KR102363625B1 - The organic-inorganic composite electrolyte membrane and an application product including the membrane - Google Patents

Abstract

The present invention relates to an organic/inorganic reinforced composite electrolyte membrane and a method for manufacturing the same, and more particularly, an organic/inorganic reinforced composite having low permeability by generating silica particles while crosslinking an organic polymer and an inorganic polymer impregnated in a porous support. It relates to an electrolyte membrane, a method for manufacturing the same, and an applied product including the membrane.

Description

The organic-inorganic composite electrolyte membrane and an application product including the membrane

The present invention relates to an organic/inorganic reinforced composite electrolyte membrane and a method for manufacturing the same, and more particularly, an organic/inorganic reinforced composite having low permeability by generating silica particles while crosslinking an organic polymer and an inorganic polymer impregnated in a porous support. It relates to an electrolyte membrane, a method for manufacturing the same, and an applied product including the membrane.

Recently, along with the leveling of the power load and the expansion of the proportion of renewable energy generation, the development of an energy storage device for storing and managing power energy is urgently required.

A vanadium redox flow battery, which is a type of energy storage device, is attracting attention as a large-capacity long-cycle energy storage device because it is possible to design the capacity and output individually, so that it is easy to increase the capacity. In the vanadium redox flow battery, the polymer electrolyte membrane is a very important core component that determines the output and long-term performance of the battery and the price of the stack. acting as a factor. Accordingly, there is a need to develop a low-permeability and low-cost polymer electrolyte membrane capable of increasing the efficiency of an energy storage device.

As a separator used in a vanadium redox flow battery, DuPont's Nafion is commercially sold, but since it is expensive and has high permeability, there was a difficulty in long-term operation of the redox flow battery.

In order to replace Nafion, which has such a problem, various types of polymer electrolyte membranes such as hydrocarbon-based polymer membranes and reinforced composite membranes have been developed. Specifically, the hydrocarbon-based polymer membrane is typically sulfonated polyether ketone, sulfonated polyether-ether ketone, sulfonated polyether sulfone, sulfonated polysulfone, sulfonated polyphenylene sulfide, sulfonated polyphenylene oxide, and sulfonated polyether. Mead and the like have been proposed, but there is a problem in that flexibility is low and chemical stability is weak.

In addition, a reinforced composite membrane has been proposed as a method of manufacturing an ionomer excellent in ion conductivity by introducing an ionomer excellent in ion conductivity to a porous support having excellent mechanical strength and durability, but there is a disadvantage in that desorption occurs between the porous support and the ionomer.

Accordingly, there is a need to develop a technology capable of solving these problems.

Patent Publication No. 10-2018-0003098

As a result of numerous studies, the present inventors have completed the present invention by impregnating an organic/inorganic polymer into a porous support to develop an organic/inorganic reinforced composite electrolyte membrane having low permeability characteristics.

Therefore, it is an object of the present invention to secure excellent dimensional stability through a porous support and at the same time to impregnate an organic/inorganic polymer having a functional group capable of ion conduction into an inexpensive porous support, thereby reducing the cost of the polymer electrolyte membrane. To provide a reinforced composite electrolyte membrane and a method for manufacturing the same.

Another object of the present invention is to generate silica particles as an organic polymer and an inorganic polymer impregnated in a porous support are cross-linked to provide ion conductivity and at the same time suppress the permeation of an active material, thereby significantly improving the low permeability properties compared to the existing reinforced composite electrolyte membrane and An object of the present invention is to provide an organic/inorganic reinforced composite electrolyte membrane capable of implementing ionic conductivity and a method for manufacturing the same.

Another object of the present invention is to form a hydrophilic polymer coating layer on a porous support first, and then proceed with impregnation with organic/inorganic polymer to have excellent bonding strength between the porous support and the organic/inorganic polymer layer. An organic/inorganic reinforced composite electrolyte membrane and To provide a manufacturing method thereof.

Another object of the present invention is to provide an energy storage device and a water treatment device advantageous for long-term operation by including an organic/inorganic reinforced composite electrolyte membrane having characteristics of low cost and low permeability.

The object of the present invention is not limited to the object mentioned above, and even if not explicitly mentioned, the object of the invention that can be recognized by a person of ordinary skill in the art from the description of the detailed description of the invention to be described later may also be included. .

In order to achieve the object of the present invention described above, the present invention is a porous polymer support; a hydrophilic polymer impregnated layer formed on all surfaces of the polymer support exposed to the outside, including pores of the polymer support; an organic/inorganic polymer impregnated layer formed on the hydrophilic polymer impregnated layer; and upper and lower organic/inorganic polymer layers respectively formed on the lower surface and the organic/inorganic polymer impregnated layer formed on the lower surface and the upper surface of the porous polymer support; provides an organic/inorganic reinforced composite electrolyte membrane comprising.

In a preferred embodiment, the organic/inorganic polymer impregnated layer and the upper and lower organic/inorganic polymer layers include a cross-linked structure of an inorganic polymer material and an organic polymer material, and nano-silica particles uniformly dispersed in the cross-linked structure. do.

In a preferred embodiment, the organic/inorganic polymer impregnated layer and the upper and lower organic/inorganic polymer layers contain an inorganic polymer material and an organic polymer material in a weight ratio of 0.01:19.99 to 19.99:0.01.

In a preferred embodiment, the inorganic polymer material is selected from the group consisting of DM-SP, D-SP (Diol Silica Precursor), BD-SP (Bisphenol Dimethylbenzanthracene SP), BDP-SP (Bisphenol Dimethylbenzanthracene Polydimethylsiloxane SP), and combinations thereof. whichever one is chosen.

In a preferred embodiment, the organic polymer material is Nafion (DuPont), 3M Ionomer (3M), Fumion (Fumatech), Aciplex (Asahi Chemical), Aquivion (Solvay), sulfonated perfluorinated polymer (PFSA, perfluorinated) sulfonic acid), polytetrafluoroethylene, polyvinylidene fluoride, polyvinyl fluoride, polyvinylidene fluorocoperfluorinated alkylvinyl ether, and any one selected from the group consisting of combinations thereof.

In a preferred embodiment, the porous polymer support is made of polyethylene or polyethylene containing hydrophilic silica.

In a preferred embodiment, the porous support comprises pores having a diameter in the range of 5 nm to 100 nm.

In a preferred embodiment, the hydrophilic polymer is at least one selected from the group consisting of polydopamine, polyethylene glycol and polyvinyl alcohol.

In addition, the present invention provides a redox flow battery comprising any one of the above-described organic / inorganic reinforced composite electrolyte membrane.

In addition, the present invention provides a water treatment device including any one of the above-described organic / inorganic reinforced composite electrolyte membrane.

The present invention described above has the following effects.

First, according to the organic/inorganic reinforced composite electrolyte membrane and the method for manufacturing the membrane of the present invention, by impregnating an organic/inorganic polymer in which a functional group capable of ion conduction is introduced into a low-cost porous support while ensuring excellent dimensional stability through a porous support. It is possible to reduce the cost of the polymer electrolyte membrane.

In addition, according to the organic/inorganic reinforced composite electrolyte membrane of the present invention and its manufacturing method, the organic polymer and the inorganic polymer impregnated in the porous support are cross-linked to form silica particles to impart ionic conductivity and at the same time suppress the permeation of the active material. It is possible to realize significantly improved low permeability and ionic conductivity compared to the reinforced composite electrolyte membrane.

In addition, according to the organic/inorganic reinforced composite electrolyte membrane of the present invention and its manufacturing method, a hydrophilic polymer coating layer is first formed on a porous support and then impregnated with organic/inorganic polymers to provide excellent binding force between the porous support and the organic/inorganic polymer layer. has

In addition, the energy storage device and water treatment device of the present invention include an organic/inorganic reinforced composite electrolyte membrane having characteristics of low cost and low permeability, which is advantageous for long-term operation and is excellent in economic feasibility.

These technical effects of the present invention are not limited only to the above-mentioned range, and even if not explicitly mentioned, the effects of the invention that can be recognized by those of ordinary skill in the art from the description of the specific content for the implementation of the invention to be described later of course included

1 is a graph showing FT-IR results of organic/inorganic reinforced composite electrolyte membranes according to embodiments of the present invention.
2 is a graph showing the results of measuring the moisture content of the organic / inorganic reinforced composite electrolyte membrane according to the embodiments of the present invention.
3 is a graph showing the results of measuring the dimensional stability of the organic / inorganic reinforced composite electrolyte membrane according to other embodiments of the present invention.
4 is a graph showing the ionic conductivity measurement results of the organic/inorganic reinforced composite electrolyte membrane according to embodiments of the present invention.

The terms used in the present invention are only used to describe specific embodiments, and are not intended to limit the present invention. The singular expression includes the plural expression unless the context clearly dictates otherwise. In the present application, terms such as “comprise” or “have” are intended to designate that a feature, number, step, operation, component, part, or combination thereof described in the description of the invention exists, but is not limited to one or more other It is to be understood that this does not preclude the possibility of addition or presence of features or numbers, steps, operations, components, parts, or combinations thereof.

Terms such as first, second, etc. may be used to describe various elements, but the elements should not be limited by the terms. The above terms are used only for the purpose of distinguishing one component from another. For example, without departing from the scope of the present invention, a first component may be referred to as a second component, and similarly, a second component may also be referred to as a first component.

Unless defined otherwise, all terms used herein, including technical and scientific terms, have the same meaning as commonly understood by one of ordinary skill in the art to which this invention belongs. Terms such as those defined in commonly used dictionaries should be interpreted as having meanings consistent with the meanings in the context of the related art, and should not be interpreted in an ideal or excessively formal meaning unless explicitly defined in the present invention. does not

In interpreting the components, it is construed as including an error range even if there is no separate explicit description. In particular, when the terms "about", "substantially", etc. of degree are used, they may be construed as being used in a sense at or close to the numerical value when manufacturing and material tolerances inherent in the stated meaning are presented. .

In the case of a description of a temporal relationship, for example, 'after', 'following', 'after', 'before', etc., when temporal precedence is described, 'immediately' or 'directly' Unless ' is used, cases that are not continuous are included.

Hereinafter, the technical configuration of the present invention will be described in detail with reference to the accompanying drawings and preferred embodiments.

However, the present invention is not limited to the embodiments described herein, and like reference numerals indicate like elements in different forms.

The technical feature of the present invention is that it is possible to reduce the cost of the polymer electrolyte membrane as well as reduce the cost of the polymer electrolyte membrane by impregnating the low-cost porous support with organic/inorganic polymers introduced with functional groups capable of ion conduction while ensuring excellent dimensional stability through the porous support. Organic and inorganic polymers are crosslinked to form silica particles to provide ionic conductivity while at the same time suppressing the permeation of active materials to realize significantly improved low permeability and ionic conductivity compared to existing reinforced composite electrolyte membranes. Organic/inorganic reinforced composite electrolyte A membrane and a method for manufacturing the same.

Accordingly, the organic/inorganic reinforced composite electrolyte membrane of the present invention includes: a porous polymer support; a hydrophilic polymer impregnated layer formed on all surfaces of the polymer support exposed to the outside, including pores of the polymer support; an organic/inorganic polymer impregnated layer formed on the hydrophilic polymer impregnated layer; and upper and lower organic/inorganic polymer layers respectively formed on the lower surface and the organic/inorganic polymer impregnated layer formed on the upper surface of the porous polymer support.

In particular, in the organic/inorganic reinforced composite electrolyte membrane of the present invention, the hydrophilic polymer impregnated layer has excellent binding force between the porous polymer support and the organic/inorganic polymer, which is an ion transport material, and the organic/inorganic polymer impregnated layer and upper and lower organic/inorganic In the polymer layer, the silica particles generated when the cross-linked structure is formed by the condensation reaction of the organic polymer and the inorganic polymer are homogeneously distributed. can

In the present invention, the porous polymer support may be any porous polymer known in the form of a membrane, but as an embodiment, it may be any one selected from the group consisting of porous polyethylene and porous polyethylene including hydrophilic silica. The porous polymer support may have a plurality of pores having a diameter in the range of 5 nm to 100 μm, but if the diameter of the pores is less than 5 nm, it is difficult to form an ion conductive channel, and if it exceeds 100 μm, it is difficult to control the transmittance. The optimal pore size included in the polymer support was determined. In addition, the porosity is not particularly limited, but may be in the range of 30 to 80%. That is, if the porosity of the porous polymer support is less than 30%, it is difficult to coat the ion conductive material, and at the same time, the ion conductivity property may be reduced due to the small amount of the ion conductive material, and if it exceeds 80%, the porous polymer This is because not only cannot maintain the mechanical strength of the support itself, but also the mechanical strength, which is an excellent property of the existing reinforced composite membrane, may decrease when an ion conductive material is coated.

The hydrophilic polymer impregnated layer is to impart hydrophilicity to the porous polymer support and is formed by impregnating the porous polymer support in a hydrophilic polymer solution. As the hydrophilic polymer, any known hydrophilic polymer may be used, but as an embodiment, any one or more selected from the group consisting of polydopamine, polyethylene glycol, polyvinyl alcohol, and combinations thereof may be used. In particular, since the organic/inorganic polymer impregnated layer is formed as an ion transport layer on the hydrophilic polymer impregnated layer formed on the porous polymer support, there is no need to perform a separate process of replacing the hydrophilic functional group with the ionic functional group. Due to the layer, the interfacial bonding force between the porous polymer support and the ion transport layer is very strong, so that hydration stability can be improved as will be described later. As an embodiment, polydopamine can be used as a hydrophilic polymer because dopamine is a hydrophilic material and has strong adhesive properties. In this case, dopamine chloride is added to distilled water and stirred, and then Tris (hydroxymethyl) aminomethane is added to the stirred solution and stirred. Thus, a hydrophilic polymer solution can be obtained.

The organic/inorganic polymer impregnation layer and the upper and lower organic/inorganic polymer layers improve hydrogen ion conductivity while significantly lowering the permeability of other active ions to secure low permeability. It can be included in a weight ratio of 19.99:0.01, and the set range is experimentally determined, and when the inorganic polymer material is included in excess of the set weight ratio, the permeability is lowered due to the formed silica particles, but there is a problem in that the hydrogen ion conductivity is lowered, and the set weight ratio When the inorganic polymer material was introduced with less than

In the present invention, all known silane-based polymers may be used as the inorganic polymer material, but as an embodiment, DM-SP, D-SP (Diol Silica Precursor), BD-SP (Bisphenol Dimethylbenzanthracene SP), BDP-SP (Bisphenol) Dimethyl benzanthracene Polydimethylsiloxane SP) and any one or more selected from the group consisting of combinations thereof, the weight average molecular weight (Mm) may be 50 ~ 　5000 g / mol. This is because, when the weight average molecular weight of the silane-based polymer is less than or exceeding the set range, many difficulties may occur due to a long time when dissolved in an organic solvent or crosslinking occurs in the polymer.

The organic polymer material is also not particularly limited as long as it is a polymer capable of ion exchange with cation conductivity or anion conductivity, and any known organic polymer may be used. Ionomer (3M), Fumion (Fumatech), Aciplex (Asahi Chemical), Aquivion (Solvay), sulfonated perfluorinated sulfonic acid (PFSA), polytetrafluoroethylene, polyvinylidene fluoride, polyvinylflo It may be any one or more selected from the group consisting of fluoride, polyvinylidene fluorocoperfluorinated alkylvinyl ether, and combinations thereof.

In addition, the organic / inorganic reinforced composite electrolyte membrane manufacturing method of the present invention comprises the steps of preparing a porous polymer support; a first impregnation step of impregnating the porous polymer support in a hydrophilic polymer solution to obtain a first impregnation-treated polymer support in which a hydrophilic polymer impregnated layer is formed on all surfaces exposed to the outside, including pores of the porous polymer support; a second impregnation step of impregnating the primary impregnation-treated polymer support with an organic/inorganic polymer solution to obtain a secondary impregnating-treated polymer support in which an organic/inorganic polymer impregnated layer is formed on the hydrophilic polymer impregnated layer; a film forming step of obtaining a precursor film in which an upper organic/inorganic polymer layer and a lower organic/inorganic polymer layer are respectively formed on the upper and lower surfaces of the secondary impregnated polymer support; and pre-treating the precursor film.

In the second impregnation step, the organic / inorganic polymer solution is prepared by the inorganic polymer solution; preparing an organic polymer solution; and mixing the inorganic polymer solution and the organic polymer solution in a weight ratio of 5:95 to 95:5.

At this time, the steps of preparing the inorganic polymer solution and the organic polymer solution may be performed in any order. The inorganic polymer solution and the organic polymer solution are individually prepared by completely dissolving the inorganic polymer material and the organic polymer material in the same solvent, respectively. do. Here, the mixing ratio of the solvent and the inorganic polymer or the organic polymer may be 1 to 70 parts by weight of each polymer based on 100 parts by weight of the solvent. The blending ratio is determined experimentally. If the weight of the polymer is less than 1 part by weight or exceeds 70 parts by weight, the viscosity is too low or high, so the workability is low, it is difficult to control the coating thickness, and it is difficult to inject the ion transport material into the pores of the support. Thus, the optimal solution concentration was experimentally established.

At this time, the solvent used for dissolving the inorganic polymer material and the organic polymer material can act to induce a uniform dispersion of the nano-silica formed in the condensation reaction of the cross-linking process by easily inducing the mixing of the two polymer solutions. have. Specifically, the solvent of the inorganic polymer solution and the organic polymer solution includes distilled water, ethanol, isopropanol, an alcoholic solvent including methanol; dimethyl sulfoxide; It may be any one or more selected from the group consisting of N,N-dimethylacetamide, N-methyl-2-pyrilidinone, N,N-dimethylformamide, and combinations thereof.

The organic/inorganic polymer solution is obtained by mixing the prepared inorganic polymer solution and the organic polymer solution in a certain ratio to prepare a homogeneous solution. In one embodiment, the inorganic polymer solution and the organic polymer solution are 0.5 parts by weight to 99.5 parts by weight: In the range of 99.5 parts by weight to 0.5 parts by weight, it is possible to configure the composition of the solution by mixing in various required mixing ratios. Meanwhile, the organic/inorganic polymer solution may be stirred for several minutes to several days in a reactor maintained at a temperature of 10 to 50 degrees to prepare a homogeneous phase.

The second impregnation step can be performed by maintaining a vacuum state after impregnating the first impregnation-treated polymer support in the organic/inorganic polymer solution. is to keep

The film forming step includes: casting an organic/inorganic polymer solution on a flat plate to form a lower organic/inorganic polymer layer; a lower layer forming step of placing the secondary impregnated polymer support on the lower organic/inorganic polymer layer, drying it, and peeling from the flat plate to obtain a primary precursor film having a lower organic/inorganic polymer layer; forming an upper organic/inorganic polymer layer by casting an organic/inorganic polymer solution on a flat plate; On the upper organic/inorganic polymer layer, the upper surface of the primary precursor film on which the lower organic/inorganic polymer layer is not formed is brought into contact, dried, and peeled from the flat plate to form the upper and lower organic/inorganic polymer layers and an upper layer forming step of obtaining a secondary precursor film. At this time, the casting may include all casting methods generally performed such as coating using a comma coater, spin coating, dip coating, slot die coating, or doctor blade coating, but in one embodiment, coating is performed using a doctor blade In particular, the lower organic/inorganic polymer layer and the upper organic/inorganic polymer layer may be formed by performing casting using separate plates. In addition, in the lower layer forming step and the upper layer forming step, the drying treatment is performed in a temperature range of 50 to 70 degrees in a vacuum state. Through this drying treatment, the organic polymer and the inorganic polymer are thermally cross-linked, and in the reaction process, silica Particles may be generated and uniformly distributed in the ion transport layer, that is, the organic/inorganic polymer impregnated layer and the upper and lower organic/inorganic polymer layers.

The pretreatment step is performed by immersing the secondary precursor membrane in a basic aqueous solution and then immersing it in distilled water, immersing it in an acidic aqueous solution, and then immersing it in distilled water. In one embodiment, the basic aqueous solution contains 1 to 30% H ₂ O ₂ aqueous solution, the acidic aqueous solution may be 0.05-5M H ₂ SO ₄ aqueous solution, and each process of the pretreatment step may be performed at 50° C. for 30 minutes.

Accordingly, in the organic/inorganic reinforced composite electrolyte membrane of the present invention, an ion transport layer is formed inside and on the surface of the pores of the porous polymer support, and a number of ion cross-links are formed inside the ion transport layer, while silica particles are formed from the inorganic polymer to form ions It has excellent conductivity as 0.064S/cm and transmittance is lowered to 2.00×10 ^-6 cm2/min or less. In addition, the organic/inorganic reinforced composite electrolyte membrane shows excellent dimensional stability of 2.2% due to the excellent durability of the porous polymer support.

As such, the organic/inorganic reinforced composite electrolyte membrane of the present invention can exhibit improved ionic conductivity by more than 100 times compared to the conventional support and can exhibit improved dimensional stability by more than 10 times compared to commercial membranes, so the organic/inorganic strengthening of the present invention It is possible to secure stable performance of energy storage devices and water treatment devices such as fuel cells, water electrolysis and secondary batteries (redox flow batteries) including a composite electrolyte membrane.

Example 1

1. Step of preparing a porous polymer support

A porous polymer support (PE separator) having a thickness of 150 μm was prepared with a horizontal × vertical size of 10 cm × 10 cm. At this time, the size of the pores was 33 nm, and the porosity was 67%. (BET measurement)

2. First impregnation step

① Preparation of hydrophilic polymer solution

Dopamine chloride was added to distilled water at a concentration of 1.5 g/L and stirred for 30 minutes. Tris (hydroxymethyl) aminomethane was added to the prepared solution at a concentration of 3.75 mM, and stirred for 10 minutes to dissolve the solution, thereby preparing a hydrophilic polymer solution.

② Impregnation step

The porous polymer support (PE separator) prepared in the prepared hydrophilic polymer solution was impregnated in a vacuum at room temperature for one day, washed with distilled water, and dried in a vacuum at 60 ° C. to obtain a first impregnation-treated polymer support with a hydrophilic polymer impregnated layer.

3. Second impregnation step

① Step of preparing inorganic polymer solution

①-1. Synthesizing Inorganic Polymers

14.8 g of DMBA and 34.8 g of TDI were completely dissolved in 100 mL of DMAC in a reaction flask at 60° C. and reacted for 12 hours. Then, 22.1 g of APTES was added and reacted at 50° C. for 8 hours to obtain a functional nanohybrid alkoxy silane precursor.

②-2. Step of preparing inorganic polymer solution

A sol-gel mixture was obtained by hydrolysis of the synthesized nanohybrid alkoxysilane functional precursor in an aqueous HCl solution of 0.1 M concentration, and then the sol-gel mixture was dispersed in DMAc to obtain a homogeneous D-SP polymer solution.

② Preparing the organic polymer solution

6 g of 3M ionomer and 24 g of DMAc were stirred on a hot-plate at 60° C. for 12 hours to obtain a 20 wt% organic polymer solution.

③ Mixing step

A homogeneous solution was prepared by variously mixing the prepared inorganic polymer solution and organic polymer solution in 5 parts by weight to 95 parts by weight: 95 parts by weight to 5 parts by weight, respectively. Specifically, the mixing ratio of the inorganic polymer solution and the organic polymer solution was 50:50, 25:75, 20:80, 10:90, and stirred at room temperature for 24 hours to prepare a homogeneous organic/inorganic polymer solution.

④ Impregnation step

The prepared organic/inorganic polymer solution was impregnated with the primary impregnation-treated porous polymer support in a vacuum at room temperature for one day, and the organic/inorganic polymer solution was added to the inside of the pores of the primary impregnated-treated porous polymer support on the hydrophilic polymer-impregnated layer. A secondary impregnation-treated polymer support on which an organic/inorganic polymer impregnated layer was formed was obtained.

4. Unveiling Stage

① Forming the lower organic/inorganic polymer layer

The organic/inorganic polymer solution prepared in the second impregnation step was cast on a glass plate at room temperature with a doctor blade to form a lower organic/inorganic polymer layer.

② Lower layer formation step

A secondary impregnation-treated polymer support was placed on the lower organic/inorganic polymer layer formed on the glass plate, and then dried in a vacuum oven at 60° C. for 24 hours. Thereafter, it was peeled from the glass plate to obtain a primary precursor film having a lower organic/inorganic polymer layer.

③ Upper layer formation step

To form the upper layer on the opposite side of the side where the lower organic/inorganic polymer layer is formed, the organic/inorganic polymer solution is cast on a new glass plate at room temperature with a doctor blade, and the lower organic/inorganic polymer layer of the primary precursor film is not formed thereon. After raising the upper surface to contact, dry in a vacuum oven at 60°C for 24 hours. Thereafter, it was peeled from the glass plate to obtain a secondary precursor film having upper and lower organic/inorganic polymer layers.

5. Pretreatment step

The secondary precursor film obtained in the film forming step was immersed in 3% H ₂ O ₂ aqueous solution and immersed in distilled water, then immersed in 0.5MH ₂ SO ₄ aqueous solution and immersed in distilled water again to perform pretreatment. Each process of the pretreatment step was performed at 50° C. for 30 minutes to finally obtain a protonated organic/inorganic reinforced composite electrolyte membrane 1.

Example 2

An organic/inorganic reinforced composite electrolyte membrane 2 was obtained in the same manner as in Example 1 except that the thickness of the porous polymer support was 65 μm.

Example 3

An organic/inorganic reinforced composite electrolyte membrane 3 was obtained in the same manner as in Example 1 except that 15 g of 3M ionomer and 15 g of DMAc were stirred in a hot-plate at 60° C. for 12 hours and a 50 wt% organic polymer solution was used.

Example 4

An organic/inorganic reinforced composite electrolyte membrane 4 was obtained in the same manner as in Example 2, except that 15 g of 3M ionomer and 15 g of DMAc were stirred on a hot-plate at 60° C. for 12 hours and a 50 wt% organic polymer solution was used.

Experimental Example 1

For the chemical structure analysis of the organic/inorganic reinforced composite electrolyte membranes prepared in Examples 1 and 2, a comparative analysis was performed by Fourier-transform infrared spectroscopy (FT-IR), and the results are shown in FIG. 1 .

As shown in FIG. 1 , CH bending vibration (1472 cm ^-1 ) and Si-O stretching (1012 cm ^-1 ) peaks of the PE separator as a support were observed in the organic/inorganic reinforced composite electrolyte membrane. In addition, the -OH functional group (3400 cm ^-1 ) peak and the C=O functional group (1720 cm ^-1 ) peak derived from the carbonyl group appeared, confirming that the inorganic polymer SP was introduced into the ion transport layer. FCF functional group (1193, 1143 cm ^-1 ) peak, COC functional group (1057 cm ^-1 ) peak and S=O functional group derived from sulfonic acid group (870, 849 cm ^-1 ) peak and SO functional group (766 cm ^-1 ) As a peak appeared, it was confirmed that the organic polymer PFSA was introduced into the ion transport layer.

Experimental Example 2

To measure the water uptake and dimensional change of the organic/inorganic reinforced composite electrolyte membranes 1 to 4 prepared in Examples 1 to 4, organic/inorganic reinforced composite electrolyte membranes and Nafion212 were targeted. The moisture content and the dimensional change rate were measured as follows, and the results are shown in FIGS. 2 and 3 .

Specifically, the organic/inorganic reinforced composite electrolyte membranes 1 to 4 and the PE separator are dried in an oven at 80° C. under vacuum for at least 24 hours, then the mass is measured, and after soaking in distilled water for 24 hours, moisture on the surface is removed to increase the weight and The dimensional change was measured, and the moisture content and dimensional change rate were measured through the following equation.

In addition, in Examples 1 to 4, the moisture content (Water uptake) and the dimensional change according to the content of the organic polymer and the inorganic polymer included in the organic / inorganic polymer solution were measured, and the results are shown in Tables 1 and 2 shown in

mixing ratio
Example Weapon: Organic
50:50 Weapon: Organic
25:75 Weapon: Organic
20:80 Weapon: Organic
10:90 Example 1 46.2 47.2 47.8 48.7 Example 2 42.0 42.7 43.5 44.2 Example 3 46.0 47.3 47.9 49.0 Example 4 42.1 42.9 43.6 44.0

mixing ratio
Example Weapon: Organic
50:50 Weapon: Organic
25:75 Weapon: Organic
20:80 Weapon: Organic
10:90 Example 1 2.0 2.2 2.3 2.7 Example 2 5.8 7.0 7.3 7.6 Example 3 2.0 2.3 2.5 2.8 Example 4 6.0 6.8 7.3 7.5

As shown in FIGS. 2 and 3, which are the results of measuring the moisture content and dimensional change rate of the organic/inorganic reinforced composite electrolyte membranes 1 to 4 and the PE separator, in the case of the PE separator, the moisture content is 98 to 106%, and the dimensional stability is 1 to 3 %, a very high moisture content was confirmed due to the pores of the PE separator, and the dimensional stability was very good. The organic/inorganic reinforced composite electrolyte membranes 1 to 4 have a moisture content of 42 to 50.2% and a dimensional stability of 2 to 8%. The organic/inorganic polymer impregnated layer and the upper and lower oil/inorganic polymer impregnated layers as an ion transport layer on the pores and surface of the porous polymer support. By forming the inorganic polymer layer, it was confirmed that the moisture content decreased and the dimensional stability increased. In general, the dimensional stability of Nafion, a commercial membrane, is known to be 15 to 20%, and it can be seen that the organic/inorganic reinforced composite electrolyte membranes 1 to 4 of the present invention exhibit superior dimensional stability.

Experimental Example 3

The organic/inorganic reinforced composite electrolyte membranes 1 and 2 prepared in Examples 1 and 2 were immersed in distilled water at room temperature for 24 hours, and then the membrane was placed between the electrodes of the ion conductivity cell, and then AC impedance measurement was performed in distilled water. Thus, the ionic conductivity of the membrane was measured, and the results are shown in FIG. 4 .

From Figure 4, which is the result of measuring the ionic conductivity of organic/inorganic reinforced composite electrolyte membranes 1 and 2 and the PE separator, the organic/inorganic reinforced composite electrolyte membrane of the present invention has higher ionic conductivity than the PE separator, which is a functional group capable of ion transfer It is predicted that this is because a channel for ion transfer was formed through the impregnation of organic/inorganic polymers with ion-conducting functional groups in PE separators without ions.

Although the present invention has been illustrated and described with reference to preferred embodiments as described above, it is not limited to the above-described embodiments, and those of ordinary skill in the art to which the present invention pertains within the scope not departing from the spirit of the present invention Various changes and modifications will be possible.

Claims (10)

porous polymer support;
a hydrophilic polymer impregnated layer formed on all surfaces of the polymer support exposed to the outside, including pores of the polymer support;
an organic/inorganic polymer impregnated layer formed on the hydrophilic polymer impregnated layer; and
Upper and lower organic / inorganic polymer layers respectively formed on the lower surface and the organic / inorganic polymer impregnated layer formed on the upper surface of the porous polymer support;
The organic/inorganic polymer impregnated layer and the upper and lower organic/inorganic polymer layers have a cross-linking structure formed by thermal cross-linking reaction between the silane-based inorganic polymer material and the organic polymer material included in each layer, and the inorganic polymer during the thermal cross-linking reaction. An organic/inorganic reinforced composite electrolyte membrane comprising nano-silica particles formed from a material and uniformly dispersed in the cross-linked structure.
delete The method of claim 1,
The organic/inorganic polymer impregnated layer and the upper and lower organic/inorganic polymer layers contain an inorganic polymer material and an organic polymer material in a weight ratio of 0.01:19.99 to 19.99:0.01.
4. The method of claim 3,
The inorganic polymer material is any one selected from the group consisting of DM-SP, D-SP (Diol Silica Precursor), BD-SP (Bisphenol Dimethylbenzanthracene SP), BDP-SP (Bisphenol Dimethylbenzanthracene Polydimethylsiloxane SP), and combinations thereof. Characterized by organic/inorganic reinforced composite electrolyte membrane.
4. The method of claim 3,
The organic polymer material is Nafion (DuPont), 3M Ionomer (3M), Fumion (Fumatech), Aciplex (Asahi Chemical), Aquivion (Solvay), sulfonated perfluorinated sulfonic acid (PFSA, perfluorinated sulfonic acid), polytetra An organic/inorganic reinforced composite electrolyte membrane, characterized in that it is any one selected from the group consisting of fluoroethylene, polyvinylidene fluoride, polyvinyl fluoride, polyvinylidene fluorocoperfluorinated alkylvinyl ether, and combinations thereof .
The method of claim 1,
The porous polymer support is an organic/inorganic reinforced composite electrolyte membrane, characterized in that it is made of polyethylene or polyethylene containing hydrophilic silica.
7. The method of claim 6,
The porous support is an organic/inorganic reinforced composite electrolyte membrane comprising pores having a diameter in the range of 5 nm to 100 nm.
The method of claim 1,
The hydrophilic polymer is an organic/inorganic reinforced composite electrolyte membrane, characterized in that at least one selected from the group consisting of polydopamine, polyethylene glycol and polyvinyl alcohol.
A redox flow battery comprising the organic/inorganic reinforced composite electrolyte membrane of any one of claims 1, 3 to 8.
A water treatment device comprising the organic/inorganic reinforced composite electrolyte membrane of any one of claims 1, 3 to 8.

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