KR102054204B1 - Defect-free membrane formed on mesh support layer, method for manufacturing the same and subtle energy harvesting device using the same - Google Patents

Abstract

The present invention relates to a defect-free separator formed on a porous support, a method of manufacturing the same, and a microenergy extraction device using the same. It relates to an element.
According to the present invention, by using an organic solvent containing a chloride group 1 Large area defect-free membranes can be formed on a porous support having a pore size of at least micrometers. In addition, it is possible to improve the binding strength of the nano thin film to the porous support through the organic acid treatment. In addition, the selectivity may be increased by introducing an excess of cations and anions to the separator surface.

Description

DEFECT-FREE MEMBRANE FORMED ON MESH SUPPORT LAYER, METHOD FOR MANUFACTURING THE SAME AND SUBTLE ENERGY HARVESTING DEVICE USING THE SAME}

The present invention relates to a defect-free separator formed on a porous support, a method for manufacturing the same, and a micro energy extraction device using the same.

The interfacial polymerization technology is a technique in which different monomers capable of condensation reaction at two unmixed interfaces grow into polymers and are applied to various applications. Due to the expansion of new industries of environment and energy, there is a continuous demand for the development of high performance separators. Reverse osmosis membranes and nano separation membranes based on interfacial polymerization technology have been applied to actual mass production, and are applied to various separation applications such as gas separation membranes and organic solution separation membranes.

Interfacial polymerization is very weak in mechanical strength because it forms a nano-thick film. Therefore, in order to maintain the performance of the nano-thickness membrane as a separator, it is necessary to use a support layer. At this time, it is divided into a flat membrane and a hollow fiber membrane according to the structure of the support layer, regardless of the shape of the support layer, the surface pore size of the support layer on which the nano thin film is coated should have very small pores (generally several nanometers in size) as shown in FIG. For this reason, as shown in FIG. 2, the structure of the nano separator formed through general interfacial polymerization has ridge-and-valley formations, and these structures basically indicate the presence of defects. In order to minimize the defects of the nano-membrane membrane, the pore size of the support layer is smaller than the size of the molten bone, and the portion of the defect may reduce the performance degradation due to the defect when combined with a portion other than the pore portion of the support layer. Related phenomena are also reported in recent papers (Macromol. Res., Vol. 24, No. 4, 2016). In order to overcome this phenomenon, a free-standing method using interfacial polymerization in the absence of a supporting layer has recently been proposed (Journal of Membrane Science, Volume 526, 15 March 2017, Pages 52-59). However, this method also cannot be said to be a real large area defect-free membrane manufacturing method because the membrane produced by the interfacial polymerization method is minimized by the support layer by the back layer on the support layer having a pore size of several nanometers or less.

Based on the concept of material permeation, the support layer serves to reduce the amount of material permeated through the nano-membrane produced through interfacial polymerization. In particular, when a solution having a different concentration exists between the supporting layers, such as pressure delay osmosis and forward osmosis, the effective concentration polarization decreases due to internal concentration polarization in water permeation due to osmotic pressure. The reduction of effective concentration polarization leads to a decrease in the performance of the entire system, leading to an increase in energy consumption and production cost. Therefore, structural factors (structure parameter, S = τ · t / ε, thickness (t), porosity (ε), and tortuosity ( τ)) must be used with a small support layer. Typical support layers are fabricated through non-solvent induced phase separation, where the pores have tens of micrometers or less, and the tortuosity may have a value of 1 due to the formation of irregular pores. There is no structure. In addition, this structure, if the presence of fouling materials (fouling materials) that degrade the membrane performance, it is easy to block the pores of the support layer, the performance degradation over the process time will appear suddenly.

The ideal support layer should have a pore size of more than a few tens of micrometers, as well as a twist of 1 to minimize internal concentration polarization. Such a support layer is typically a mesh, but as mentioned above, since the existing interfacial polymerization method cannot form a defect-free film, it has not been used as a support layer to date. If these flawless nano thin films can be coated on the mesh, not only can maximize performance due to minimizing internal concentration polarization, but also find new applications.

If the defect-free nano thin film has a function of passing only water or controlling the selective permeability of cations and anions, it is possible to form a membrane potential difference. Depending on the performance of the separation membrane ion and water permeability rate will vary, basically, the size of the water molecules 1 ion (Na ^+, Cl ^-) is smaller than will have the fast transmission rate at least four fold (J. Phys Chem.. B 2004, 108, 16064-16070). Since the permeation rate is directly related to the size of ions or molecules, the permeation rate of water molecules becomes faster when comparing the permeation rates of divalent ions with water. Particularly, in the support layer having a torsion index of 1, such as a mesh, the diffusion rate of water becomes faster due to the increase in the mixing rate due to convection, which makes the separator potential difference even larger.

Membrane potential difference is a phenomenon existing in all cells of nature, and is used for various biological reactions. If the potential difference is formed using water molecules having a high permeation rate, the potential difference can be easily formed by an external magnetic pole (for example, vibration, pressure, and bending). In a previous study, a new study reported that a pressure delay osmosis membrane can simultaneously form a potential difference and generate electricity based on this potential difference (Phys. Chem. Chem. Phys., 2016, 18, 23469-23473). ). The pressure delay osmosis membrane is a membrane that allows only water to pass through, which shows that the potential difference can be formed and thus electricity can be directly generated. In particular, the potential difference formation based on the separator is based on a free energy equation. In other words, since free energy represents a change in equilibrium, any external change is perceived. That is, by using a membrane that only permeates water or a membrane having ion selectivity, a membrane potential difference can be formed for all external energy sources. Therefore, when the composite nano membrane combined with the ideal membrane manufacturing technology and the support layer forms a cell in which ions capable of electrochemical reaction are dissolved, Gibbs-free energy changes spontaneously due to pressure, temperature, and vibration. This makes it possible to directly generate electricity. In particular, since the nano-separation membrane coated on the mesh is very flexible, if the device has flexibility, it is also possible to form a film potential difference by changing due to vibration, bending, bending, pressure, temperature, and the like. By using this, a new concept of a new concept that can be applied to a wide variety of applications such as waste heat recovery, wind power generation, piezoelectric elements, etc. can be made.

Republic of Korea Patent Publication No. 10-2016-0128771

The present invention provides a defect-free separator formed on a porous support, a method for manufacturing the same, and a micro energy extraction device using the same.

In the method for preparing a separator according to an embodiment of the present invention, (a) impregnating a porous support in a polyfunctional amine solution, (b) removing the polyfunctional amine solution from the porous support impregnated in step (a), Reacting the porous support with a polyfunctional organic solvent, and (c) immersing the porous support, in which the reaction is completed in step (b), in a solution containing an organic acid and post-treatment, and in step (b), Functional organic solvents include organic solvents having polyfunctional acyl halides and chloride groups.

The pore size of the porous support may be 1 ~ 150μm, preferably 10 ~ 90μm, more preferably 35μm. The performance of the support layer is determined by the structure parameter (S = t x t / ε, t = separator thickness, t = bitrim index, ε = porosity). In other words, the smaller the structure parameter, the greater the membrane performance in terms of material permeation. In general, an increase in pore size is associated with an increase in porosity, but may also lower the mechanical strength of the separator. Porosity can be used in a variety of 10 to 50%, it is appropriate to use a thickness of the porous support 10 ~ 500μm to minimize the internal concentration polarization. The porous support may minimize the internal concentration polarization of the separator bar having a tortuosity of 1. A torsional index of 1 refers to the case where the pores are straight, like highways.

The porous support may be composed of at least one material selected from the group consisting of polyester, polyamide, and mixtures thereof.

The polyfunctional amine is piperazine, m-phenylenediamine, p-phenylenediamine, 1,3,5-benzenetriamine, 4-chloro-1,3-phenylenediamine, 5-chloro-1,3- At least one selected from the group consisting of phenylenediamine, 3-chloro-1,4-phenylenediamine and mixtures thereof.

The amine solution may be an aqueous amine solution, wherein the aqueous amine solution may be prepared by dissolving 1 to 20 wt% of amine in water, preferably 5 wt%.

The time for impregnating the porous support into the amine solution may be 2 to 10 seconds.

The polyfunctional acyl halide may be trimezoyl chloride, isophthaloyl chloride, benzene-1,3-disulfonyl chloride, cyanuric chloride, alkyl chloride (ClCO-R ₁ -COCl, R ₁ is CH ₂ or CH = CH Compound) and mixtures thereof, and may be at least one selected from the group consisting of acyl chloride.

The organic solvent having a chloride group may be at least one selected from the group consisting of chloride benzene, 1,2-dichloro benzene and mixtures thereof.

In general, the organic solvent used in interfacial polymerization uses hexane (n-hexane), which has a disadvantage in that its performance changes drastically by reducing solubility by increasing chemical instability of acyl chloride. In general, the nano-membrane formed by interfacial polymerization has a ridge bone structure, so there are many defects. However, the use of a solvent in which the chloride is bonded to the organic solvent can overcome the chemical instability of the acyl chloride. In addition, the polyfunctional amine material reacting when having a benzene structure is capable of directional control when forming a separator at an interface by molecules of acyl chloride and benzene-benzene (pi-pi interaction), thereby forming a defect-free film.

The organic solvent in which the acyl halide is mixed may contain 0.1 to 5 wt%, preferably 1 wt% of acyl chloride.

The contact (reaction) of the acyl chloride solution may be performed at room temperature (15-40 ° C.) for 30 seconds to 30 minutes, preferably 10 minutes.

The solution containing the organic acid in step (c) may be at least one selected from the group consisting of divalent metal ions, amines, polyfunctional organic materials including hydroxy groups and mixtures thereof.

The organic acid is formic acid (acetic acid), acetic acid (acetic acid), propionic acid (propinic aicd), butyric acid (butyric acid), valeric acid (valeric acid), caproic acid (caproic acid), oxalic acid, lactic acid (lactic) acid, malic acid, citric acid, benzoic acid, carbonic acid, carbonic acid, uric acid, taurine, toluenesulfonic acid, trifluoromethanesulfonic acid (trifluoromethanesulfonic acid), aminomethylphosphonic acid (aminomethylphosphonic acid), and at least one selected from the group consisting of a mixture thereof.

The divalent metal ion may be Mg ²⁺ , Ca ²⁺ , Cu ²⁺ , Zr ²⁺ or Zn ²⁺ , preferably Zr ²⁺ .

The organic acid-containing solution may be water or an organic solvent as a solvent.

The organic solvent may include one or more selected from the group consisting of dimethylformamide, N-methyl-2-pyrrolidone, and tetrahydrofuran.

The solution containing the organic acid may include 10 to 50% by weight of the organic acid.

The solution containing the organic acid may contain 5 to 30% by weight of divalent metal ions and the like.

The post-treatment may be performed by immersing the separator formed on the porous support in a solution containing an organic acid for 1 minute to 1 hour, preferably 10 minutes).

After the step (c) (d) may further comprise the step of heat-treating the porous support for 30 seconds to 10 minutes, preferably 5 minutes at a temperature of 80 ~ 130 ℃, preferably 90 ℃.

A separator according to another embodiment of the present invention is prepared by impregnating a porous support in a polyfunctional amine solution, reacting with a polyfunctional acyl halide mixed in an organic solvent having a chloride group, and then working up with a solution containing an organic acid. .

According to another embodiment of the present invention, a method of preparing a nanomembrane (a-1) impregnates a porous support with a solution containing a polyfunctional amine solution, a cation and anion monomer having a double bond, a crosslinking agent, and an initiator. Step, (b-1) after removing the solution from the porous support impregnated in the step (a-1), the step of interfacial polymerization by pouring a polyfunctional organic solvent on the porous support and (c-1) the (b-1) In step), the polymerization is completed by pouring a solution containing a catalyst onto the porous support.

In the step (a-1), the polyfunctional amine is piperazine, m-phenylenediamine, p-phenylenediamine, 1,3,5-benzenetriamine, 4-chloro-1,3-phenylenediamine, 5 At least one member selected from the group consisting of -chloro-1,3-phenylenediamine, 3-chloro-1,4-phenylenediamine, and mixtures thereof.

In the step (a-1), the crosslinking agent may be an organic compound including at least two or more double bonds.

In the step (a-1), the initiator may be at least one selected from the group consisting of azo, peroxide, and mixtures thereof.

In the step (b-1), the multifunctional organic solvent may include an organic solvent having a polyfunctional acyl halide and a chloride group.

In the step (b-1), the polyfunctional acyl halide is trimesoyl chloride, isophthaloyl chloride, benzene-1,3-disulfonyl chloride ), Cyanuric chloride (cyanuric chloride), alkyl chloride (alkyl chloride, ClCO-R1-COCl, R1 may be at least one selected from the group consisting of CH2 or CH = CH) and mixtures thereof.

In the step (c-1), the catalyst is an organic material including an amine, and the solution may be an organic solvent.

According to another embodiment of the present invention, the nano-membrane is impregnated with a porous support in a solution containing a polyfunctional amine solution, a cation and anion monomer having a double bond, a crosslinking agent, and an initiator, followed by interfacial polymerization with the polyfunctional acyl halide. Positive and negative charges are present on the surface prepared by inducing polymerization with a solution containing a catalyst.

In the case of a separator capable of forming a potential difference by excluding a divalent ion and selectively permeating only water, an excess of positive or negative charge must be induced on the surface of the separator. To this end, a monomer and an initiator having one or more double bonds are mixed with a polyfunctional amine solution, and then, through interfacial polymerization, a polyfunctional amine and a polyfunctional acyl chloride are first reacted to form a separator. Thereafter, the catalyst for polymerizing the mixed monomer is dissolved in an organic solvent not mixed with water, and then coated on the membrane on which the separator is formed. This causes the catalyst to diffuse from the organic phase to the water phase, at which time a highly reactive substance such as radicals is formed from the membrane surface to the initiator, and the monomers polymerize, which makes it very easy to induce excess negative or positive charge separators on the membrane surface. Can be. Positive charge or negative charge is determined by the characteristics of the monomer selected. For example, when a monomer having a double bond with a functional group of a tetravalent ammonium group is used, the positive charge separation membrane is a monomer having a double bond with a functional group such as a carboxyl group. In case of use, an excess negative charge separator is produced. Since the present technology is capable of continuous processes, in particular, since the interface formed in the existing interfacial polymerization is continuously maintained, there is a strong distinction that positive and negative charges are formed only on the surface and inside of the separator.

 According to another embodiment of the present invention, an energy extraction device includes a first electrode, a first gasket filled with an electrolyte solution, a separator stacked on the first gasket, and an electrolyte stacked on the separator. An energy extraction device comprising a second gasket filled with an aqueous solution and a second electrode stacked on the second gasket, wherein the separator selectively penetrates an external energy source to provide the electrolyte.

The membrane is impregnated with a porous support in a polyfunctional amine solution, the polyfunctional acyl halide mixed in an organic solvent having a chloride group is contacted, and then the energy extraction device using the separator produced by enhancing the characteristics of the separator through a post-process To provide. The separator may permeate water and exclude divalent ions.

The electrolyte may include one or more selected from the group consisting of salts containing divalent metal ions, salts including monovalent salts and ferricyanates, but are not limited thereto and may be subjected to an electrochemical reaction. Any substance can be used without limitation. In the case of an electrolyte containing monovalent ions, it is suitable to use a separator in which metals are treated by post-treatment, and in the case of an electrolyte containing divalent ions, a separator in which excess positive / negative charges are introduced.

The electrolyte solution may be maintained at a concentration of 1 to 50wt% and more preferably at a concentration of 10wt%.

The energy extraction device may be a flexible device.

The energy extraction device may be modified into various structures, and the electrolyte solution may include a flowing nanoparticle electrode.

According to the present invention, a large area defect-free membrane can be formed by interfacial polymerization on a porous support having a pore size of 1 micrometer or more by using an organic solvent containing a chloride group. In addition, the post-treatment technology may not only improve the bonding strength between the porous support and the nano thin film, but also improve the mechanical strength of the separator. In addition, positive and negative charges may be introduced to the separator surface.

In addition, the present invention can minimize the internal concentration polarization phenomenon by applying a porous support having a value of torsion index 1.

In addition, it is possible to easily manufacture a multi-energy extracting device at a low price by using the separator prepared according to the present invention, since the energy extracting device is not broken as a flexible device is applied to various applications due to the diversity of the device structure Will be easy.

In addition, energy was generated when pressure, vibration, bending, warping, and temperature change were applied to the energy extracting device according to the present invention, and it was confirmed that energy storage is particularly long-lasting.

1A and 1B are images of a support layer (generally used support layer) fabricated through solvent induced phase separation. FIG. 1B is an enlarged view of the square of FIG. 1A.
Figure 2a shows an image of the ridge bone structure of the nano-film formed through the general interfacial polymerization method.
2B is an image of a defect-free nanoseparation membrane structure.
Figure 3 is an image of a defect-free nano separator prepared in accordance with Example 1.
Figure 4 is an image showing a phenomenon that the nanofilm is torn when not subjected to the post-treatment in Example 1.
5A is a conceptual diagram of a multiple microenergy extraction device according to a third embodiment.
FIG. 5B illustrates when bending or vibration is applied to the multiple microenergy extraction elements of FIG. 5A.
FIG. 5C illustrates a case in which compression energy is applied to the multiple microenergy extraction elements of FIG. 5A.
FIG. 5D illustrates when thermal energy is applied to the multiple microenergy extraction device of FIG. 5A.
Figure 5e shows the microenergy extraction device is inserted into the separator actually manufactured.
6 is a graph showing that the potential difference increases when bending energy is continuously applied to a device manufactured according to Example 3. FIG.
FIG. 7 is a graph showing an increase in current when pressure and bending energy are continuously applied to a device manufactured according to Example 3. FIG.
8 is a graph showing that the device manufactured according to Example 3 retains power for a long time and increases internal energy due to temperature change.
9 is a graph showing a potential difference that varies according to the number of stacked layers when the cationic anion separators are sequentially stacked.
10 is a graph showing the generated current according to the concentration of the electrolyte.

Hereinafter, the present invention will be described in more detail with reference to Examples. The objects, features and advantages of the present invention will be readily understood through the following examples. The present invention is not limited to the embodiments described herein and may be embodied in other forms. The embodiments introduced herein are provided to sufficiently convey the spirit of the present invention to those skilled in the art. Therefore, the present invention should not be limited by the following examples.

According to one embodiment of the present invention, a method of manufacturing a defect-free composite separator by interfacial polymerization is briefly described as follows.

Wet a porous support with a pore size of 35 um in amine aqueous solution (MPD, m-pheneylenediamine) used for general interfacial polymerization, and remove excess MPD solution using a rubber roller. Subsequently, an organic solution obtained by dissolving acyl chloride (TMC, trimesoyl chloride) in 1,2-dichlorobenzene or chlorobenzene is poured to perform interfacial polymerization to prepare a nano separator. In general, the organic solvent used in interfacial polymerization uses hexane (n-hexane), which has a drawback in that its performance changes drastically by increasing chemical instability of acyl chloride and reducing solubility. In addition, the formed nano-separated membrane has a ridge bone structure, so there are many defects. However, the use of a solvent in which the chloride is bonded to the organic solvent can overcome the chemical instability of the acyl chloride. In addition, when the benzene structure has a benzene structure, the reacting material can be directionally controlled when forming a separator at the interface by benzene-benzene (pi-pi interaction) of acyl chloride, thereby forming a defect-free film.

However, the formed nano thin film (composite membrane) does not have sufficient physicochemical bonding strength when coated on the porous support. Therefore, there is a need for a post-process that can improve the bonding force between them. The material of the porous support to be used is preferably at least one selected from the group consisting of polyesters, polyamides, and mixtures thereof, in which case it should be possible to increase the chemical bonding force. The post treatment process presented here is a solvent treatment technique. The post-treatment process suitably uses organic acids which not only lower the glass transition temperature of the surface of these porous supports but also induce charge on the surface. Here, the organic acid is formic acid (acetic acid), acetic acid (acetic acid), propionic acid (propinic aicd), butyric acid (butyric acid), valeric acid (valeric acid), caproic acid (caproic acid), oxalic acid, lactic acid ( lactic acid, malic acid, citric acid, citric acid, benzoic acid, carbonic acid, uric acid, taurine, toluenesulfonic acid, trifluoromethane At least one selected from the group consisting of sulfoic acid (trifluoromethanesulfonic acid), aminomethylphosphonic acid, and mixtures thereof, preferably formic acid (acetic acid), acetic acid (acetic acid) can be used. And some organic solvent such as dimethylformamide (n, n-dimethyformaide) or water may be used. In addition, it is suitable to include various divalent or more metals in the post-treatment solvent in order to eliminate the defects present in the nano separator. Divalent or more metals (Mg, Ca, Cu, Zr, Zn, etc.) may be used. After the heat treatment can finally form a stable separator (Fig. 3). 3 shows that the separator is stably formed on the porous support without defects when the heat treatment is performed. In FIG. 4, the membrane prepared by the interfacial polymerization method is easily torn when not treated through the organic acid solution.

When MPD is used as the polyfunctional amine, the monovalent ion exclusion rate can be increased up to 99% or more. However, since this increases the ion resistance of the separator, it may occur when an electrolyte containing divalent ions must be used. MPD may be used to prepare a separator that selectively excludes divalent ions, but it is suitable to use piperazine or polyethyleneimine in terms of ion permeation resistance and chemical stability. In order to enhance the selective rejection of cations and anions in the electrolyte containing divalent ions, positive and negative charges may be increased through a post-treatment method to the separator surface. In general, the introduction of positive and negative charges can be induced through a chemical method with acyl chloride remaining after interfacial polymerization. However, the reactants are limited to amines or alcohols that can react with acyl chlorides and cannot increase the degree of crosslinking, which leads to a sharp increase in swelling when the membrane enters water after grafting. . This not only reduces the ion exclusion rate, but also causes a decrease in mechanical strength of the separator.

 Therefore, a new surface charge induction method is needed. The newly proposed technology is the post-processing technology. First, a monomer having a radical initiator and a double bond in an amine solution, including a positive or negative charge, and a crosslinking agent are prepared as necessary. Then, after lamination to the porous support, excess solution is removed using a device such as a rubber roller. After the TMC is dissolved in 1wt% in chlorobenzene and applied, the reaction is performed for about 10 minutes at a temperature of 10 ~ 30 ℃, suitably 22 ℃. After washing the unreacted TMC using n-hexane, the radical reaction catalyst is dissolved in n-hexane 0.1 ~ 50%, suitable 2% and reapplied. At this time, there is still water in the support layer to form the same interface as the interfacial polymerization, and radical polymerization occurs at this interface. Polymerization occurs precisely on the surface of the separator, and unlike the conventional method, polymerization does not affect the performance of the membrane because it occurs under conditions where the separator is formed. After the reaction for 10 minutes at 22 ℃ room temperature to remove the residual catalyst through n-hexane can be produced a defect-free membrane. The separator is characterized in that only water can pass through the divalent electrolyte.

The polyfunctional amine is m-phenylenediamine, p-phenylenediamine, 1,3,5-benzenetriamine, 4-chloro-1,3-phenylenediamine, 5-chloro-1,3-phenylenediamine , 3-chloro-1,4-phenylenediamine, piperazine, and mixtures thereof. The amine solution may be an aqueous amine solution, wherein the aqueous amine solution may be prepared by dissolving 1 to 20 wt%, preferably 5 wt% amine in water.

The time for impregnating the porous support into the amine solution may be 2 to 10 seconds.

An energy extraction device capable of extracting multiple micro energy using the separator thus prepared was manufactured (FIG. 5).

The energy extracting device includes a first electrode, a first gasket filled with an electrolyte solution stacked on the first electrode, a separator stacked on the first gasket, a second gasket filled with an electrolyte solution stacked on the separator, and the first gasket. And a second electrode laminated on the two gaskets.

As the first or second electrode, a copper electrode was used, and Cu (NO ₃ ) ₂ was used as a solution capable of electrochemical reaction. 1 to 50wt%, more preferably about 10wt% can be used by dissolving in water. First, attach the solution to the gasket to fill the solution on the flexible substrate, and then fill the copper solution. After that, put the prepared membrane on it and seal it so that the solution does not flow out. After that, the other side is also attached with a gasket and filled with copper solution to finally assemble the cell. At this time, seal should be secured to prevent leakage of solution.

Materials capable of electrochemical reactions can be used both inorganic organic, in this embodiment was used a solution containing copper. Since the prepared membrane can selectively penetrate an external energy source to provide the electrolyte, and in detail, it is a mechanism for selectively forming only the water to form a potential difference. The electrodes and electrochemicals used can be used with any material that can form concentration polarization.

Example 1 Membrane Preparation

A porous support made of polyester was prepared (pore size 50 μm, thickness 250 μm). Multifunctional amine solution (MPD, m-pheneylenediamine) was prepared as an aqueous solution of amine dissolved in 5wt%. The porous support was then placed on a flat glass or film without porosity and then impregnated in the polyfunctional amine solution at 22 ° C. for 5 seconds. Since the porosity is large, impregnation time is sufficient for several seconds. Then, as soon as the excess amine solution was removed through mechanical methods, suitably rubber rollers, a polyfunctional acyl chloride (TMC) trimesoyl chloride (TMC) solution was poured. The polyfunctional acylchloride solution was prepared by dissolving TMC in 1,2-dichloride benzene to 1% by weight of TMC. The reaction time was about 10 minutes and the reaction was performed at room temperature. Thereafter, the polyfunctional organic solvent was removed and then unreacted polyfunctional acyl chloride was removed through hexane. After preparing a 30 wt% formic acid aqueous solution, zirconium ions were added to make it 10 wt% in the solution. The thin film coated on the porous support was immersed in the prepared aqueous formic acid solution at 25 ° C. for 10 minutes. After washing the unreacted material through water, it was heat-treated for 5 minutes in a 90 ℃ oven.

Example 2. Positive / Negative Charge Excess Nanoseparation Membranes

Excessive cations or anions may be formed to form a nano thin film. First, in the case of a membrane containing an anion, a weight ratio of 1 to 90%, preferably, in water of a negatively charged monomer (for example acrylic acid) or a monomer having an acetate (for example vinyl acryl monomer, vinyl acetate monomer) Dissolve at 30%. Thereafter, a crosslinking agent having two or more double bonds (eg, methylenebisacrylamide, N, N-methylenebisacrylamide) is dissolved in a weight ratio of 1 to 90%, preferably 10%. And an initiator (for example, ammonium persulfate) is dissolved in 0.1-30% by weight, suitably 5% here. In the solution dissolved therein, piperazine (piperazine) is dissolved in water at a weight ratio of 1 to 20 wt%, suitably 5 wt%.

For membranes containing excess cations, positively charged excess monomers with double bonds (monomers containing tetravalent amines, such as vinyl benzene trimethylammonium, vinylbenzyl trimethylammonium, diallydimethylammonium chloride), monomers with acetate (Eg, vinyl acryl monomer, vinyl acetate monomer) is dissolved in water at a weight ratio of 1 to 90%, suitably 30%. Thereafter, a crosslinking agent having two or more double bonds (eg, methylenebisacrylamide, N, N-methylenebisacrylamide) is dissolved in a weight ratio of 1 to 90%, preferably 10%. And an initiator (for example, ammonium persulfate) is dissolved in 0.1-30% by weight, suitably 5% here. PEI (Mw = 1,000) was dissolved in a solution dissolved in water at a weight ratio of 1 to 20 wt%, suitably 5 wt%.

Thereafter, the reaction proceeds in the same manner. TMC was dissolved in chloroform at a weight ratio of 0.1 to 10%, suitably 2%, and then laminated in a place where excess solution was removed on the surface of the support layer impregnated with monomers and piperazine or PEI and an initiator, followed by interfacial polymerization. Reaction is about 1-40 minutes, suitably about 10 minutes. Then, after removing the unreacted TMC through n-hexane, a catalyst (for example, tetramethylethylenediamine, N, N, N, N-tetramethylethylenediamine) in n-hexane weight ratio of 0.1 to 50%, suitably After dissolving at 2%, the surface is wetted with interfacial polymerization and reacted for 1 to 40 minutes, preferably 10 minutes. After washing through n-hexane to terminate the reaction by reacting about 0.5 ~ 30 minutes, suitably 3 minutes in an environment of 60 ℃ or more. Excess charge is present on the surface of the prepared membrane, thereby improving the surface charge density on the membrane.

The following shows the results of the bivalent selectivity and open circuit voltage of the separator without positive and negative charges and introduced. In the experiment below, Pt wire was used as the electrode, Cu (NO ₃ ) ₂ was used as the electrolyte, and 0.001M was used for the 1M low concentration. The measured open circuit voltage was directly related to the surface charge density of the separator, and the maximum voltage was found to be up to 280mV. When no positive or negative charge was introduced on the surface of the separator, it could be seen that 100mV. In the case of divalent selectivity experiment, MgCl ₂ solution was used at 0.2 wt%, and selectivity was measured by measuring the concentration of divalent ions in water permeated at 5 bar. The introduction of cations or anions showed very high selectivity of more than 99%, whereas for membranes without the introduction of cations or anions, the selectivity was 95%.

Monomer Initiator Crosslinking agent TMC catalyst Divalent ion selectivity OCV (1M: 0.001M) Cu (NO) ₃ ² Piperazine vinylbenzyl trimethylammonium Ammonium peroxide N, N-methylenebisacrylamide TMC N, N, N, N-tetramethylethylenediamine 99% (Mg +, Ca +, Ca + etc) 280 mV Piperazine acrylic acid N, N-methylenebisacrylamide N, N-methylenebisacrylamide TMC N, N, N, N-tetramethylethylenediamine > 99% (SO ₂ ^4- , etc) -270mV Piperazine TMC > 95% 100 mV

Example 3 Fabrication of Multiple Microenergy Extraction Devices

First, a copper electrode was attached on the PET transparent film in the same size as the film. Then, after attaching a square gasket having a side size of 1 cm, the gasket was filled with a 10 wt% Cu (NO ₃ ) ₂ aqueous solution. Then, after raising the separator prepared according to Example 1 was sealed so that the aqueous solution does not flow out. After attaching the gasket on the other side in the same manner, and filled with 10wt% Cu (NO ₃ ) ₂ aqueous solution, and then laminated a copper electrode to complete the cell.

However, the structure shown in Example 3 is only one method and may be changed to any structure.

Experimental Example 1. Multiple Microenergy Extraction

The multi-micro energy extraction device fabricated according to Example 3 is characterized by a free energy induction mechanism based on the selective water permeation ability. The reason for having this characteristic is that since the diffusion rate of water is larger than that of other ions, the response speed due to external stimulation is faster. In addition, when the membrane permeates selective ions, performance degradation may occur due to pH changes and chemical changes between the membrane material and the permeating ions.

 When the device fabricated according to Example 3 receives continuous bending energy, it was confirmed that the potential difference of the device is continuously improved (FIG. 6). In addition, it was confirmed that a current is generated in the device when it is bent when a pressure is applied to the device manufactured according to Example 2 (FIG. 7). In addition, after continuously applying pressure to the device fabricated according to Example 3, the energy tended to decrease gradually for about 5 days, and then the internal energy of the device was changed when the ambient temperature was changed. (FIG. 8).

Experimental Example 2 Extraction Energy Increase

A method for increasing the potential difference of the device fabricated in accordance with Example 3 is that the positive-negative charge separators are connected in series like the structure of an electric eel. It has the same configuration as in Example 3 for this purpose, but when the separator is sequentially stacked, it can be seen that the voltage rises in relation to the number of stacked as shown in FIG. In the absence of a membrane, it did not occur when pressure was applied to the device, about 0.02V when using an excess of one anion separator, about 0.04V when using two anions, and about 0.04V when using one cation. When using two cations, 0.08V was confirmed to come out. When the concentration of the electrolyte is different, it is shown in FIG. 10 that the amount of current generated rather than the change in voltage is changed.

Claims (22)

delete delete delete delete delete delete delete delete delete delete delete delete (a-1) impregnating the porous support with a solution containing a polyfunctional amine solution, a cation and anionic monomer having a double bond, a crosslinking agent, and an initiator;
(b-1) removing the solution from the porous support impregnated in step (a-1), and then performing interfacial polymerization by pouring a multifunctional organic solvent on the porous support; And
(C-1) The method of manufacturing a nano-membrane comprising the step of inducing polymerization by pouring a solution containing a catalyst on the porous support in which the polymerization is completed in the step (b-1).
Claim 14 was abandoned upon payment of a set-up fee. The method of claim 13,
In the step (a-1), the polyfunctional amine is piperazine, m-phenylenediamine, p-phenylenediamine, 1,3,5-benzenetriamine, 4-chloro-1,3-phenylenediamine, 5 -Chloro-1,3-phenylenediamine, 3-chloro-1,4-phenylenediamine, and a mixture thereof.
The method of claim 13,
The cross-linking agent in the step (a-1) is a method for producing a nano separation membrane which is an organic compound containing at least two double bonds.
The method of claim 13,
In the step (a-1), the initiator is at least one selected from the group consisting of azo-based, peroxide-based and mixtures thereof.
The method of claim 13,
The multifunctional organic solvent in the step (b-1) is a method for producing a nano separation membrane comprising an organic solvent having a polyfunctional acyl halide and chloride group.
Claim 18 has been abandoned upon payment of a setup registration fee. The method of claim 17,
In the step (b-1), the multifunctional acyl halide is trimesoyl chloride, isophthaloyl chloride, benzene-1,3-disulfonyl chloride ), Cyanuric chloride (cyanuric chloride), alkyl chloride (alkyl chloride, ClCO-R1-COCl, R1 is a compound consisting of CH2 or CH = CH) and mixtures thereof at least one selected from the group consisting of nano-membranes Way.
The method of claim 13,
In the step (c-1), the catalyst is an organic material containing an amine, and the solution is an organic solvent manufacturing method of the nano separator.
The porous support is impregnated into a solution containing a polyfunctional amine solution, a cation and anionic monomer having a double bond, a crosslinking agent, and an initiator, followed by interfacial polymerization with a polyfunctional acyl halide, and then a polymerization agent to induce polymerization into a solution containing a catalyst. Nano-separation membrane having a positive charge and a negative charge on the surface prepared according to the manufacturing method of claim 13.
A first electrode;
A first gasket filled with an aqueous electrolyte solution stacked on the first electrode;
A nano separator according to claim 20 stacked on the first gasket;
A second gasket filled with the electrolyte solution stacked on the separator; And
An energy extraction device comprising a second electrode stacked on the second gasket,
And the separator selectively penetrates an external energy source to provide the electrolyte into the electrolyte.
The method of claim 21,
The separator permeates water and excludes divalent ions.

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