the greater the osmotic pressure, which requires higher pressure applied from outside.
  • Tap water should be treated by chlorination for sterilization.
  • Water for industrial use or desalinated water from sea water should also be treated with chlorine so as to prevent water from being contaminated by bacteria present on a reverse osmosis membrane, and then undergone a dechlorination process.
  • Such dechlorination is generally done by use of activated charcoal or chemical agents, thus having many difficulties in their maintenance.
  • Reverse osmosis membranes prepared from a porous supporting layer and a polyamide membrane formed on said supporting layer have been widely used.
  • the polyamide membrane can be obtained by interfacial polymerization between polyfunctional amines and polyfunctional acyl halides.
  • US patent No. 5,614,099 issued to Hirose discloses a technique of adjusting a polyamide surface structure.
  • the invention is to provide a process for preparing a membrane having at least a certain degree of surface roughness, from the finding that the surface roughness is closely related to a flow rate increase, based on the Tomashke's membrane preparation method.
  • the present inventors have continued researches to develop polyamide membranes having greater resistance to both chlorine and fouling, and excellent permeation performance. As a result, the present inventors have developed a method for preparing a polyamide composite membrane having both satisfying chlorine resistance and fouling resistance by coating or crosslinking the surface of a polyamide membrane with epoxy-silane compounds.
  • the present invention is to provide a method for preparing a polyamide composite membrane having both fouling resistance and chlorine resistance at the same time, by coating or crosslinking the polyamide membrane surface with epoxy-silane compounds.
  • the present invention is to provide a polyamide composite membrane having improved chlorine resistance and fouling resistance prepared by said method.
  • the present invention is to provide a polyamide composite membrane having excellent permeability.
  • the present invention is to provide a method for preparing a polyamide composite membrane through a simplified and economical process.
  • the present invention provides a method for preparing a polyamide composite membrane, characterized by comprising the steps of: forming a polyamide thin film on a porous supporting layer; coating or crosslinking the polyamide thin film surface with a solution of epoxy-silane compounds and drying the resulted membrane; and washing the dried membrane with a basic aqueous solution.
  • the epoxy-silane compounds may be at least one selected from the group consisting of [2,3-epoxypropoxy)alkyl]trialkoxy silane represented by the following chemistry figure 1, glycidylalkyltrialkoxy silane represented by the following chemistry figure 2 and mixtures thereof:
  • R is C1 ⁇ C4 alkylene group, and R' is C1 ⁇ C4 alkyl group.
  • the [2,3-epoxypropoxy)alkyl]trialkoxy silane may be at least one selected from the group consisting of [(2,3-epoxypropoxy)methyl]trimethoxy silane, [(2,3-epoxypropoxy)methyl]triethoxy silane, [(2,3-epoxypropoxy)methyl]tripropoxy silane, [(2,3-epoxypropoxy)methyl]tributoxy silane, [2-(2,3-epoxypropoxy)ethyl]trimethoxy silane, [2-(2,3-epoxypropoxy)ethyl]triethoxy silane, [2-(2,3-epoxypropoxy)ethyl]tripropoxy silane, [2-(2,3-epoxypropoxy)ethyl]tributoxy silane, [3-(2,3-epoxypropoxy)propyl]trimethoxy silane, [3-(2,3-epoxypropoxy)propyl]triethoxy silane, [
  • the glycidylalkyltrialkoxy silane may be at least one selected from the group consisting of glycidylmethyltrimethoxy silane, glycidylmethyltriethoxy silane, 2-glycidylethyltrimethoxy silane, 2-glycidylethyltriethoxy silane, 3-glycidylpropyltrimethoxy silane, 3-glycidylpropyltriethoxy silane, 3-glycidylpropyltri(methoxyethoxy silane) and mixtures thereof.
  • the concentration of said epoxy-silane compounds may be 0.1 ⁇ 5 wt%.
  • the method further includes, after coating or crosslinking the polyamide thin film surface with an epoxy-silane compound solution, a step of drying the resulted membrane with hot air at the temperature range of 25 ⁇ 100°C.
  • the present invention provides a polyamide composite membrane prepared by the foregoing method.
  • a polyamide composite membrane is provided, which is comprised of: a porous supporting layer; a polyamide composite membrane formed on the porous supporting layer; and an epoxy-silane compound layer coated or crosslinked on the polyamide composite surface.
  • the polyamide composite membrane according to the method of the present invention exhibits excellent fouling resistance and chlorine resistance at the same time as well as good permeation performance, by coating or crosslinking the surface of a polyamide thin film with epoxy-silane compounds. Further, the method of the present invention can produce a polyamide composite layer through a simple process, thus at a relatively low production cost.
  • the method for preparing a polyamide composite membrane of the present invention includes the steps of: forming a polyamide thin film on a porous supporting layer; coating or crosslinking the polyamide thin film surface with a solution of epoxy-silane compounds and drying the resulted membrane; and washing the dried membrane with a basic aqueous solution.
  • the step of forming a polyamide thin film on a porous supporting layer may be carried out by well-known methods in this field of art.
  • the polyamide thin film is generally formed by: spreading an aqueous polyfunctional amine solution over the microporous supporting layer; removing the excess solution therefrom; contacting the resulted surface with an organic solvent containing amine-reactive compounds selected from the group consisting of polyfunctional acylhalide, polyfunctional sulfonylhalide and polyfunctional isocyanate; and carrying out interfacial polymerization.
  • the porous supporting layer used herein refers to a microporous supporting layer. Any well-known materials and production methods for the porous supporting layer in this field of art may be used herein without being specifically limited.
  • the dimension of a micropore should be large enough for the feed water to permeate, but not too much to hinder the crosslinking of a thin film formed on the micropores.
  • the hole diameter of the porous supporting layer is desirably 1 ⁇ 500 nm, without being specifically limited to this. When the hole diameter of the porous supporting layer is more than 500 nm, the surface membrane obtained from the interfacial polymerization permeates through the holes on the supporting layer, being difficult to form a normal flat membrane.
  • microporous supporting layer there is no specific restriction on materials for the microporous supporting layer, any materials generally used in this field of art may be employed. For instance, polymers such as polysulfone, polyether sulfone, polyimide, polyamide, polyether amide, polyacrylonitrile, polymethylmethacrylate, polyethylene, polypropylene, polyvinylidene fluoride and the like may be desirably mentioned. Although thickness of the microporous supporting layer is not specifically limited, 25 ⁇ 130 ⁇ m is desirable.
  • polyfunctional amines are not specifically limited, and any types well-known in this field of art may be used, for example, such as one polyfunctional amine or mixtures thereof.
  • examples include aromatic primary diamines of methylphenyldiamine or para-phenyl diamine, or substituted derivatives thereof; analogues having N-alkyl or aryl substituents; alkane diamines or cycloaliphatic primary amines such as cyclohexane diamine, cycloaliphatic secondary amines such as piperazine and alkyl derivatives thereof; and aromatic secondary diamines.
  • the substituent for the substituted aromatic primary amines includes an alkyl group, an alkoxy group, a hydroxyalkyl group or a halogen atom.
  • the polyfunctional amine is used in the form of an aqueous solution.
  • the polyfunctional amine may be contained in the aqueous solution at the amount of 0.1 ⁇ 30 wt%.
  • the aqueous solution of the polyfunctional amine has a pH of 7 ⁇ 13.
  • Acid acceptors such as hydroxide, carboxylate, carbonate, borate, alkali metal phosphate, trialkyl amine and the like may be further added to the aqueous solution of the polyfunctional amine, so as to neutralize acids (hydrochloric acid, etc.) generated during the interfacial polymerization.
  • the polyfunctional amine solution i.e. aqueous polyamine solution may be used alone or with other additives described in conventional arts.
  • a polar protic solvent and a mixture thereof a mixture of polar protic solvent and polar aprotic solvent may be used.
  • the polar protic solvent include alcohol, dialcohol, alcohol-ether and the like
  • examples of the polar aprotic solvent include diethyleneglycol; ether derivatives such as di(ethylene glycol) tertiary butylmethylether; and sulfoxide derivatives such as dimethylsulfoxide, butylsulfoxide, tetramethylenesulfoxide.
  • Other additives containing monomeric amine salts may be used for increasing the flow rate.
  • the polyfunctional acyl halide used in the interfacial polymerization is an aromatic compound having 2 ⁇ 3 carboxylic acid halides and for example, trimesoyl chloride, isophthaloyl chloride, terephthaloyl chloride and mixtures thereof may be widely used.
  • the aromatic polyfunctional acylhalide may be used alone or as a mixture, for example such as trimesoyl chloride, a mixture of trimesoyl chloride and isophthaloyl chloride and a mixture of trimesoyl chloride and terephthaloyl chloride.
  • the content of whole carboxylic acid halides in organic solvent may be 0.005 ⁇ 5 wt%.
  • the surface thereof is coated or crosslinked with a solution of epoxy-silane compounds, and the resulted membrane is dried.
  • the epoxy-silane compounds have both hydrophobic groups and hydrophilic groups.
  • the term 'coating' used herein generally means immobilization of epoxy silane compounds to the polyamide surface by the physical adsorption therebetween.
  • the term 'crosslink' used herein means immobilization of epoxy silane compounds to the polyamide surface by chemical linkages resulted from chemical reactions between nitrogen and oxygen on the polyamide surface and epoxy silane compounds.
  • the coating process of the surface of the polyamide thin film with a solution of epoxy-silane compounds involves a reaction of epoxy-silane compounds with polar atoms present on the surface of a polyamide reverse osmosis thin film, via a sol-gel reaction.
  • the epoxy-silane compounds may be crosslinked, for example, by Si-O bonds of functional groups such as ethoxy group formed on the polyamide surface, with the result that alkyl groups or epoxy groups can be coated on the membrane surface through a sol-gel method.
  • the epoxy-silane compounds may have a structure which contains not more than 3 alkoxy groups bonded with silicon, 1 or more alkyl group and glycidyl group. They may have a structure which contains not more than 3 alkoxy groups bonded with silicon, 1 or more alkyl group, ether group and glycidyl group at the end at the same time. Said compounds may be used alone or as a mixture in the form of a solution.
  • the epoxy-silane compounds may be at least one selected from the group consisting of [2,3-epoxypropoxy)alkyl]trialkoxy silane represented by the following chemistry figure 1, glycidylalkyltrialkoxy silane represented by the following chemistry figure 2 and mixtures thereof:
  • R is C1 ⁇ C4 alkylene group, and R' is C1 ⁇ C4 alkyl group.
  • the [2,3-epoxypropoxy)alkyl]trialkoxy silane may be selected from [(2,3-epoxypropoxy)methyl]trimethoxy silane, [(2,3-epoxypropoxy)methyl]triethoxy silane, [(2,3-epoxypropoxy)methyl]tripropoxy silane, [(2,3-epoxypropoxy)methyl]tributoxy silane, [2-(2,3-epoxypropoxy)ethyl]trimethoxy silane, [2-(2,3-epoxypropoxy)ethyl]triethoxy silane, [2-(2,3-epoxypropoxy)ethyl]tripropoxy silane, [2-(2,3-epoxypropoxy)ethyl]tributoxy silane, [3-(2,3-epoxypropoxy)propyl]trimethoxy silane, [3-(2,3-epoxypropoxy)propyl]triethoxy silane, [3-(2,3-ep
  • the glycidylalkyltrialkoxy silane may be selected from glycidylmethyltrimethoxy silane, glycidylmethyltriethoxy silane, 2-glycidylethyltrimethoxy silane, 2-glycidylethyltriethoxy silane, 3-glycidylpropyltrimethoxy silane, 3-glycidylpropyltriethoxy silane, 3-glycidylpropyltri(methoxyethoxy silane) and mixtures thereof, without being limited to these examples.
  • 3-glycidylpropyltrimethoxy silane or 3-glycidylpropyltriethoxy silane may be preferably used.
  • the epoxy-silane compounds may be used alone or as a mixture in the form of a solution.
  • the concentration of the epoxy-silane compounds is preferably 0.1-5 wt%.
  • the sol-gel reaction of silane occurs so negligibly on the membrane surface that it cannot cover the whole polyamide surface, which would deteriorate the chlorine resistance or fouling resistance properties.
  • the concentration is more than 5 wt%, the sol-gel reaction of silane on the membrane surface occurs excessively, forming a thick coat, which may cause a significant decrease in the flow rate, making the resulting membrane inefficient, although resistance to chlorine and fouling can be obtained.
  • ethanol is mainly used, however a mixed solvent of other polar solvent and water may be used.
  • the hot-air or air drying process increases the effective concentration of the materials for a sol-gel reaction.
  • the present invention further comprises, after coating or crosslinking the polyamide thin film surface with the solution of epoxy-silane compound, a step of drying the resulted membrane with hot air at the temperature range of 25 ⁇ 100°C.
  • the hot air drying process effectively fixes the epoxy-silane compounds to the surface of the polyamide thin film.
  • the resulted polyamide membrane is washed with a basic aqueous solution.
  • a basic aqueous solution Any types of basic aqueous solutions generally used in this field of art may be used without specific restriction. In this specification, a sodium carbonate or sodium hydroxide solution was used.
  • the polyamide composite membrane coated (or crosslinked) with epoxy-silane compounds obtained from the foregoing process, has both hydrophobic groups and hydrophilic groups coated on the polyamide thin film surface at the same time, thus showing fouling resistance and chlorine resistance, simultaneously.
  • Still another aspect of the present invention provides a polyamide composite membrane prepared by the above-described method.
  • the polyamide composite membrane is comprised of: a porous supporting layer; a polyamide thin film formed on the porous supporting layer; and an epoxy-silane compound layer coated or crosslinked on the polyamide thin film surface.
  • porous supporting layer, polyamide thin film and epoxy silane compounds are same as in the foregoing description.
  • the present invention used a disassembled commercial membrane as a substrate to minimize the changes in physical properties in the course of preparing a polyamide membrane, wherein the commercial membrane was originally manufactured as a module.
  • Used was a reverse osmosis membrane for brackish water (CPA2-4040), manufactured by Hydranautics corp. USA, which was formed on a porous supporting layer.
  • the porous supporting layer was a thin film made of polyester unwoven fabric casted with polysulfone, wherein the thickness of the thin film was 100-150 ⁇ m and the pore size was 0.01 ⁇ m.
  • the reverse osmosis membrane used herein was a polyamide reverse osmosis membrane for industrial use, made of about 90-95 ⁇ m of a reinforcing layer made of polyester unwoven fabric, 40-50 ⁇ m of a polysulfone support casted on said reinforcing layer, and about not more than 2 ⁇ m of polyamide polymer coated on the polysulfone support.
  • the initial salt rejection rate and permeation flow rate in the present invention were measured by using 2,000 ppm of an aqueous NaCl solution.
  • a system used for estimation of a reverse osmosis membrane was comprised of a permeation cell in the form of a flat panel, a high pressure pump, a reservoir and a cooling device.
  • the structure of the permeation cell in the form or a flat panel employs a cross-flow type, having an effective permeation area being 27.01 cm 2 .
  • warm-up operation of the system for testing a reverse osmosis membrane was carried out sufficiently for about 1 hour until the pressure and water permeation becomes regular. Water permeation degree was determined by measuring the amount of permeated water at an interval of 30 minutes.
  • Salt rejection was determined by analyzing the salt concentration before and after permeation, by using a conductivity meter.
  • the resistance to chlorine was determined in a mixed aqueous solution of 2,000 ppm of NaCl and 2,000 ppm of NaOCl.
  • the mixed solution was allowed to flow through the inside of the system for 10 to 30 seconds and maintained as being a stationary phase so that the salt permeation only occurs through the polyamide surface. Changes in salt rejection and flow rate were practically measured by operating time.
  • aqueous solution 2,000 ppm of NaCl and 100 ppm of casein was used. After determination of the initial permeation property, 100 ppm of the aqueous casein solution was directly fed to a tank, and then the permeation property was immediately determined. The changes in water permeation before and after the introduction of the casein-containing solution were plotted, and the slope at the time of change was calculated by using a computer program, determining the level of fouling.
  • the surface of the above-mentioned polyamide membrane (CPA2-4040) was coated with 1.5 wt% of an aqueous solution of 3-(2,3-epoxypropoxy)propyltrimethoxy silane (GPPTMS), wherein ethanol was used as a solvent, and dried with hot air at 70°C for 10 minutes. After drying, the surface was washed with water, and soaked in an aqueous NaOH solution at the pH of 10-11 for 2 hours or more so as to clean it, resulting in a polyamide composite layer. The performance of the resulted composite layer was measured by using 2,000 ppm of an aqueous NaCl solution, under pressure of 225 psi, and the results were represented in Table 1.
  • GPPTMS 3-(2,3-epoxypropoxy)propyltrimethoxy silane
  • the polyamide membrane (CPA2-4040) was not subjected to any surface treatment, but only soaked in distilled water 1 hour or more. Then, its permeation performance was estimated under the same conditions as described in Example 1, and the results were represented in Table 1.
  • a polyamide composite membrane was prepared as in Example 1, except that the concentration of GPPTMS was changed to 0.1 wt% (Example 2), 1.5 wt% (Example 3) and 3.0 wt% (Example 4), respectively.
  • the system for testing a reverse osmosis membrane was operated with a mixture of 2,000 ppm of an aqueous NaCl solution and 2,000 ppm of an aqueous NaOCl solution, under pressure of 225 psi. Then, the above obtained reverse osmosis membrane was subjected to the system to determine the initial permeation property, and the results were represented in Table 2.
  • a polyamide composite membrane was prepared as in Example 1, except that the drying condition for the coat formed by the aqueous GPPTMS solution was changed to 25°C (Example 5) and 70°C (Example 6), respectively.
  • the system for testing a reverse osmosis membrane was operated with a mixture of 2,000 ppm of an aqueous NaCl solution and 2,000 ppm of an aqueous NaOCl solution, under pressure of 225 psi. Then, the above obtained reverse osmosis membrane was subjected to the system to determine the initial permeation property, and the results were represented in Table 3.
  • a polyamide composite membrane was prepared as in Example 1.
  • the system for testing a reverse osmosis membrane was operated with a mixture of 2,000 ppm of an aqueous NaCl solution and 2,000 ppm of an aqueous NaOCl solution, under pressure of 225 psi. Then, the above resulted reverse osmosis membrane was subjected to the system to determine the initial permeation property, and the results were represented in Tables 4 and 5.
  • the polyamide membrane (CPA2-4040) was not subjected to any surface treatment, but only soaked in distilled water 1 hour or more. Then, its permeation performance was estimated under the same conditions as described in Example 2, and the results were represented in Tables 4 and 5.
  • Example 2 After completion of the estimation as in Example 1, the system for testing a reverse osmosis membrane was maintained with the permeation cell equipped with said coated membrane for 6 hours under the same conditions as described above, then operated 30 minutes under 225 psi, and the performance of the polyamide reverse osmosis composite membrane was measured. After an elapse of 12 hours, the system was operated 30 minutes under 225 psi again, and then the permeation property of the polyamide reverse osmosis composite membrane was measured. The results showing the changes in performance as time elapsed were represented in Tables 4 and 5.
  • the polyamide membrane (CPA2-4040) was not subjected to any surface treatment, but only soaked in distilled water 1 hour or more. Then, its permeation performance was estimated under the same conditions as described in Example 3, and the results were represented in Tables 4 and 5.
  • the salt rejection and permeation flow rate of the polyamide composite membrane prepared by the method of Example 1 were measured by using a mixed aqueous solution of 2,000 ppm NaCl and 100 ppm casein.
  • the salt rejection and flow rate before and after the introduction of the casen-containing solution were determined and compared.
  • the permeation flow rate was converted to MFI, an index of membrane fouling, and the results were disclosed in Table 6.
  • MFI defined by the following math figure, is mainly used for measuring a fouling level in a microfiltration membrane.
  • the MFI can be represented by the above math figure, provided that the thickness of a cake layer formed on the membrane surface (fouling) is in proportion to the filtered amount.
  • the flow rate (Q) is obtained by multiplying the measured permeation flux by the membrane area (A).
  • the resulted value is multiplied by filtration time (t) to obtain the filtered amount (V).
  • t filtration time
  • V the slope of t/V to V curve is a MFI value.
  • MFI is applied to a reverse osmosis membrane process
  • the change in permeation before and after introduction of fouling materials can be expressed as a change in the slope, helping to understand the level of fouling on the reverse osmosis membrane by comparing the slopes.
  • the higher the MFI value of a reverse osmosis membrane the greater the membrane fouling occurred.
  • the polyamide membrane (CPA2-4040) was not subjected to any surface treatment, but only soaked in distilled water 1 hour or more. Then, its permeation performance was estimated under the same conditions as in Example 4. The change in permeation flow rate represented by MFI was disclosed in Table 6.
  • the polyamide composite membranes of the present invention exhibit excellent chlorine and fouling resistance at the same time. Therefore, the polyamide composite membranes according to the present invention show strong resistance to cleaning agents such as sodium hypochlorite(NaOCl) that is generally introduced to reduce the membrane fouling, and are capable of reducing fouling of the membrane surface, thereby being advantageously applicable to a sea water desalination system or ultrapure water system.
  • cleaning agents such as sodium hypochlorite(NaOCl) that is generally introduced to reduce the membrane fouling
  • the process of preparing the polyamide composite membrane according to the present invention is simple and economical, since it employs kind of post-treatment of the surface of a polyamide thin film which has already been prepared, with epoxy-silane compounds.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Water Supply & Treatment (AREA)
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Abstract

La présente invention concerne un procédé de préparation d'une membrane composite à base de polyamide qui consiste à former un film mince de polyamide sur une couche de support poreuse, recouvrir ou réticuler la surface de ce film mince avec une solution de composés d’époxysilane, sécher la membrane résultante, et laver la membrane séchée avec une solution aqueuse basique. L’invention concerne également une membrane composite à base de polyamide préparée par ce procédé.
PCT/KR2009/001762 2008-11-28 2009-04-06 Membrane composite à base de polyamide résistant à l'encrassement et au chlore, et procédé de préparation associé WO2010062016A2 (fr)

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CN114425238A (zh) * 2022-01-19 2022-05-03 自然资源部天津海水淡化与综合利用研究所 耐污耐氯双功能化聚酰胺复合反渗透膜及其制备方法

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CN114425238B (zh) * 2022-01-19 2022-11-25 自然资源部天津海水淡化与综合利用研究所 耐污耐氯双功能化聚酰胺复合反渗透膜及其制备方法

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