KR20150079180A - Reverse-osmosis membrane having high boron rejection and method for manufacturing thereof - Google Patents

Abstract

The present invention relates to a reverse osmosis membrane with an excellent boron removal performance and a production method thereof. More particularly, the invention shows an excellent performance to remove a salt, a non-electrolytic organic compound, and a non-ionized compound while maintaining a relatively high flow rate compared with a reverse osmosis membrane. In particular, highly efficient boron removal has been realized and remarkably excellent stain resistance property has been achieved. Accordingly, the invention is useful as a membrane for water treatment. Further, the invention can be produced at lower cost compared with other reverse osmosis membranes and thus highly advantageous for mass production.

Description

BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a reverse osmosis membrane having high boron removal performance,

BACKGROUND OF THE INVENTION Field of the Invention The present invention relates to a reverse osmosis membrane having excellent boron removal performance and a method for producing the reverse osmosis membrane, and more particularly, to a reverse osmosis membrane having a boron removal rate and a stain resistance superior to that of a conventional reverse osmosis membrane .

Generally, the dissociated material can be separated from the solvent using various types of selective membranes. These selective membranes are classified into reverse osmosis membranes, ultrafiltration membranes and microfiltration membranes in order of increasing pore size.

Conventional use of reverse osmosis membranes is a desalination process of semi-saline or seawater, and this desalination process allows a large amount of fresh or pure water that is relatively suitable for industrial, agricultural, or domestic use. The desalination process of semi-brine or seawater using reverse osmosis membrane is a process of literally filtering salts, other dissolved ions or molecules from the brine. By passing the brine through the reverse osmosis membrane, the purified water passes through the membrane, Ions or molecules can not pass through the separator. The osmotic pressure is inevitably generated in the reverse osmosis process, and the higher the concentration of the raw water, the higher the osmotic pressure. Therefore, there are some conditions that reverse osmosis membranes must be equipped for in order to commercially use salt and seawater in large amounts for desalination, one of which has a high salt rejection rate. At present, the salt rejection rate of the reverse osmosis membrane for semi-saline water for commercial application is at least 97%.

One common type of reverse osmosis membrane is a composite membrane composed of a polymer support layer and a polyamide thin film formed on the polymer support layer. The polyamide thin film is formed by interfacial polymerization of a polyfunctional amine and a polyfunctional acyl halide.

Various attempts have been made in order to increase the permeation flow rate and the salt rejection rate of the polyamide reverse osmosis composite membrane. The attempts have been made to improve the chemical resistance of the membrane in addition to the membrane permeability. Most of these studies are based on the use of various types of additives in solutions used in interfacial polycondensation. Korean Patent Laid-Open Publication No. 2012-0073908 discloses a method in which a polyamide layer is interfacially polymerized to prepare a reverse osmosis membrane, wherein a material not participating in the reaction is added to an aqueous solution containing a polyfunctional amine and an organic solution containing a polyfunctional acid halide Discloses a technique for finely controlling the pore size. However, the above-mentioned technology has a disadvantage in that the use of additives is limited depending on the production method of the reverse osmosis membrane and the kind of the raw materials.

On the other hand, the concentration of boron present in the irrigation water plays an important role in the production and growth of crops. When the concentration is high, yellow spots appear on the plant leaves, accelerate decay, and ultimately end plant growth In particular, the presence of a high concentration of boron in drinking water can impair human reproductive function. In Europe, the maximum allowable level of boron in drinking water is 1ppm and in the United States (WHO) it is regulated to be less than 2.4ppm.

Boron generally has a greatly different ionization tendency depending on pH. For example, it is mostly boric acid (H ₃ BO ₃ ) in the form of boric acid at low pH, and has a small molecular size and is not charged. Therefore, it is difficult to remove from the separation membrane due to its weak electrical repulsion . However, as the pH is increased, the ionization proceeds, the molecular size becomes relatively large, and the negative charge becomes so that a large amount of boron can be removed due to the electrical repulsive force with the negative charge surface of the separation membrane.

In general, seawater contains about 4 to 5 ppm of boron at a pH of about 7 to 8, and the boron exists in the form of boric acid. Specifically, at pH 7, non-ionized boric acid (H ₃ BO ₃ ) accounts for 99.3% and at pH 8 it accounts for 93.2%. For most seawater desalination, the boron removal rate is 82-86% at pH 8. Applying a removal rate of 86% compared to the source water, the treatment water concentration is more than 0.5ppm, which exceeds the WHO regulatory limit.

Therefore, research on reverse osmosis membranes having boron removal ability has been continued, and there are a method of changing pH and a method of changing pore size.

The method of changing the pH is a method of increasing the boron removal rate by increasing the pH of the treated water. In this case, the boron removal rate increases vertically. That is, as the pH increases, the boric acid (H ₃ BO ₃ ) form proceeds in the form of a negatively charged borate (H ₂ BO ₃ ^- ), and the molecular size becomes relatively large and the electrical repulsive force with the negative charge surface increases to be. Therefore, it has been reported that the boron removal rate is more than 99% at pH 10 and 100% at pH 12.

However, when the pH of the raw water is increased to raise the removal rate of boron, the scaling phenomenon of calcium carbonate and magnesium hydroxide present in seawater is increased, and finally the flow rate of permeated water is reduced and the life of the membrane is shortened It causes. In addition, the use of a large amount of buffer solution to lower the pH leads to an increase in cost.

On the other hand, in the case of the method of changing the pore size as the second method of removing boron, according to T. Uemura in the conference of [2007 Asian Conference on Desalination & Water Reuse] As a result of measuring the pore size of the polyamide layer of the reverse osmosis membrane using molecular design technology, it was reported that the size of the reverse osmosis membrane was 0.56 ~ 0.70 nm and the porosity removal rate increased with decreasing pore size. It has been reported that the method of controlling the pore size can be one of the parameters to improve the boron removal rate.

However, it is not easy to control the pore size when the separation membrane is manufactured, and the small pore size has a problem of lowering the overall flow rate.

Therefore, a reverse osmosis membrane having a high boron removal ability has been developed, but a reverse osmosis membrane that satisfies all of the above cases has a problem in that it is difficult to commercialize a reverse osmosis membrane that has a reduced flow rate or a large amount of reverse osmosis. Also, even if all of them are satisfied, there is a problem that the production cost is excessively high and the contamination resistance is not remarkably low.

SUMMARY OF THE INVENTION The present invention has been conceived to solve the above-mentioned problems, and an object of the present invention is to provide a reverse osmosis membrane having remarkably improved boron removal performance while maintaining a proper flow rate of reverse osmosis membrane, Two modules.

In order to solve the above-mentioned first problem, the present invention provides a method of manufacturing a semiconductor device, comprising the steps of: (1) treating a polymer solution on a support to form a polymer support layer; (2) immersing the polymer support layer in an aqueous solution containing a polyfunctional amine, and then contacting the polymer support layer with an organic solution containing a polyfunctional acid halide compound to form a polyamide layer; (3) reacting the polyamide layer with a solution containing a halogen compound; And (4) reacting the polyamide layer with a precursor solution containing a hydrophilic acrylic monomer to bind a polymer containing a hydrophilic acrylic monomer to the polyamide layer, thereby providing a reverse osmosis membrane production method having excellent boron removal performance .

According to a preferred embodiment of the present invention, the polymer solution of the step (1) may be selected from the group consisting of a polysulfone polymer, a polyamide polymer, a polyimide polymer, a polyester polymer, an olefin polymer, polyvinylidene fluoride, Acrylonitrile, acrylonitrile, and acrylonitrile.

According to another preferred embodiment of the present invention, the halogen compound in the step (3) is selected from the group consisting of a halogen acid, a hypohalogenous acid, a metal salt of a halogen acid, a metal salt of a hypohalous acid, a halogen complex and a metal halide And may include any one or more of them.

According to another preferred embodiment of the present invention, the step (3) may include treating the polyamide layer with a solution containing 0.01 to 1% by weight of a halogen compound.

According to another preferred embodiment of the present invention, the hydrophilic acrylic monomer of the step (4) may include one or more of the compounds represented by the following formulas (1) and (2).

[Chemical Formula 1]

Wherein R ₁ and R ₂ are each independently a C ₁ -C ₃ alkyl group, a hydrogen atom or a hydroxyl group, and a is an integer of 1 to 100.

(2)

Wherein R ₃ and R ₄ are each independently a C ₁ -C ₃ alkyl group, a hydrogen atom or a hydroxyl group, and b is an integer of 1 to 100.

According to another preferred embodiment of the present invention, the step (4) is modified to include a transition metal compound as a catalyst, and the transition metal compound may be contained in a molar ratio of 1: 0.01 to 1 based on the hydrophilic acrylic monomer.

According to another preferred embodiment of the present invention, the catalyst is _{CuCl, CuBr, CuBr 2, CuCl} 2, CuCl 2 · 2H 2 O, FeCl 3, FeCl 2, FeCl 3 · 6H 2 O, FeBr 2, FeBr 3 _{, [Fe (CpCl 2)]} n (where n is 1-4 _{integer), RuCl 2 (PPh 3)} 2, RuCl 3 X · H 2 O ( where X is _{F, Cl, Br, C 1} ~ 10 aryl phosphine of an alkyl phosphine, or C _{6 ~ 20 pinim), Ru [CpPPh 3 Cl 2} ], [RuCpCl 2] n ( where, n is 1-4 integer, Cp is cyclopentadienyl nilim), RuCl _3, At least one transition metal compound selected from the group consisting of NiBr ₂ , NiCl ₂ , Fe (OAc) ₂ , Ru [CpCl ₂ ] ₃ , NiCl ₂ (PPh ₃ ) ₂ and NiBr ₂ (PPh ₃ ) ₂ ; And at least one transition metal compound selected from the group consisting of triphenylphosphine, 2,2'-6,2'-terpyridine, 1,1,4,7,10,10-hexamethyltriethylenetetramine, N, N, N, N ', N'-tetramethylethylenediamine, 2,2', N'-tetramethylethylenediamine, N, N'-pentamethyldiethylenetriamine, -Bipyridine, diphenyl-2-pyridylphosphine, tributylphosphine, 2-amino-3-methyl-5-nitropyridine, 2- diphenylphosphino- Amino) biphenyl, 2- [(diphenylphosphino) methyl] pyridine, 9,9-dimethyl-4,5-bis (diphenylphosphino) , N, N'-dimethylethylenediamine, N, N (N, N'-dimethylaniline) -Dimethylthiophene-2-methylamine, triphenylphosphate, trimethylphosphite, trimethylphosphate, triphenylphosphite, imino-tris (dimethylamino) (Diphenylphosphino) benzaldehyde, 1,4,8,11-tetramethyl-1,4,8,11-tetraazacyclotetradecane, 1,3-bis (diphenylphosphino) Any one selected from the group consisting of bis (diphenylphosphino) methane, ethylene bis (diphenylphosphine), tri-t-butylphosphine, diphenyl (2- methoxyphenyl) Or a compound in which the above-mentioned ligands are bonded.

According to another preferred embodiment of the present invention, the step (4) may be performed at a temperature of 30 to 80 ° C for 0.5 to 10 minutes.

Further, in order to solve the second problem described above, the present invention provides a semiconductor device comprising: a support; A polymeric support layer formed on at least one side of the support; A polyamide layer formed on the polymer support layer; And a polymer represented by the following formulas (3) and (4) bonded to the polyamide layer.

(3)

이고, a는 1~100인 정수임.
In Formula 3, A ₁ , A _2, and A ₃ are each independently a C ₁ -C ₃ alkyl group, a hydrogen atom, a hydroxyl group,

And a is an integer of 1 to 100.

[Chemical Formula 4]

이고, b는 1~100인 정수임.In Formula 4, B ₁ , B _2, and B ₃ are each independently a C ₁ to C ₃ alkyl group, a hydrogen atom, a hydroxyl group,

And b is an integer of 1 to 100.

According to a preferred embodiment of the present invention, the polymer support layer may be formed of a polymer including a polysulfone polymer, a polyamide polymer, a polyimide polymer, a polyester polymer, an olefin polymer, polyvinylidene fluoride and polyacrylonitrile And at least one polymer selected from the group consisting of polyolefins.

According to another preferred embodiment of the present invention, the reverse osmosis membrane may contain a halogen atom covalently bonded to the surface of the polyamide layer.

According to another preferred embodiment of the present invention, the polymer represented by Formula 3 may be a polymer represented by Formula 5 below.

[Chemical Formula 5]

이고, r은 1~100인 정수임.In the general formula (5), A ₇ represents a C ₁ -C ₃ alkyl group, a hydrogen atom, a hydroxyl group or

And r is an integer of 1 to 100.

According to another preferred embodiment of the present invention, the molecular weight of the compound represented by any one of Chemical Formulas 3 to 5 may be 300 to 200,000 u (Dalton).

According to another preferred embodiment of the present invention, the reverse osmosis membrane may have a permeate flow rate of 12 gfd or more and a boron removal rate of 91% or more at 25 ° C and 800 psi pressure in an aqueous solution containing 32,000 ppm sodium chloride and 5 ppm boron.

According to another preferred embodiment of the present invention, the reverse osmosis membrane may have a flow rate reduction rate of 5% or less after being operated for 2 hours at 25 ° C and 800 psi pressure in an aqueous solution of 25 ppm fat powder.

In order to solve the second problem, the present invention provides a reverse osmosis module including a reverse osmosis membrane according to the present invention.

Hereinafter, terms used in the present invention will be described.

As used herein, the term "*" in the formula means a binding site with another atom or compound not shown in the chemical formula.

The reverse osmosis membrane of the present invention is excellent in the removal efficiency of salt removal ratio, non-electrolytic organic compound and non-ionized compound while maintaining a proper flow rate compared to the conventional reverse osmosis membrane. Particularly, the removal efficiency of boron is high, And is useful as a water treatment separator. Furthermore, the production cost is lower than other reverse osmosis membranes and the production time is short, which is very advantageous for mass production.

1 is a graph of an X-ray photoelectron spectrum (XPS) of a surface of a reverse osmosis membrane according to a preferred embodiment of the present invention.
2 is an exploded perspective view of a reverse osmosis module according to a preferred embodiment of the present invention.

Hereinafter, the present invention will be described in more detail.

As described above, reverse osmosis membranes having high boron removal ability have been developed. However, reverse osmosis membranes satisfying all of them have been found to be difficult to commercialize because reverse osmosis membranes having a high boron removal ability have been developed. In addition, there is a problem that the production cost is excessively high and / or the contamination resistance is not remarkable even if all of them are satisfied.

(1) forming a polymer support layer by treating a polymer solution on a support; (2) immersing the polymer support layer in an aqueous solution containing a polyfunctional amine, and then contacting the polymer support layer with an organic solution containing a polyfunctional acid halide compound to form a polyamide layer; (3) reacting the polyamide layer with a solution containing a halogen compound; And (4) reacting the polyamide layer with a precursor solution containing a hydrophilic acrylic monomer to bind a polymer containing a hydrophilic acrylic monomer to a polyamide layer, thereby providing a reverse osmosis membrane production method having excellent boron removal performance And solved the above-mentioned problem. As a result, it is possible to maintain the proper flow rate of the conventional reverse osmosis membrane and to remove the salts, the non-electrolytic organic compounds and the non-ionized compounds. In particular, since the boron removal efficiency is high and the stain resistance is excellent, useful. Furthermore, the production cost is lower than other reverse osmosis membranes and the production time is short, which is very advantageous for mass production.

In step (1), the polymer solution is treated on the support to form a polymer support layer. The support is not particularly limited as long as it usually serves as a support for the membrane, but more preferably synthetic fibers selected from the group consisting of polyester, polypropylene, nylon and polyethylene; Or a natural fiber including a cellulose-based material may be used, and it may preferably be a woven fabric or a nonwoven fabric in its shape. The fabric means that the fibers included in the fabric have longitudinal and lateral directions, and the specific structure may be plain weave, twill weave, etc., and the density of warp and weft yarn is not particularly limited. Further, when the support is a nonwoven fabric, the physical properties of the membrane can be controlled according to the porosity and hydrophilicity of the material. The nonwoven fabric may have an average pore diameter of 1 to 600 μm, preferably 5 to 300 μm, so that smooth permeation of the fluid and water permeability required for the reverse osmosis membrane can be enhanced. However, the diameter of the pores is not limited. The thickness of the nonwoven fabric layer is preferably 20 to 150 占 퐉, and if it is less than 20 占 퐉, the strength and supportability of the entire membrane is insufficient, and if it exceeds 150 占 퐉, the flow rate may be decreased.

The solvent for forming the polymer solution is not particularly limited as long as it can dissolve the polymer uniformly without forming precipitates, but is more preferably selected from the group consisting of N-methyl-2-pyrrolidone (NMP), dimethylformamide (DMF) Dimethylsulfoxide (DMSO) or dimethylacetamide (DMAc), or the like.

If the temperature is lower than 20 ° C, the polymer may not be dissolved and the membrane may not be produced. If the temperature is higher than 90 ° C, the viscosity of the polymer solution may become too thin, and thus the membrane may be difficult to produce .

The polymer forming the polymer solution is not particularly limited as long as it is capable of forming a reverse osmosis membrane, but it is more preferably a polysulfone-based polymer including a polysulfone or polyethersulfone, a polyamide-based polymer, a polyimide-based polymer, An olefin-based polymer such as a polyester-based polymer and a polypropylene, a polybenzimidazole polymer, polyvinylidene fluoride or polyacrylonitrile, or the like.

The polymer solution may preferably contain 7 to 35% by weight of the polymer. If the content of the polymeric substance is less than 7% by weight, the strength is lowered and the solution viscosity is low. Thus, the film is difficult to manufacture and has a problem. When it exceeds 35% by weight, the concentration of the polymer solution is too high.

The polymer support layer used in the reverse osmosis membrane of the present invention is a general microporous support layer and is not particularly limited in its kind but is generally large enough to permit permeation of permeated water and large enough to interfere with the ultra- Should not. At this time, the pore size of the polymer support layer is preferably 1 to 500 nm, and if it exceeds 500 nm, the ultra thin film may sink into the pore size after the formation of the thin film, so that it may be difficult to achieve the required flat sheet structure.

Next, in step (2), the polymer support layer is immersed in an aqueous solution containing a polyfunctional amine and then contacted with an organic solution containing a polyfunctional acid halide compound to form a polyamide layer.

Specifically, the polyfunctional amine may be a polyamine having two or three amine functional groups per monomer, and may include a primary amine or a secondary amine. As the polyamines, aromatic primary diamine is used as the metaphenylenediamine, paraphenylenediamine, orthophenyldiamine and the substituent. As another example, aliphatic primary diamine and cycloaliphatic primary diamine such as cyclohexenediamine , Cycloaliphatic secondary amines such as piperazine, and aromatic secondary amines. More preferably, the polyfunctional amine is selected from the group consisting of metaphenylenediamine, and the concentration thereof is preferably in the form of an aqueous solution containing 0.5 to 10 wt% of metaphenylenediamine, more preferably 1 to 4 wt% % May be contained.

Upon formation of the polyamide layer of the present invention, the polyfunctional amine-containing aqueous solution may be applied onto the polymer support layer for 0.1 to 10 minutes, more preferably for 0.5 to 1 minute.

The material which reacts with the polyfunctional amine used in forming the polyamide layer of the present invention is a polyfunctional acid halide, that is, a polyfunctional acyl halide. Preferably, it may be used alone or in a mixed form of trimesoyl chloride, isophthaloyl chloride, 5-methoxy-1,3-isophthaloyl chloride, terephthaloyl chloride and the like. At this time, the use of the mixed form is most preferable in terms of the salt removal rate. The polyfunctional acyl halide may be dissolved in an aliphatic hydrocarbon solvent in an amount of 0.01 to 2% by weight. The aliphatic hydrocarbon solvent may be a mixture of n-alkanes having 5 to 12 carbon atoms and structural isomers of saturated or unsaturated hydrocarbons having 8 carbon atoms It is preferable to use a cyclic hydrocarbon having 5 to 7 carbon atoms. The polyfunctional acyl halide-containing solution preferably dissolves 0.01 to 2% by weight, more preferably 0.05 to 0.3% by weight, of the polyfunctional acyl halide in the aliphatic hydrocarbon solvent. In forming the polyamide layer of the present invention, the polyfunctional acid halide compound may be applied to the membrane treated with the aqueous solution containing the polyfunctional amine for 0.1 to 10 minutes, more preferably for 0.5 to 1 minute.

Next, in step (3), the polyamide layer is reacted with a solution containing a halogen compound.

The hydrogen atom of the amide group contained in the polyamide layer is substituted with a halogen atom contained in the halogen compound through the reaction of the step (3), and the substituted halogen atom reacts with the hydrophilic acrylic monomer in the step (4) To the polyamide layer.

Conventionally, there have been many attempts to control the pore size of the reverse osmosis membrane, more specifically, the polyamide layer. To this end, there has been a method of adding additives. However, this technique has been problematic in that the use of additives is limited or limited depending on the membrane preparation method and membrane material . In addition, there have been attempts to bond a substance for adjusting the pore size to the surface of the polyamide layer in the prior art, and a method using a cross-linking agent such as bis-epoxide or glutaraldehyde has been widely used. However, when a substance that controls the pore size using a crosslinking agent is bonded to the surface of the polyamide layer, the substances for controlling the pore size bound to the surface during use of the reverse osmosis membrane are separated, and the molecular weight distribution of the polymer It is difficult to make it narrow, and oxygen and moisture must be absolutely removed in the polymerization process.

However, in the present invention, the substitution of the halogen atom with the hydrogen atom of the amide group without the use of such a crosslinking agent makes the halogen atom a reaction point for the polymerization reaction in the step (4) to be described below, so that the hydrophilic acrylic monomer can be more easily reacted with the polyamide layer .

Specifically, the halogen compound may include at least one halogen atom selected from fluorine, chlorine, bromine, and iodine, and the halogen compound is preferably a halogen acid, a hypohalogen acid, a metal salt of a halogen acid, Metal complexes, metal halides, metal complexes, and metal halides.

More specifically, the halogen acid may include at least one of chloric acid, bromic acid, and iodic acid. The hypochlorous acid may include at least one of hypochlorous acid, hypochlorous acid and hypochlorous acid.

The metal salt of the halogen acid or the hypohalogen acid may include at least one of an alkali metal salt, an alkaline earth metal salt and a transition metal salt of a halogen acid or a hypohalous acid. The halogen complex may be aluminum fluoride or the like.

The metal halide may be a compound containing a metal such as an alkali metal, an alkaline earth metal, or a transition metal, and examples thereof include lithium fluoride, lithium chloride, lithium bromide, lithium iodide, sodium fluoride, Magnesium chloride, magnesium bromide, magnesium iodide, calcium fluoride, calcium chloride, calcium bromide and calcium iodide, which may be used singly or in a mixture of two or more kinds. . The metal halide can be preferably potassium iodide, which can achieve a better boron removal rate.

The solvent of the solution containing the halogen compound is not particularly limited as long as it can dissolve the halogen compound uniformly without forming a precipitate. More preferably, the n-alkane having 5 to 12 carbon atoms and the saturated or unsaturated A structural isomer of a hydrocarbon, or a cyclic hydrocarbon having 5 to 7 carbon atoms may be used. The solution containing the halogen compound may contain 0.01 to 1% by weight of a halogen compound. If the concentration of the solution containing the halogen compound is less than 0.01% by weight, the polymerization of the polyamide layer and the monomer may not be initiated or may be formed thinly to decrease the physical properties. If the concentration exceeds 1% by weight, There may be a problem that the degree of polymerization between the polyamide layer and the monomer is lowered.

The step (3) may be carried out by treating the polyamide layer with a solution containing a halogen compound having the above-mentioned concentration. The treatment method is not particularly limited, but the polyamide layer is immersed in a solution containing a halogen compound Can be performed. At this time, the temperature of the solution containing the halogen compound may preferably be 25 to 100 ° C. If the temperature of the solution is less than 25 ° C, the substitution reaction between the hydrogen atom and the halogen atom of the amide group contained in the polyamide layer may be insufficient. If the temperature of the solution exceeds 100 ° C, There may be a problem that the flow amount is reduced. The immersion time may be 0.5 to 3 minutes, and the solution may be washed after immersion. The solution used for washing may be used without limitation in the case of a solution which does not affect the polyamide layer containing substituted halogen atoms, It may be washed with distilled water, and it is preferable to wash at a temperature of 25 to 80 ° C for 1 to 10 minutes.

Next, in step (4), the modified polyamide layer is reacted with a precursor solution containing a hydrophilic acrylic monomer to bind a polymer containing a hydrophilic acrylic monomer to the polyamide layer.

First, the hydrophilic acrylic monomer will be described.

The hydrophilic acrylic monomer introduced into the polyamide layer enhances the pore size of the polyamide layer to improve the salt removal rate, the removal efficiency of the non-electrolytic organic compound and the non-ionized compound, and particularly the boron removal rate.

According to a preferred embodiment of the present invention, the hydrophilic acrylic monomer may include at least one of compounds represented by the following general formulas (1) and (2).

First, the formula (1) will be described.

 [Chemical Formula 1]

In Formula 1, R ₁ and R ₂ may each independently be a C ₁ -C ₃ alkyl group, a hydrogen atom, or a hydroxy group. At least one of R ₁ and R ₂ may not be a hydrogen atom, and when both of R ₁ and R ₂ are hydrogen atoms, the hydrophilicity may be lowered and the water permeability may be reduced. In addition, R ₁ and R ₂ may each independently be a C ₁ -C ₃ alkyl group. In order to achieve both a better water permeability and a boron removal rate at the same time, R ₁ in the above formula (1) ₂ may be a hydroxy group.

Also, a may be an integer of 1 to 100, and if a is more than 100, there may be a problem that the molecular weight of the polymer to be combined with the polyamide layer becomes too large to reduce the flow rate.

Next, the formula (2) will be described.

 (2)

In Formula 2, R ₃ and R ₄ may each independently be a C ₁ -C ₃ alkyl group, a hydrogen atom, or a hydroxy group. Further, the R ₃ and at least one of R4 may be the hydrophilic property is lowered if the transmission rate is reduced can not be hydrogen atoms, wherein R ₃ and R ₄ are both a hydrogen atom. In addition, R ₃ and R ₄ may each independently be a C ₁ -C ₃ alkyl group. In order to achieve both a better water permeability and a boron removal rate at the same time, R ₃ in the general formula (2) ₂ may be a hydroxy group.

In addition, b may be an integer of 1 to 100, and if b is more than 100, there may be a problem that the molecular weight of the polymer to be combined with the polyamide layer becomes too large to reduce the flow rate.

According to a preferred embodiment of the present invention, among the monomers represented by the formula (1) and the monomer represented by the formula (2), a boron removal rate better than that obtained when the monomer represented by the formula (1) is introduced onto the surface of the polyamide layer , And the pollution resistance was also better.

Meanwhile, in the step (4), the polyamide layer is reacted with a precursor solution containing the hydrophilic acrylic monomer as described above. Hereinafter, a specific method will be described.

The reaction can be performed by applying a precursor solution containing a hydrophilic acrylic monomer to a polyamide layer or by immersing the polyamide layer to induce polymerization reaction of the hydrophilic acrylic monomer on the polyamide layer. More specifically, the hydrophilic acrylic monomer can be chemically bonded directly to the position of the halogen atom bonded to the amide group of the polyamide layer formed through the step (3), and the hydrophilic acrylic monomer can be chemically bonded to the position of the halogen atom bonded to the amide group of the polyamide layer formed through the step The hydrophilic monomer is polymerized to form a polymer having hydrophilic monomers in the polyamide layer, and the pores can be formed more densely and the pores of the polyamide layer can be finely adjusted have. Thus, fine control of the pore size can be achieved by controlling the degree of polymerization, and as the hydrophilic monomer is directly chemically bonded to the amide group of the polyamide layer, the bonding force is excellent compared with the case where the hydrophilic monomer is bonded to the polyamide layer by the cross- The polymer containing the hydrophilic monomer may not be released, and the structure of the film may be remarkably improved. In addition, polymers containing hydrophilic acrylic monomers directly bonded to the polyamide layer have the advantage of making the pores more uniform as they have a narrow molecular weight distribution. Further, the polymerization reaction of the step (4) according to the present invention can improve the productivity in a time and cost as the polymerization rate rapidly occurs, and mass production can be possible.

There is no particular limitation so long as it is a solvent for a precursor solution containing a hydrophilic acrylic monomer for coating or immersion on a polyamide layer, and can be uniformly dissolved without forming a precipitate of a hydrophilic acrylic monomer. The concentration of the precursor solution containing the hydrophilic acrylic monomer may preferably be 0.0001M to 1M, and more preferably 0.005 to 0.02M. If the molar concentration of the precursor solution containing the hydrophilic acrylic monomer is less than 0.0001M, the introduction of the polyamide layer of the hydrophilic acrylic monomer is weak and the boron removal rate can not be improved. When the molar concentration exceeds 1M, There may be a problem in that it is deteriorated at the same time.

When the polyamide layer is coated or immersed in the precursor solution containing the hydrophilic acrylic monomer, the temperature of the solution may be 30 to 80 ° C. If the temperature range is not satisfied, The introduction of the monomer into the polyamide layer and the degree of polymerization may be lowered, so that the improvement of the boron removal rate may be insignificant.

The reaction time of step (4) is preferably 0.5 to 10 minutes. If the reaction time is less than 0.5 minutes, the desired degree of polymerization can not be obtained. If the reaction time is more than 10 minutes, It is not possible to obtain a polymer, and there may be a problem of deterioration of physical properties such as a decrease in flow rate.

Also, according to a preferred embodiment of the present invention, the step (4) may include a transition metal compound as a catalyst. Preferably, the transition metal compound is _{CuCl, CuBr, CuBr 2, CuCl} 2, CuCl 2 · 2H 2 O, FeCl 3, FeCl 2, FeCl 3 · 6H 2 O, FeBr 2, FeBr 3, [Fe (CpCl 2) ] _n (where n is 1-4 _{integer), RuCl 2 (PPh 3)} 2, RuCl 3 X · H 2 O ( where X is F, Cl, Br, alkyl phosphine of C _{1 ~ 10,} or C _{6 ~} aryl phosphonium _{pinim), Ru [CpPPh 3 Cl 2} ] of _20, [RuCpCl _{2] n} (where, n is 1-4 integer and, Cp is cyclopentadienyl _{nilim), RuCl 3, NiBr 2,} NiCl 2, Fe (OAc) ₂ , Ru [CpCl ₂ ] ₃ , NiCl ₂ (PPh ₃ ) ₂ and NiBr ₂ (PPh ₃ ) ₂ . Among the above transition metal compounds, PPh means phenylphosphine and Cp means cyclopentadienyl. The transition metal compound may have an improved reaction rate by inducing a reversible oxidation-reduction reaction to induce a reversible reaction of a halogen atom between a growth species and a dormant species, and a polymer containing a hydrophilic monomer having a narrower molecular weight distribution .

In order to induce polymerization reaction more stably, a ligand may be used in combination with a transition metal compound used as the catalyst. Specifically, the ligand is selected from the group consisting of triphenylphosphine, 2,2'-6,2'-terpyridine, 1,1,4,7,10,10-hexamethyltriethylenetetramine, N, N, N ', N ', N' '- pentamethyldiethylenetriamine, 4,4'-dimethyl-2,2'-dipyridyl, N, N, N', N'-tetramethylethylenediamine, 2,2'- Amino-3-methyl-5-nitropyridine, 2-diphenylphosphino-2 '- (N, N'-dimethylamino ) Biphenyl, 2 - [(diphenylphosphino) methyl] pyridine, 9,9-dimethyl-4,5-bis (diphenylphosphino) (2-picolyl) amine, hexamethylphosphoramide, N, N'-dimethylethylenediamine, N, N'- Dimethylthiophene-2-methylamine, triphenylphosphate, trimethylphosphite, trimethylphosphate, triphenylphosphite, imino-tris (dimethylamino) (Diphenylphosphino) benzaldehyde, 1,4,8,11-tetramethyl-1,4,8,11-tetraazacyclotetradecane, 1,3-bis (diphenylphosphino) Bis (diphenylphosphino) methane, ethylenebis (diphenylphosphine), tri-t-butylphosphine, diphenyl (2-methoxyphenyl) phosphine and 2-pyridinethioamide.

The transition metal compound or the transition metal compound to which the ligand is bound may be contained in a molar ratio of 1: 0.01 to 1 based on the hydrophilic acrylic monomer. If the transition metal compound is contained in an amount of less than 0.01 mol, There is a problem that the improvement of the boron removal rate may be insignificant. When the amount of the boron excess is more than 1 mol, the improvement of the polymerization reactivity may be insignificant.

As described above, the reverse osmosis membrane carried out up to step (4) may be subjected to a washing process, and the solution used in the washing process may be used without limitation as long as the solution does not affect the reverse osmosis membrane produced through step (4) May be washed with distilled water at a temperature of 25 to 80 ° C and a washing time of 1 to 10 minutes.

On the other hand, the reverse osmosis membrane of the present invention produced by the above-described production method comprises a support; A polymeric support layer formed on at least one side of the support; A polyamide layer formed on the polymer support layer; And a hydrophilic acrylic polymer bonded to the polyamide layer.

First, the support included in the reverse osmosis membrane of the present invention will be described.

The support is not particularly limited as long as it usually serves as a support for the membrane, but more preferably synthetic fibers selected from the group consisting of polyester, polypropylene, nylon and polyethylene; Or a natural fiber including a cellulose-based material may be used, and it may preferably be a woven fabric or a nonwoven fabric in its shape. The fabric means that the fibers included in the fabric have longitudinal and lateral directions, and the specific structure may be plain weave, twill weave, etc., and the density of warp and weft yarn is not particularly limited. Further, when the support is a nonwoven fabric, the physical properties of the membrane can be controlled according to the porosity and hydrophilicity of the material. The nonwoven fabric may have an average pore diameter of 1 to 600 μm, preferably 5 to 300 μm, so that smooth permeation of the fluid and water permeability required for the reverse osmosis membrane can be enhanced. However, the diameter of the pores is not limited. The thickness of the nonwoven fabric layer is preferably 20 to 150 占 퐉, and if it is less than 20 占 퐉, the strength and supportability of the entire membrane is insufficient, and if it exceeds 150 占 퐉, the flow rate may be decreased.

Next, the polymer support layer formed on at least one side of the support will be described.

The polymer support layer is not particularly limited as long as it can form a reverse osmosis membrane. However, in consideration of mechanical strength, it is preferable to use a polymer having a weight average molecular weight in the range of 65,000 to 150,000, and preferred examples thereof include polysulfone or polyethersulfone An olefin polymer such as a polysulfone polymer, a polyamide polymer, a polyimide polymer, a polyester polymer or a polypropylene, a polybenzimidazole polymer, polyvinylidene fluoride or polyacrylonitrile, Lt; / RTI >

The thickness of the polymer support layer may be in the range of 30 to 300 占 퐉. If the thickness is less than 30 占 퐉, there may be a problem of lowering the flow rate and durability due to compaction, and if it is more than 300 占 퐉, . The pore size of the polymer support layer is preferably 1 to 500 nm.

Next, the polyamide layer formed on the polymer support layer will be described.

The polyamide layer formed on the polymer support layer may be formed by interfacial polymerization by immersing in an aqueous solution containing a polyfunctional amine and then contacting the solution with an organic solution containing a polyfunctional acid halide compound. If the thickness of the polyamide layer is less than 0.1 탆, the salt removing ability is deteriorated to fail to serve as a selective layer. If the thickness exceeds 1 탆, the thickness of the selective layer is excessively thick, There may be a problem.

Next, the hydrophilic acrylic polymer bonded to the polyamide layer will be described.

The inventors of the present invention have found that the conventional reverse osmosis membrane can not satisfy both excellent water permeability and boron removal rate at the same time. In order to solve the problem, hydrophilic acrylic polymer is bonded to the polyamide layer, And at the same time, the polymer was not desorbed during the reverse osmosis operation, so that it was possible to continuously obtain an excellent boron removal rate and to obtain a good flow rate.

The hydrophilic acrylic polymer may be any one or more of the polymers represented by the following general formulas (3) and (4).

(3)

이고, a는 1 ~ 100인 정수임.In Formula 3, A ₁ , A _2, and A ₃ are each independently a C ₁ -C ₃ alkyl group, a hydrogen atom, a hydroxyl group,

And a is an integer of 1 to 100.

[Chemical Formula 4]

이고, b는 1 ~ 100인 정수임.
In Formula 4, B ₁ , B _2, and B ₃ are each independently a C ₁ to C ₃ alkyl group, a hydrogen atom, a hydroxyl group,

And b is an integer of 1 to 100.

First, the polymer represented by the general formula (3) in the above polymer will be described.

이며, 여기서, A₁, A₂ 및 A₃는 각각 독립적으로 C₁ ~ C₃의 알킬기, 수소원자, 하이드록시기 또는

(이하, 화학식 X라고 함)일 수 있다. The polymer represented by the general formula (3)

Wherein A ₁ , A ₂ and A ₃ are each independently a C ₁ -C ₃ alkyl group, a hydrogen atom, a hydroxyl group or a

(Hereinafter referred to as the formula X).

In this case, a in Formula 3 may be an integer of 1 to 100, and if a is more than 100, there may be a problem that a polymer having a desired molecular weight can not be obtained.

In addition, any one or more of A ₁ , A ₂ and A ₃ in the above formula (3) may be a C ₁ -C ₃ alkyl group, more preferably a methyl group, and in this case, it may have a better boron removal ability.

At least one of A ₁ , A ₂ and A ₃ in the general formula (3) may be a hydrogen atom, but preferably all of A ₁ , A ₂ and A ₃ may not be a hydrogen atom. If all of A ₁ , A ₂ and A ₃ are hydrogen atoms, the hydrophilicity may be lowered compared with the case where the hydrogen atoms are not hydrogenated, the water permeability may be reduced, and the polymerization may not be properly performed, have.

(화학식 X)일 경우, 상기 화학식 X의 중합체에 포함되는 A₁, A₂ 및 A₃는 각각 독립적으로 C₁ ~ C₃의 알킬기, 수소원자, 하이드록시기 또는

(화학식 Y)일 수 있고, a는 1 ~ 100인 정수일 수 있다.
Further, at least one of A ₁ , A ₂ and A ₃ in the general formula (3)

(X), A ₁ , A _2, and A ₃ contained in the polymer of Formula X are each independently a C ₁ -C ₃ alkyl group, a hydrogen atom, a hydroxyl group,

(Formula Y), and a may be an integer from 1 to 100. [

The polymer of formula (3) covalently bonded to the polyamide layer of the present invention may further comprise a polymer represented by formula (X) in the polymer, and the polymer represented by formula (X) may further comprise a polymer represented by formula , In this case, the polyamide layer covalently bonded to the polymer represented by the general formula (3) can form denser pores and thus can have a higher boron removal rate.

However, depending on the degree of polymerization, the polymer of formula (3) may have a molecular weight distribution in a wide range, preferably a molecular weight of 300 to 200,000 u (daltons), and if the molecular weight is less than 300 u, The improvement of the boron removal rate may be deteriorated. If the molecular weight exceeds 200,000 u, there may be a problem that the density of pores is excessive and the water permeability is lowered.

According to a preferred embodiment of the present invention, the polymer represented by Formula 3 may be a polymer represented by Formula 5 below.

[Chemical Formula 5]

이고, r은 1 ~ 100인 정수일 수 있다. 상기 알킬기의 탄소수와 r의 범위에 대한 임계적 의의는 상술한 바와 동일한 바, 생략한다. In the general formula (5), A ₇ represents a C ₁ -C ₃ alkyl group, a hydrogen atom, a hydroxyl group or

And r may be an integer of 1 to 100. The critical meaning of the number of carbon atoms of the alkyl group and the range of r is the same as described above.

When the polymer represented by the formula (5) is contained on the surface of the polyamide layer of the present invention, it is possible to obtain a better boron removal rate and water permeability as compared with the case of containing other polymers, and also excellent in stain resistance and durability An improved reverse osmosis membrane can be provided.

(화학식 Z)일 수 있고, 화학식 Z의 A₇은 C₁ ~C₃의 알킬기, 수소원자, 하이드록시기 또는

이고, r은 1 ~ 100인 정수일 수 있으며, 화학식 Z의 A₇이

일 경우 중합도가 증가하여 기공의 크기가 조밀해지고 보론제거율이 더 향상될 수 있으며, 바람직하게는 상기 화학식 7로 표시되는 중합체의 분자량은 300 ~ 200,000 u(달톤)일 수 있다.
The A ₇ contained in the polymer of formula (5)

(Formula Z) can be one, of the formula Z A ₇ is C ₁ ~ C ₃ alkyl group, a hydrogen atom, a hydroxyl group or

, R may be an integer of 1 to 100, and A ₇ of formula

, The degree of polymerization may be increased to increase the pore size and further improve the boron removal rate. Preferably, the molecular weight of the polymer represented by the above formula (7) may be 300 to 200,000 u (daltons).

Next, the polymer represented by the general formula (4) will be described.

이며, 여기서, B₁, B₂ 및 B₃는 각각 독립적으로 C₁ ~ C₃의 알킬기, 수소원자, 하이드록시기 또는

(이하, 화학식 P라고 함)일 수 있다. The polymer represented by the general formula (4)

Wherein B ₁ , B ₂ and B ₃ are each independently a C ₁ to C ₃ alkyl group, a hydrogen atom, a hydroxyl group or

(Hereinafter referred to as the chemical formula P).

In this case, b in the formula (4) may be an integer of 1 to 100, and if b is more than 100, there may be a problem that a polymer having a desired molecular weight can not be obtained.

In addition, any one or more of B ₁ , B ₂ and B ₃ in Formula 4 may be a C ₁ -C ₃ alkyl group, more preferably a methyl group, and in this case, it may have a better boron removal ability.

Further, at least one of B ₁ , B ₂ and B ₃ in Chemical Formula 4 may be a hydrogen atom, but preferably all of B ₁ , B ₂ and B ₃ in Chemical Formula 4 may not be a hydrogen atom. If all of B ₁ , B ₂ and B ₃ are hydrogen atoms, the hydrophilicity may be lowered compared with the case where the hydrogen atoms are not bonded to each other, the water permeability may be reduced, and the polymerization may not be properly performed, .

(화학식 P)일 경우, 상기 화학식 P의 중합체에 포함되는 B₁, B₂ 및 B₃는 각각 독립적으로 C₁ ~ C₃의 알킬기, 수소원자, 하이드록시기 또는

(화학식 Q)일 수 있고, b는 1 ~ 100인 정수일 수 있다.
Further, any one or more of B ₁ , B ₂ and B ₃ in the general formula (4)

(P), B ₁ , B ₂ and B ₃ contained in the polymer of the formula (P) are each independently a C ₁ to C ₃ alkyl group, a hydrogen atom, a hydroxyl group or

(Formula (Q)), and b may be an integer of 1 to 100.

The polymer of formula (4) covalently bonded to the polyamide layer of the present invention may contain a polymer represented by formula (Q) in the same manner as the polymer of formula (3), and the polymer represented by formula (P) And in this case, the polyamide layer covalently bonded to the polymer represented by the formula (4) can form denser pores, and thus can have a higher boron removal rate.

However, depending on the degree of polymerization, the polymer of formula (4) may have a molecular weight distribution in a wide range, preferably a molecular weight of 300-200,000 u (daltons). If the molecular weight is less than 300 u, The improvement of the boron removal rate may be deteriorated. If the molecular weight exceeds 200,000 u, there may be a problem that the density of pores is excessive and the water permeability is lowered.

On the other hand, the polymer represented by the above-mentioned formulas (3) and (4) can be bonded to the hydrophilic acrylic polymer bonded to the polyamide layer. Among them, the polymer represented by the formula (3), more preferably the polymer represented by the formula Covalently bonded reverse osmosis membranes can exhibit better water permeability and boron removal rate.

In addition, the reverse osmosis membrane according to the present invention may contain a halogen atom in addition to any one or more of the polymers represented by the above formulas (3) and (4) covalently bonded to the surface of the polyamide layer. Specifically, the nitrogen atom and the halogen atom of the amide group contained in the polyimide layer may be covalently bonded. More specifically, FIG. 1 is a graph of X-ray photoelectron spectroscopy (XPS) of halogen atoms present on the surface of a reverse osmosis membrane according to a preferred embodiment of the present invention. As shown in the graph, Can be confirmed.

Since the reverse osmosis membrane according to the present invention has both good water permeability and boron removal rate, it has been found that a permeation flow rate of 12 gfd or more and a boron removal rate of 91% or more at 25 ° C and 800 psi pressure at an aqueous solution containing 32,000 ppm sodium chloride and 5 ppm boron Lt; / RTI >

Also, since there is excellent stain resistance, the flow rate reduction rate is only 5% or less after the operation at 25 DEG C and 800 psi pressure for 2 hours in the 25 ppm maintenance powder aqueous solution, which is remarkably excellent in stain resistance as compared with the conventional reverse osmosis membrane.

Meanwhile, the present invention includes a reverse osmosis module including a reverse osmosis membrane according to the present invention.

As a non-limiting example, the reverse osmosis membrane may be wound into a porous permeable effluent tube in a spiral wound with spacers for flow path formation, and the amount of wound membrane And an end cap for shape stability of the membrane wound on the end. The material, shape, and size of the spacer and end cap can be spacers and end caps used in conventional reverse osmosis modules. The reverse osmosis membrane thus wound may be housed in an outer case, and the material, size, and shape of the outer case may be the material, size, and shape of the outer case used in a conventional reverse osmosis module.

In addition, the reverse osmosis membrane thus wound can be wrapped using fiber reinforced plastics (FRP) or the like instead of the outer case.

Specifically, FIG. 2 is an exploded perspective view of a reverse osmosis module according to a preferred embodiment of the present invention, in which a reverse osmosis membrane 22 is wound around a reverse osmosis production water inlet pipe 20 in a twisted manner and included in the outer case 30 At this time, the produced water can be introduced into the pipe through the hole 21 formed in the inlet pipe 20.

The present invention will now be described more specifically with reference to the following examples. However, the following examples should not be construed as limiting the scope of the present invention, and should be construed to facilitate understanding of the present invention.

[ Example ]

< Example  1>

A solution of 18% by weight of dimethylformamide and polysulfone was cast on a polyester nonwoven fabric (100 탆) to a thickness of about 145 탆. Immediately, this was immersed in distilled water at 25 캜 for phase transformation and then a nonwoven reinforced polysulfone microporous substrate After sufficiently washing with water, the solvent in the substrate was replaced with water and then stored in pure water at room temperature. Thereafter, the surface water layer was removed by a compression method after immersing in a 1,4-metaphenylenediamine aqueous solution having a concentration of 3.5% by weight for 1 minute. This substrate was immersed in an organic solution containing 0.08% by weight of trimethoyl chloride and 0.114% by weight of isophthaloyl chloride for 1 minute, followed by interfacial polymerization, followed by natural drying at room temperature (25 ° C) for 1 minute and 30 seconds, To form a polyamide layer. The membrane with the polyamide layer formed was immersed in a 0.002M aqueous solution of potassium iodide (KI) at 60 DEG C for 2 minutes and then washed in distilled water at 60 DEG C for 2 minutes. The washed membranes were immersed in a solution 1 at 60 ° C for 1 minute and then washed in distilled water at 60 ° C for 1 minute to prepare a reverse osmosis membrane.

* Preparation of solution 1.

0.01 g of copper chloride (CuCl) and 0.018 g of 4,4'-dimethyl-2,2'-dipyridyl (DMDP) were dissolved in ethanol to make a total of 10 g of solution (a). 2 g of the solution (a) was added to 1 L of an aqueous solution containing 0.002 M of a monomer represented by the following formula (6) having a molecular weight of 360, followed by stirring at 60 캜 for 1 hour or longer to prepare solution 1.

[Chemical Formula 6]

< Example  2>

Except that the concentration of the potassium iodide aqueous solution was changed to 0.001M instead of 0.002M, the concentration of the monomer represented by the formula 6 in the solution 1 was changed to 0.001M instead of 0.002M, (a) was changed to 1 g instead of 2 g to prepare a reverse osmosis membrane.

< Example  3>

The reverse osmosis membrane was prepared in the same manner as in Example 1 except that the aqueous solution of potassium iodide and the solution 1 were changed to 25 ° C instead of 60 ° C.

< Example  4>

The reverse osmosis membrane was prepared in the same manner as in Example 1 except that sodium hypochlorite (NaOCl) aqueous solution was used instead of potassium iodide aqueous solution.

< Example  5 to 6>

Except that the monomers of Formula 7 (molecular weight 345) and Formula 8 (molecular weight 500) were added in place of the monomer of Formula 6 contained in Solution 1 to prepare a reverse osmosis membrane.

(7)

[Chemical Formula 8]

< Example  7>

Except that the concentration of the monomer represented by the formula 6 in the solution 1 was changed to 0.00005M instead of 0.002M and 0.5g was added instead of 2g of the solution (a) to prepare a reverse osmosis membrane .

< Example  8>

Except that the concentration of the monomer represented by the formula 6 in the solution 1 was changed to 1.2 M instead of 0.002 M and 120 g of the solution (a) was added instead of 2 g to prepare a reverse osmosis membrane Respectively.

< Comparative Example  1>

Except that a polyamide layer alone was formed on the polymer support layer, and a reverse osmosis membrane was prepared without being immersed in the aqueous solution of potassium iodide and the solution 1.

< Comparative Example  2>

The membrane having the polyamide layer formed on the polymer support layer was immersed in an aqueous solution containing 0.002M of the monomer represented by the formula 6 at 60 ° C for 1 minute, The reverse osmosis membrane was prepared by binding the monomer of the above formula (6) by a crosslinking treatment method of immersing in a glutaraldehyde solution for 30 seconds and washing with distilled water.

< Experimental Example  1>

The membrane performance of the reverse osmosis membrane manufactured through the above Examples and Comparative Examples was evaluated and shown in Table 1 below.

At this time, the membrane performance of the reverse osmosis membrane was measured at a concentration of 32,000 ppm of sodium chloride (NaCl) and 5 ppm of boron aqueous solution at 25 ° C. and 800 psi, and the boron concentration was measured by using an emission spectrophotometer (ICP). The measurement wavelength range is 400 to 880 nm and the measurement error is within 1 nm.

< Experimental Example  2>

The antifouling performance of the reverse osmosis membrane of Example 1 and Comparative Example 1 was evaluated and shown in Table 2 below.

At this time, the pollution resistance performance was evaluated by measuring the flow rate and the salt rejection rate after the operation at 25 ° C and 800 psi pressure for 2 hours in the aqueous solution of 25ppm oil retention powder and comparing it with the flow rate and salt rejection rate measured in Experimental Example 1, Reduction rate was calculated.

< Experimental Example  3>

The reverse osmosis membrane prepared in Example 1 was analyzed by X-ray photoelectron spectroscopy (XPS) to determine whether or not the surface of the reverse osmosis membrane contained halogen atoms. The results are shown in FIG.

Specifically, as can be seen from FIG. 1, a peak indicating an iodine atom can be confirmed on the XPS graph. As a result, it can be seen that the iodine atom exists on the surface of the reverse osmosis membrane of Example 1.

Flow rate (gfd) Salt exclusion rate (%) Boron removal rate (%) Example 1 13.92 99.53 92.39 Example 2 13.52 99.45 91.72 Example 3 16.67 99.42 87.03 Example 4 19.31 99.24 84.35 Example 5 14.22 99.32 88.52 Example 6 12.98 99.44 89.98 Example 7 17.18 99.20 84.12 Example 8 13.23 99.34 90.54 Comparative Example 1 18.05 99.33 83.36 Comparative Example 2 12.85 99.25 87.68

Specifically, as shown in Table 1, it can be confirmed that the boron removal rate of Example 4 using sodium hypochlorite as the halogen compound was lower than that of Example 1 using potassium iodide.

In Example 5 using the monomer of Formula 7 as the hydrophilic monomer, the flow rate was somewhat improved as compared with Example 1, but the boron removal rate was remarkably lowered. In Example 6 using the monomer of Formula 8 as the hydrophilic monomer, It can be confirmed that the removal rate was significantly lower than that of Example 1.

Further, in Example 7, the flow rate was significantly increased as compared with Example 1, but the boron removal rate was significantly reduced as compared with Example 1, and in Example 8, the boron removal rate and the salt removal rate were decreased as compared with Example 1 have.

In addition, in Comparative Example 2 using glutaraldehyde, which is a crosslinking agent, it is confirmed that the boron removal performance is significantly lower than that in Examples.

Before the maintenance powder input After 2 hours of maintenance powder input Flow rate (gfd) Salt exclusion rate (%) Flow rate (gfd) Salt exclusion rate (%) Flow rate reduction (%) Example 1 13.92 99.53 13.26 99.6 4.74 Comparative Example 1 18.05 99.33 15.77 99.4 12.63

Specifically, in Table 2, the reverse osmosis membrane of Example 1 showed that the flow rate reduction rate was only 4.74% even after the addition of the fat powder, whereas in Comparative Example 1, the flow rate reduction rate was 12.63% The reverse osmosis membrane of Example 1 is superior to the reverse osmosis membrane of Comparative Example 1 in that the stain resistance is excellent, and the results of Table 1 show that the reverse osmosis membrane of the present invention exhibits remarkably superior boron removal performance It can be seen that it is excellent.

Claims (18)

(1) treating the polymer solution on the support to form a polymer support layer;
(2) immersing the polymer support layer in an aqueous solution containing a polyfunctional amine, and then contacting the polymer support layer with an organic solution containing a polyfunctional acid halide compound to form a polyamide layer;
(3) reacting the polyamide layer with a solution containing a halogen compound; And
(4) reacting the polyamide layer with a precursor solution containing a hydrophilic acrylic monomer to bind a polymer containing a hydrophilic acrylic monomer to the polyamide layer. The method according to claim 1, wherein the polymer solution in step (1) is selected from the group consisting of a polysulfone polymer, a polyamide polymer, a polyimide polymer, a polyester polymer, an olefin polymer, polyvinylidene fluoride and polyacrylonitrile Wherein the at least one polymeric material is selected from the group consisting of polyvinylidene fluoride (PVDF) and polyvinylidene fluoride (PVDF). The method according to claim 1, wherein the halogen compound in step (3) comprises at least one selected from the group consisting of a halogen acid, a hypohalogen acid, a metal salt of a halogen acid, a metal salt of a hypohalous acid, a halogen complex, and a metal halide And removing the boron from the solution. The method of claim 1, wherein the step (3) comprises treating a polyamide layer with a solution containing 0.01 to 1% by weight of a halogen compound. The method of claim 1, wherein the hydrophilic acrylic monomer in step (4) comprises at least one of compounds represented by the following formulas (1) and (2).
[Chemical Formula 1]

Wherein R ₁ and R ₂ are each independently a C ₁ -C ₃ alkyl group, a hydrogen atom or a hydroxyl group, and a is an integer of 1 to 100.
(2)

Wherein R ₃ and R ₄ are each independently a C ₁ -C ₃ alkyl group, a hydrogen atom or a hydroxyl group, and a is an integer of 1 to 100. The method of claim 1, wherein the step (4) comprises treating the polyamide layer with a precursor solution containing 0.0001 to 1 M of a hydrophilic acrylic monomer. The method of claim 1, wherein the step (4) comprises a transition metal compound as a catalyst, and the transition metal compound is contained in a molar ratio of 1: 0.01 to 1 based on the hydrophilic acrylic monomer. Gt; 8. The process according to claim 7,
_{CuCl, CuBr, CuBr 2, CuCl} 2, CuCl 2 · 2H 2 O, FeCl 3, FeCl 2, FeCl 3 · 6H 2 O, FeBr 2, FeBr 3, [Fe (CpCl 2)] n ( where n is 1 to 4 is an _{integer), RuCl 2 (PPh 3)} 2, RuCl 3 X · H 2 O ( where X is F, Cl, Br, aryl phosphine pinim) of C _{1 ~ 10} alkyl phosphine or C _{6 ~ 20} of, Ru _{[CpPPh 3 Cl 2], [} RuCpCl 2] n ( where, n is 1-4 integer and, Cp is cyclopentadienyl _{nilim), RuCl 3, NiBr 2,} NiCl 2, Fe (OAc) 2, Ru [CpCl ₂ ] ₃ , NiCl ₂ (PPh ₃ ) ₂ and NiBr ₂ (PPh ₃ ) ₂ ; And
N, N, N &apos;, N &apos;, N &apos;, N '',N''- pentamethyldiethylenetriamine, 4,4'-dimethyl-2,2'-dipyridyl, N, N, N', N'-tetramethylethylenediamine, 2,2'- Amino-3-methyl-5-nitropyridine, 2-diphenylphosphino-2 '- (N, N'-dimethylamino ) Biphenyl, 2 - [(diphenylphosphino) methyl] pyridine, 9,9-dimethyl-4,5-bis (diphenylphosphino) (2-picolyl) amine, hexamethylphosphoramide, N, N'-dimethylethylenediamine, N, N'- Dimethylthiophene-2-methylamine, triphenylphosphate, trimethylphosphite, trimethylphosphate, triphenylphosphite, imino-tris (dimethylamino) phosphore , Bis (diphenylphosphino) benzaldehyde, 1,4,8,11-tetramethyl-1,4,8,11-tetraazacyclotetradecane, 1,3-bis (diphenylphosphino) (Diphenylphosphino) methane, ethylenebis (diphenylphosphine), tri-t-butylphosphine, diphenyl (2-methoxyphenyl) phosphine and 2-pyridinethioamide A ligand-bound compound;
Wherein the boron removal is performed at a temperature higher than the boiling point of the reverse osmosis membrane. The method of claim 1, wherein the step (4) is performed at a temperature of 30 to 80 ° C for 0.5 to 10 minutes. A support;
A polymeric support layer formed on at least one side of the support;
A polyamide layer formed on the polymer support layer; And
And a hydrophilic acrylic polymer bonded to the polyamide layer. The reverse osmosis membrane according to claim 10, wherein the hydrophilic acrylic polymer comprises at least one polymer selected from the group consisting of polymers represented by the following formulas (3) and (4).
(3)

In Formula 3, A ₁ , A _2, and A ₃ are each independently a C ₁ -C ₃ alkyl group, a hydrogen atom, a hydroxyl group,

And a is an integer of 1 to 100.

[Chemical Formula 4]

In Formula 4, B ₁ , B _2, and B ₃ are each independently a C ₁ to C ₃ alkyl group, a hydrogen atom, a hydroxyl group,

And b is an integer of 1 to 100. 11. The method of claim 10, wherein the polymer support layer is selected from the group consisting of a polysulfone polymer, a polyamide polymer, a polyimide polymer, a polyester polymer, an olefin polymer, polyvinylidene fluoride, and polyacrylonitrile The reverse osmosis membrane having excellent boron removal performance, which comprises at least one polymer material. The reverse osmosis membrane according to claim 10, wherein the reverse osmosis membrane contains a halogen atom covalently bonded to the polyamide layer. The reverse osmosis membrane according to claim 11, wherein the polymer represented by the formula (3) is a polymer represented by the following formula (5).
[Chemical Formula 5]

In the general formula (5), A ₇ represents a C ₁ -C ₃ alkyl group, a hydrogen atom, a hydroxyl group or

And r is an integer of 1 to 100. The reverse osmosis membrane according to claim 11 or 14, wherein the molecular weight of the polymer is 300 to 200,000 u (Dalton). The reverse osmosis membrane according to claim 10, wherein the reverse osmosis membrane has a permeate flow rate of 12 gfd or more and a boron removal rate of 91% or more at 25 ° C and 800 psi pressure in an aqueous solution containing 32,000 ppm sodium chloride and 5 ppm boron, . 11. The reverse osmosis membrane according to claim 10, wherein the reverse osmosis membrane has a flow rate reduction rate of 5% or less after being operated for 2 hours at 25 DEG C and 800 psi pressure in an aqueous 25 ppm holding powder solution. A reverse osmosis module comprising a reverse osmosis membrane according to claim 10.

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