JP7284001B2 - Diaphragm for alkaline water electrolysis and method for producing the diaphragm - Google Patents

Description

TECHNICAL FIELD The present invention relates to a diaphragm for alkaline water electrolysis and a method for producing the diaphragm.

Electrolysis of water is known as one of the industrial production methods of hydrogen gas, which has been attracting attention as an energy source in recent years. Electrolysis of water is generally performed by applying a direct current to water to which sodium hydroxide, potassium hydroxide, or the like has been added as an electrolyte in order to increase conductivity. For such electrolysis of water, an electrolytic cell having an anode compartment and a cathode compartment separated by a diaphragm is used.

Electrolysis of water is performed by the transfer of electrons (or ions). Therefore, in order to perform electrolysis efficiently, the diaphragm is required to have high ion permeability. In addition, it is required to have gas barrier properties capable of blocking oxygen generated in the anode chamber and hydrogen generated in the cathode chamber. The electrolysis of water uses a highly concentrated alkaline aqueous solution of about 30% and is carried out at about 80 to 90°C. Therefore, a diaphragm for alkaline water electrolysis used for electrolysis of water is required to have high temperature resistance and alkali resistance. Further, as a diaphragm for alkaline water electrolysis, a diaphragm that achieves both higher ion conductivity and higher gas barrier properties has been demanded.

Various porous membranes produced by non-solvent induced phase separation (NIPS) have been proposed as diaphragms for alkaline water electrolysis.
Regarding film formation by a non-solvent-induced phase separation method, Non-Patent Document 1 describes a porous membrane produced by a non-solvent-induced phase separation method from a resin solution containing polysulfone, zirconia and polyvinylpyrrolidone. However, the molecular weight of the polyvinylpyrrolidone used and the denseness of the surface layer of the porous membrane have not been studied.

Front. Chem. Sci. Eng. 2014, 8(3); 295-305

An object of the present invention is to provide a diaphragm for alkaline water electrolysis that has both high ionic conductivity and high gas barrier properties, and a method for producing the diaphragm.

The present inventors found that the use of polyvinylpyrrolidone with a high molecular weight in forming a membrane for alkaline water electrolysis containing an organic polymer and inorganic particles increases the resin composition ratio on the surface, resulting in a dense surface structure. The inventors have found that it is possible to provide a diaphragm for alkaline water electrolysis that has both high ion conductivity and high gas barrier properties, and have completed the present invention.

That is, the diaphragm for alkaline water electrolysis of the present invention is a diaphragm for alkaline water electrolysis containing an organic polymer and inorganic particles, and in a cross section perpendicular to the surface of the membrane, from both ends in the longitudinal direction to the center, the The sum of the areas of the inorganic particles and the organic polymer ( Inorganic particles in the range between the ratio A (Pa / Sa) of the sum of the areas (Pa) of the organic polymer to Sa) and the position 2 μm away from the surface of the film in the depth direction and the position 15 μm away The ratio B/A of the ratio B (Pb/Sb) of the sum of the areas of the organic polymer (Pb) to the sum of the areas of the organic polymer (Sb) is 1.0 or less.

Further, in the diaphragm for alkaline water electrolysis of the present invention, in a cross section perpendicular to the surface of the membrane, the membrane has a The porosity C in the range between the surface of and a position 1 μm away from the surface of the film in the depth direction, and the range between the position 2 μm away from the surface of the film and the position 15 μm away in the depth direction It is preferable that the ratio D/C to the porosity D in is 1.8 or more.

Furthermore, the method for producing a diaphragm for alkaline water electrolysis of the present invention includes a dispersion preparation step of preparing a dispersion containing inorganic particles, polyvinylpyrrolidone having a weight average molecular weight of 200,000 or more and 1,300,000 or less, and a solvent; A resin mixture preparation step of mixing an organic polymer resin (R) to prepare a resin mixture; and a film forming step of forming a film using the resin mixture.

INDUSTRIAL APPLICABILITY According to the present invention, it is possible to provide a diaphragm for alkaline water electrolysis that has both high ionic conductivity and high gas barrier properties, and a method for producing the diaphragm.

BRIEF DESCRIPTION OF THE DRAWINGS It is sectional drawing which shows typically one form of the cross section of the diaphragm for alkaline water electrolysis of this invention. In the cross section perpendicular to the surface of the diaphragm for alkaline water electrolysis of the present invention, the surface of the membrane and the separation of the membrane are separated from the longitudinal ends toward the center by 0.4 a or more with respect to the width a of the cross section. FIG. 2 schematically represents the range between 1 μm in the depth direction from the surface and the range between 2 μm and 15 μm in the depth direction from the surface of the film.

The present invention will be described in detail below. A combination of two or more of the individual preferred embodiments of the invention described below is also a preferred embodiment of the invention. Further, in this specification, the description of "A to B" means "A or more and B or less".

1. Diaphragm for alkaline water electrolysis The diaphragm for alkaline water electrolysis of the present invention is a diaphragm for alkaline water electrolysis containing an organic polymer and inorganic particles, and in a cross section perpendicular to the surface of the membrane, from both ends in the longitudinal direction to the center. The area of the inorganic particles and the organic polymer in the range between the surface of the film and the position 1 μm away from the surface of the film in the depth direction in the range of 0.4a or more with respect to the width a of the cross section. In the range between the ratio A (Pa / Sa) of the sum (Pa) of the area of the organic polymer to the sum (Sa) of the The ratio B/A of the sum of the areas of the organic polymer (Pb) to the sum of the areas of the inorganic particles and the organic polymer (Sb) (Pb/Sb) is 1.0 or less.

In the diaphragm for alkaline water electrolysis of the present invention, in a cross section perpendicular to the surface of the membrane, the surface of the membrane is separated from both ends in the longitudinal direction toward the center by 0.4 a or more with respect to the width a of the cross section. and the position 1 μm away from the surface of the film in the depth direction C, and the gap in the range between the position 2 μm away from the surface of the film and the position 15 μm away in the depth direction It is preferable that the ratio D/C to the ratio D is 1.8 or more.

Further, in the diaphragm for alkaline water electrolysis of the present invention, the nitrogen/carbon element atm % determined by X-ray photoelectron spectroscopy (ESCA) on the surface of the membrane is preferably 2.0 to 8.0.

1-1 Organic Polymer The diaphragm for alkaline water electrolysis of the present invention contains an organic polymer. The organic polymer holds the inorganic particles. The organic polymer functions as a partition that holds the inorganic particles, and can suppress the inorganic particles from falling off from the partition in an alkaline solution while minimizing the decrease in the hydrophilic surface of the inorganic particles, which will be described later.

As the organic polymer, an organic polymer resin (R) capable of retaining inorganic particles, preferably without swelling in an alkaline solution, and exhibiting the effects of the present invention [hereinafter sometimes simply referred to as resin (R)]. is not particularly limited. Examples of the resin (R) include fluorine-based resins such as polyvinylidene fluoride and polytetrafluoroethylene; olefin-based resins such as polypropylene; and aromatic hydrocarbon-based resins such as polysulfone and polystyrene. These may be used individually by 1 type, and may be used in combination of 2 or more type. Among them, aromatic hydrocarbon-based resins are preferable in that they can be used as a diaphragm for alkaline water electrolysis with further excellent heat resistance and alkali resistance. Further, the organic polymer constituting the membrane may be one in which a hydrophilic additive, which will be described later, remains in the membrane.

More specifically, the aromatic hydrocarbon resins include, for example, polyethylene terephthalate, polybutylene terephthalate, polybutylene naphthalate, polystyrene, polysulfone, polyethersulfone, polyarylene sulfide resins such as polyphenylene sulfide, and polyphenylsulfone. , polyarylate, polyetherimide, polyimide, polyamideimide, and the like. Among them, at least one selected from the group consisting of polysulfone, polyethersulfone, and polyphenylsulfone is preferable in terms of being able to impart even better alkali resistance. Ethersulfone is more preferred.

By using at least one selected from the group consisting of polysulfone, polyethersulfone, and polyphenylsulfone, for example, when producing a diaphragm using a non-solvent-induced phase separation method or a vapor-induced phase separation method, When the sulfonyl group has an appropriate affinity with the inorganic particles described later, it becomes easy to adjust the phase separation conditions. In addition, since the alkali resistance is further increased, the stability of dimensions, mass and resistance value when used in an alkaline solution for a long time and the effect of suppressing the generation of new voids are excellent.

The content of the resin (R) is preferably 3 to 50% by mass in 100% by mass of the diaphragm for alkaline water electrolysis. When the content of the resin (R) is within the above range, the ion permeability and toughness of the diaphragm for alkaline water electrolysis are good, but inorganic components are not eluted from the diaphragm for alkaline water electrolysis in an alkaline solution. It is even more suppressed. In addition, the diaphragm for alkaline water electrolysis exhibits high ion conductivity and is also excellent in ion permeability, gas barrier properties, heat resistance, and alkali resistance. The content of the resin (R) is more preferably 5 to 47% by mass, still more preferably 7 to 45% by mass, based on 100% by mass of the diaphragm for alkaline water electrolysis.

The content of the resin (R) is preferably 5 to 50% by mass based on 100% by mass of the diaphragm for alkaline water electrolysis when the diaphragm for alkaline water electrolysis of the present invention does not contain a porous support, which will be described later. , more preferably 10 to 47% by mass, more preferably 10 to 45% by mass. When the diaphragm for alkaline water electrolysis of the present invention contains a porous support described later as an organic polymer, the content of the resin (R) is preferably 3 to 25% by mass based on 100% by mass of the diaphragm for alkaline water electrolysis, More preferably 5 to 20% by mass, still more preferably 7 to 18% by mass.

The diaphragm for alkaline water electrolysis of the present invention preferably contains 10 to 50 parts by mass, more preferably 12 to 45 parts by mass, and more preferably 15 to 40 parts by mass of the resin (R) with respect to 100 parts by mass of the inorganic particles described later. It is more preferable to include parts by mass. When the content ratio of the inorganic particles and the resin (R) is within the range described above, the elution of inorganic components from the diaphragm for alkaline water electrolysis in an alkaline solution is further suppressed. In addition, the diaphragm for alkaline water electrolysis exhibits high ion conductivity and is also excellent in ion permeability, gas barrier properties, flexibility, heat resistance, and alkali resistance.

1-1-1 Porous Support The diaphragm for alkaline water electrolysis of the present invention comprises a membrane containing the above-described organic polymer and inorganic particles described below, and contains a porous support as the organic polymer. good too. The porous support is a porous organic polymer, and is a member that does not inhibit ion permeability and can serve as a support for a diaphragm for alkaline water electrolysis. The porous support is preferably a sheet-like member.

Examples of materials for the porous support include polyarylene sulfide resins such as polyethylene, polypropylene, polysulfone, polyethersulfone, polyphenylsulfone, and polyphenylene sulfide; resin materials such as polyketones, polyimides, polyetherimides, and fluorine-based resins. is mentioned. These may be used individually by 1 type, and may be used in combination of 2 or more type. Among them, it preferably contains at least one resin material selected from the group consisting of polypropylene, polyethylene, and polyphenylene sulfide in that it can exhibit excellent heat resistance and alkali resistance, and the group consisting of polypropylene and polyphenylene sulfide. More preferably, it contains at least one more selected resin material.

Examples of the form of the porous support include nonwoven fabric, woven fabric (fabric), knitted fabric, mesh, porous membrane, felt, and mixed fabric of nonwoven fabric and woven fabric. Nonwoven fabric and woven fabric are preferred. Examples include cloth, mesh, or felt, and more preferably non-woven fabric, woven fabric, and mesh.

As the porous support, nonwoven fabric, woven fabric, mesh, or felt containing at least one resin selected from the group consisting of polypropylene, polyethylene, and polyphenylene sulfide is preferred. Furthermore, non-woven fabrics, meshes, or felts containing polyphenylene sulfide are preferred as porous supports. The total content of polypropylene, polyethylene, and polyphenylene sulfide in the porous support is preferably 50% by mass or more, more preferably 70% by mass or more, and even more preferably 90% by mass or more.

When the porous support is in the form of a sheet, the thickness of the porous support is not particularly limited as long as the diaphragm for alkaline water electrolysis of the present invention can exhibit the effects of the present invention. , more preferably 50 to 1000 μm, still more preferably 80 to 500 μm, and most preferably 80 to 250 μm.

1-2 Inorganic Particles The diaphragm for alkaline water electrolysis of the present invention contains inorganic particles. The diaphragm for alkaline water electrolysis of the present invention can exhibit ion permeability by filling the gaps between the inorganic particles or between the particles and the organic polymer with the electrolytic solution. In addition, by including inorganic particles, the diaphragm for alkaline water electrolysis becomes hydrophilic, and oxygen gas and hydrogen gas generated in the electrolysis of water can be prevented from adhering to the diaphragm and interfering with the electrolysis.

Examples of inorganic particles used in the present invention include hydroxides or oxides of magnesium, zirconium, titanium, zinc, aluminum and tantalum, sulfates of calcium, barium, lead, strontium and the like. Among them, magnesium hydroxide, zirconium hydroxide, titanium hydroxide, zirconium oxide, titanium oxide, calcium sulfate, and barium sulfate are preferable in terms of dispersibility of inorganic particles and stability in an alkaline solution. Magnesium oxide, zirconium oxide, titanium oxide and barium sulfate are more preferred. The inorganic particles may be used singly or in combination of two or more.

The inorganic particles may be natural or synthetic. In addition, the surface may be untreated, and in order to improve dispersion in the solvent, the surface is treated with a silane coupling agent, stearic acid, oleic acid, fatty acid, higher fatty acid, carboxylic acid ester, phosphate ester, etc. It may be processed. The shape of the inorganic particles is not particularly limited as long as it is particulate, and may be amorphous; spherical such as a perfect sphere or oblong sphere; plate-like such as flaky or hexagonal plate-like; or fibrous. However, it is preferably spherical, plate-shaped, or fibrous in terms of being easy to disperse in a solvent and easy to prepare a resin composition. A plate-like shape is more preferable.

The inorganic particles preferably have an aspect ratio of 1.0 to 8.0. When the aspect ratio is within the above range, the membrane can have even better ion permeability and excellent uniformity. The aspect ratio is more preferably 1.5 to 7.0, even more preferably 2.0 to 6.0.
In the present specification, the aspect ratio means the ratio (a/b) between the longest diameter a and the shortest diameter b, and powdery inorganic particles are observed with SEM, and any 10 particles of the obtained image are In the above, using analysis software or the like, the ratio (a/b) between the longest diameter a and the shortest diameter b of each particle is measured, and the simple average value of these ratios can be obtained as the aspect ratio of the particle. .

As the longest diameter a, for example, when the shape of the particle is plate-like, the length of the plate surface of the particle is used, and when the particle is fibrous, the length of the fiber is used. The shortest diameter among the diameters passing through the midpoint of the longest diameter a and perpendicular to the longest diameter is defined as the shortest diameter b. As the shortest diameter b, for example, when the shape of the particles is plate-like, the thickness of the particles is used, and when the shape is fibrous, the thickness of the fibers is used. As the thickness of the particles and the thickness of the fibers, the thickness and thickness at the midpoint of the longest diameter a are employed, respectively.

The average particle diameter of the inorganic particles is preferably 0.01 to 2.0 μm, more preferably 0.05 to 1.0 μm, from the viewpoint of further improving the dispersibility of the inorganic particles. It is more preferably 0.08 to 0.7 μm. The average particle size is obtained from particle size distribution measurement by a laser diffraction/scattering method using an inorganic particle dispersion liquid that has been subjected to dispersion treatment using inorganic particles and a 0.2% by mass sodium hexametaphosphate aqueous solution. Average particle size (d50). When the average particle size of the inorganic particles is within the above range, the membrane can exhibit high ion conductivity, ion permeability, and gas barrier properties.

The specific surface area of the inorganic particles is preferably 5 to 35 m ² /g, more preferably 5.5 to 25 m ² /g, more preferably 6 to 20 m ² /g, in that the ion permeability of the diaphragm is further improved. is more preferable. The above specific surface area is a specific surface area measured by the BET method using liquid nitrogen for powdery inorganic particles. Since the ion path in the diaphragm for alkaline water electrolysis is formed by the highly hydrophilic surface of the inorganic particles, the specific surface area of the inorganic particles within the above range can provide a diaphragm with even better ion permeability.

The content of the inorganic particles is preferably 30 to 95% by mass based on 100% by mass of the diaphragm for alkaline water electrolysis. When the content of the inorganic particles is within the above range, the elution of the inorganic component in the alkaline solution is further suppressed, exhibiting high ionic conductivity, ion permeability, gas barrier properties, heat resistance and alkali resistance. An excellent diaphragm can be obtained. The content of the inorganic particles is more preferably 32 to 92% by mass, still more preferably 35 to 90% by mass, based on 100% by mass of the diaphragm for alkaline water electrolysis.

When the diaphragm for alkaline water electrolysis of the present invention does not contain the porous support, the content of the inorganic particles is preferably 50 to 95% by mass in 100% by mass of the diaphragm for alkaline water electrolysis, more preferably. is 53 to 92% by mass, more preferably 55 to 90% by mass.
When the diaphragm for alkaline water electrolysis of the present invention contains the porous support, the content of the inorganic particles is preferably 30 to 48% by mass, more preferably 32 to 45%, based on 100% by mass of the diaphragm for alkaline water electrolysis. % by mass, more preferably 35 to 43% by mass.

FIG. 1 schematically shows one embodiment of the diaphragm for alkaline water electrolysis of the present invention. A diaphragm 1 for alkaline water electrolysis includes a single membrane layer 2 and a support layer 3 . The single layer 2 is a layer containing the resin (R) and inorganic particles, and the support layer 3 is a layer containing the resin (R), inorganic particles and a porous support.

In the diaphragm for alkaline water electrolysis of the present invention, the single membrane layer 2 may be formed on one surface of the support layer 3 or may be formed on both surfaces.
In addition, the diaphragm for alkaline water electrolysis of the present invention may not have the above-described single layer 2, and a composite as a support layer 3 in which the inorganic particles, the resin (R), and the porous support are integrated. It can be a body. By forming the above composite, the strength and toughness of the diaphragm for alkaline water electrolysis can be improved.

1-3 Composition Ratio of Organic Polymer in Membrane Surface Layer The diaphragm for alkaline water electrolysis of the present invention has a cross-section perpendicular to the surface of the membrane, from both ends in the longitudinal direction toward the center, with respect to the width a of the cross-section of 0.00. In the range of 4a or more, the area of the organic polymer with respect to the sum of the areas of the inorganic particles and the organic polymer (Sa) in the range between the surface of the film and the position 1 μm away from the surface of the film in the depth direction. The ratio A (Pa/Sa) of the sum (Pa) and the sum of the areas of the inorganic particles and the organic polymer (Sb ) to the ratio B (Pb/Sb) of the sum of the areas of the organic polymer (Pb) is 1.0 or less . A lower limit of the ratio B/A is 0.6. When the ratio B/A is within the range described above, the composition ratio of the organic polymer in the surface layer of the film increases in the vicinity of the surface of the film, and the surface layer of the film has a dense structure, resulting in high ionic conductivity and high gas barrier properties. A compatible diaphragm for alkaline water electrolysis is obtained. In the present specification, the term "film surface layer" refers to the range between the film surface and a position 1 μm away from the film surface in the depth direction, and the term "near the film surface" refers to the film surface and the depth from the film surface. It refers to the range between a position 15 μm away in the vertical direction.

FIG. 2 schematically shows a cross section 10 of the diaphragm 1 for alkaline water electrolysis. The method for calculating the ratio B/A will be specifically described with reference to FIG. In a range Ta between the surface 11 of the film and a position 1 μm away from the surface 11 in the depth direction S in a range 0.4a or more away from the width a, a cross-sectional observation image by FE-SEM measurement is obtained. obtain. Analysis software is used to divide the obtained cross-sectional observation image into a bright portion and a semi-bright portion. Here, the bright portion is the inorganic particles, and the semi-bright portion is the organic polymer. Then, the sum of the areas of the inorganic particles and the organic polymer (Sa) is obtained from the sum of the areas of the light portion and the semi-light portion, and the sum of the areas of the organic polymer (Pa) is obtained from the sum of the areas of the semi-light portion. (Pa/Sa) is obtained.
In addition, in a cross section 10 perpendicular to the surface 11 of the diaphragm for alkaline water electrolysis, from both ends in the longitudinal direction toward the center, in a range separated by 0.4 a or more with respect to the width a of the cross section 10, from the surface 11 of the membrane A cross-sectional observation image is obtained by FE-SEM measurement in a range Tb between a position separated by 2 μm and a position separated by 15 μm. In the same manner as described above, the sum of the areas of the inorganic particles and the organic polymer (Sb) and the sum of the areas of the organic polymer (Pb) are obtained from the obtained cross-sectional observation image, and the ratio B (Pb/Sb) is obtained. .
From the obtained ratios A and B, the ratio B/A is determined.

The surface of the diaphragm for alkaline water electrolysis is not particularly limited, and may be, for example, the surface on the single membrane layer 2 side of the diaphragm 1 for alkaline water electrolysis in FIG. 1 or the surface on the support layer 3 side. In the case of the surface on the side of the support layer 3, the calculation excluding the support component is required. In addition, as a method for determining the B / A value, it is preferable to evaluate and determine an image (for example, a 4.4 μm × 6.2 μm field of view) observed at 20,000 magnifications with an FE-SEM in the above range 12. . In the diaphragm for alkaline water electrolysis of the present invention, if the B/A value determined in this way is 1.0 or less, both ionic conductivity and gas barrier properties are improved, and it is suitable for use in electrolysis of alkaline water. It can be a diaphragm that can As for the B/A value, if a value of 1.0 or less is obtained as a B/A value from at least one set of A value and B value in a field of view arbitrarily selected in the ranges Ta and Tb, the present invention included in the range of A minimum area size for obtaining A and B values includes an area of 1.0 μm×6.2 μm.

1-4 Remaining amount of nitrogen The diaphragm for alkaline water electrolysis of the present invention has a nitrogen/carbon element atm% of 2.0 to 8.0 as determined by X-ray photoelectron spectroscopy (ESCA) on the surface of the membrane. is preferred. Elements detected by ESCA analysis are carbon, nitrogen, oxygen, magnesium, and sulfur. The above nitrogen/carbon element atm % is more preferably 2.2 to 7.0, still more preferably 2.5 to 6.0. These elemental concentrations are, for example, values obtained by measuring with an X-ray photoelectron spectrometer (JPS-9000MX manufactured by JEOL Ltd., X-ray source: MgKα ray). The nitrogen element detected by ESCA analysis is preferably nitrogen element derived from polyvinylpyrrolidone with a molecular weight of 200,000 or more and 1,300,000 or less. Furthermore, the polyvinylpyrrolidone having a molecular weight of 200,000 or more and 1,300,000 or less is preferably added in the later-described method for producing a diaphragm for alkaline water electrolysis of the present invention. The surface of the diaphragm for alkaline water electrolysis is not particularly limited, and may be, for example, the surface on the single membrane layer 2 side of the diaphragm 1 for alkaline water electrolysis in FIG. 1 or the surface on the support layer 3 side. In the case of the surface on the side of the support layer 3, the calculation excluding the support component is required.
In the diaphragm for alkaline water electrolysis of the present invention, when the nitrogen/carbon element atm% determined by ESCA analysis is within the above-described range, the denseness of the membrane surface layer is further improved in the vicinity of the membrane surface, and the ion conductivity is high. and a high gas barrier property.

1-5 Porosity In the diaphragm for alkaline water electrolysis of the present invention, in the cross section perpendicular to the surface of the membrane, from both ends in the longitudinal direction toward the center, the range is 0.4 a or more with respect to the width a of the cross section. , the porosity C in the range between the surface of the film and a position 1 μm away from the surface of the film in the depth direction, and the position 2 μm away and 15 μm away from the surface of the film in the depth direction. It is preferable that the ratio D/C to the porosity D in the range between is 1.8 or more. The ratio D/C is more preferably 2.0 or more, further preferably 2.2 or more. The upper limit of the ratio D/C is 4.5. When the ratio D/C is set in the range described above, the density of the membrane surface layer is further improved in the vicinity of the membrane surface, and a diaphragm for alkaline water electrolysis that has both high ionic conductivity and high gas barrier properties is obtained. .

The method for calculating the ratio D/C will be specifically described with reference to FIG. In a range Ta between the surface 11 of the film and a position 1 μm away from the surface 11 in the depth direction S in a range 0.4a or more away from the width a, a cross-sectional observation image by FE-SEM measurement is obtained. obtain. Analysis software is used to divide the obtained cross-sectional observation image into a bright portion and a dark portion. Here, the dark areas are voids. Then, the porosity C is obtained as a ratio of the sum of the areas of the dark portions to the area of the entire image.
In addition, in a cross section 10 perpendicular to the surface 11 of the diaphragm for alkaline water electrolysis, from both ends in the longitudinal direction toward the center, in a range separated by 0.4 a or more with respect to the width a of the cross section 10, from the surface 11 of the membrane A cross-sectional observation image is obtained by FE-SEM measurement in a range Tb between a position separated by 2 μm and a position separated by 15 μm. For the cross-sectional observation image thus obtained, the porosity D is obtained as a ratio of the sum of the areas of the dark portions to the area of the entire image in the same manner as described above.
From the porosities C and D thus obtained, the ratio D/C is obtained.

The surface of the diaphragm for alkaline water electrolysis is not particularly limited, and may be, for example, the surface on the single membrane layer 2 side of the diaphragm 1 for alkaline water electrolysis in FIG. 1 or the surface on the support layer 3 side. In the case of the surface on the side of the support layer 3, the calculation excluding the support component is required. As a method for determining the B/A value, it is preferable to determine the B/A value from an image (for example, a 4.4 μm×6.2 μm field of view) observed at a magnification of 20,000 with an FE-SEM in the range 12 above. In the diaphragm for alkaline water electrolysis (3) of the present invention, if the D/C value determined in this way is 1.8 or more, both ionic conductivity and gas barrier properties are improved, and it is suitable for electrolysis of alkaline water. It can be a diaphragm that can be used for As the D/C value, in the field of view arbitrarily selected in the ranges Ta and Tb, if a value of 1.8 or more is obtained as the D/C value from at least one set of C value and D value, the present invention included in the range of The minimum size of the area for obtaining the C value is an area of 1.0 μm×6.2 μm, and the minimum size of the area for obtaining the D value is an area of 4.4 μm×6.2 μm. .

The membrane for alkaline water electrolysis of the present invention preferably has a porosity of 25 to 80%, more preferably 30 to 75%, and even more preferably 35 to 70% as a whole membrane. When the porosity of the membrane as a whole is within the above range, the pores in the diaphragm are more continuously filled with the electrolytic solution, so that the membrane exhibits higher ionic conductivity, more excellent ion permeability, and more excellent gas barrier properties. It can be used as a film.

The porosity of the membrane as a whole is the calculated density value of the diaphragm calculated using the measured density value of the diaphragm measured by the method shown below, and the density value (true density) and composition ratio of each component constituting the diaphragm. It can be calculated from the following formula.
Porosity (%) = [1 - (measured density value) / (calculated density value)] × 100
The measured density value can be calculated by measuring the mass and volume of a test piece cut from an arbitrary location of the obtained diaphragm and dividing the mass by the volume. The volume can be calculated by measuring the vertical and horizontal lengths of the test piece using calipers, and measuring the film thickness based on the film thickness measurement method described above. Also, the mass of the test piece can be measured using a precision balance with four digits below the decimal point for the test piece whose volume has been measured.

1-6 Ionic Conductivity The ionic conductivity of the diaphragm for alkaline water electrolysis of the present invention can be calculated by the method described in Examples. The ion conductivity of the diaphragm for alkaline water electrolysis of the present invention is preferably more than 100 mS/cm. In this case, the electrolysis efficiency in alkaline water electrolysis can be made higher.

1-7 Thickness The thickness of the diaphragm for alkaline water electrolysis of the present invention is not particularly limited, and may be appropriately selected according to the size of the equipment to be used, the handleability, etc. 50 to 2000 μm is preferable, 100 to 1000 μm is more preferable, 100 to 500 μm is still more preferable, and 150 to 350 μm is most preferable from the viewpoint of ion permeability and strength.
Further, when the porous support described above is included, the thickness of the diaphragm for alkaline water electrolysis of the present invention is preferably 50 to 2000 μm, more preferably 100 to 1000 μm, still more preferably 100 to 500 μm, most preferably 150 to 300 μm. is.

2. Method for producing diaphragm for alkaline water electrolysis The method for producing a diaphragm for alkaline water electrolysis of the present invention includes a dispersion preparation step of preparing a dispersion containing inorganic particles, polyvinylpyrrolidone having a molecular weight of 200,000 or more and 1,300,000 or less, and a solvent; A resin mixed solution preparation step of mixing a liquid and an organic polymer resin (R) to prepare a resin mixed solution; and a film forming step of forming a film using the resin mixed solution.
Each step will be described below.

2-1 Dispersion Preparation Step In the above production method, when inorganic particles are mixed with the resin (R), a dispersion is prepared in advance by dispersing the inorganic particles in a solvent and then mixed with the resin (R). Further, in the above-described dispersion liquid preparation step, a dispersion liquid is prepared by adding polyvinylpyrrolidone having a molecular weight of 200,000 or more and 1,300,000 or less to the inorganic particles and the solvent. By preparing a dispersion containing inorganic particles and polyvinylpyrrolidone having a molecular weight of 200,000 or more and 1,300,000 or less and then mixing it with the resin (R), the ratio of the resin (R) in the surface layer of the produced film is increased. In addition, the porosity of the surface layer of the membrane is suppressed to a particularly low value in the vicinity of the membrane surface, resulting in a dense structure, which makes it possible to improve ion conductivity and gas barrier properties at the same time. In order to actively act "polyvinylpyrrolidone with a molecular weight of 200,000 or more and 1,300,000 or less" on the particles so that more "polyvinylpyrrolidone with a molecular weight of 200,000 or more and 1,300,000 or less" remains in the film, " Polyvinylpyrrolidone having a molecular weight of 200,000 or more and 1,300,000 or less" is preferably added. A dispersant other than polyvinylpyrrolidone having a molecular weight of 200,000 or more and 1,300,000 or less may be added to the dispersion liquid.

The lower limit of the molecular weight of polyvinylpyrrolidone having a molecular weight of 200,000 or more and 1,300,000 or less is preferably 250,000, more preferably 300,000. The upper limit of the molecular weight is preferably 1,250,000. By setting the molecular weight of the polyvinylpyrrolidone to be added to 200,000 or more, the residual amount of the polyvinylpyrrolidone in the film is increased, and it is considered that the effect of aggregation of the resin (R) is likely to be exhibited. Further, when the molecular weight of polyvinylpyrrolidone to be added exceeds 1,300,000, the viscosity of the dispersion liquid increases, and the effect of dispersing the particles decreases.
In addition, in this specification, molecular weight is a weight average molecular weight, and can be obtained by measuring under the conditions of the following gel permeation chromatography (GPC) method.
Apparatus: Tosoh HLC-8320GPC
Detector: RI
Column: Shodex KD-806M (2 pieces) manufactured by Showa Denko K.K., KD-G 4A
Column temperature: 40°C
Flow rate: 0.8ml/min
Calibration curve: Polystyrene Standards
Eluent: N,N-dimethylformamide (containing 0.1% LiBr)

The addition amount of polyvinylpyrrolidone having a molecular weight of 200,000 or more and 1,300,000 or less is preferably 1 to 10 parts by mass, more preferably 1 to 8 parts by mass, and further preferably 2 to 7 parts by mass with respect to 100 parts by mass of the inorganic particles. 4 to 6 parts by weight is particularly preferred. Further, it is preferably 3 to 30 parts by mass, more preferably 3 to 40 parts by mass, even more preferably 6 to 30 parts by mass, with respect to 100 parts by mass of the resin (R) mixed in the resin mixture preparation step described later. ~20 parts by weight is particularly preferred.

Examples of the dispersant include cationic surfactants; anionic surfactants; and conventionally known pigment dispersants having a hydrophilic functional group such as a carboxy group, a phosphoric acid group, and a sulfonic acid group.
As the cationic surfactant, a cationic surfactant having a hydrocarbon chain with 5 or more carbon atoms in the molecule is more preferable.
As the anionic surfactant, an anionic surfactant having a hydrocarbon chain with 5 or more carbon atoms in the molecule is more preferable.
The polymer pigment dispersant is not particularly limited as long as it is a polymer having a hydrophilic functional group, but is preferably a polymer having a hydrocarbon chain having 5 or more carbon atoms in its main chain or side chain, and furthermore, a structural unit ( A polymer containing a hydrocarbon chain having 5 or more carbon atoms as a repeating unit) is more preferable, and a polymer containing a polyester or polyether having 5 or more carbon atoms as a structural unit is more preferable.
As such a polymer, even a polymer containing only a structural unit containing a hydrocarbon chain having 5 or more carbon atoms as a repeating unit, a structural unit other than a structural unit containing a hydrocarbon chain having 5 or more carbon atoms may be used. It may be further included as a repeating unit.
In the latter case, even if the polymer consists of a block containing only a structural unit containing a hydrocarbon chain having 5 or more carbon atoms as a repeating unit and a block composed of other structural units, carbon atoms in the molecule It may be a polymer having a structure in which structural units containing hydrocarbon chains of 5 or more and other structural units are randomly connected.
The amount of the dispersant used is preferably 1 to 10 parts by mass, more preferably 1.2 to 8.0 parts by mass, and even more preferably 1.5 to 5.0 parts by mass or less with respect to 100 parts by mass of the solvent. . By doing so, the dispersion stability of the inorganic particles can be improved more effectively.

The content of inorganic particles in the dispersion liquid is preferably 20 to 70% by mass, more preferably 30 to 65% by mass, and still more preferably 50 to 65% by mass.

The solvent for dispersing the inorganic particles is not particularly limited as long as it has the property of dissolving the resin (R) to be mixed later. Examples include N-methyl-2-pyrrolidone and N,N-dimethyl. acetamide, N,N-dimethylformamide, dimethylsulfoxide, methyl ethyl ketone, toluene and the like. These solvents may be used singly or in combination of two or more. Among them, N-methyl-2-pyrrolidone is preferable in terms of good dispersibility of the inorganic particles. The amount of the solvent used relative to the inorganic particles in the dispersion is preferably 50 to 100 parts by mass, more preferably 50 to 90 parts by mass, and even more preferably 50 to 80 parts by mass with respect to 100 parts by mass of the inorganic particles.

The method for dispersing the inorganic particles in the solvent is not particularly limited, and known mixing and dispersing means such as a method using a mixer, ball mill, jet mill, disper, sand mill, roll mill, pot mill, bead mill, paint shaker, etc. are applied. be able to.

The average particle size of the inorganic particles in the dispersion is preferably 0.1 to 1.0 μm, more preferably 0.15 to 0.8 μm, still more preferably 0.15 to 0.5 μm. The average particle size of the inorganic particles in the dispersion liquid is obtained by measuring the particle size of the inorganic particles dispersed in the dispersion liquid using a particle size distribution analyzer based on the dynamic light scattering method, and performing cumulant method analysis. It can be an average particle size.

2-2 Resin mixture preparation step In the resin mixture preparation step, the dispersion prepared in the dispersion preparation step is mixed with the organic polymer resin (R) to prepare a resin mixture. A hydrophilic additive may be added to the resin mixture. The hydrophilic additive may be an organic hydrophilic additive or an inorganic hydrophilic additive. Examples of the organic hydrophilic additive include polyethylene glycol, polyethylene oxide, polyethylene imine having a molecular weight of less than 100,000, polyacrylic acid, water-soluble polymers such as dextran; surfactants; glycerin; Examples of the inorganic hydrophilic additive include calcium chloride, magnesium chloride and lithium chloride. The amount of the hydrophilic additive used is preferably 0.1 parts by mass or more and 20 parts by mass or less with respect to 100 parts by mass of the inorganic particles in the dispersion.

The method for mixing the resin (R) with the dispersion liquid prepared in the dispersion liquid preparation step is not particularly limited as long as it is a method capable of sufficiently mixing the dispersion liquid and the resin (R). The resin (R) may be mixed with the dispersion as it is, or a resin solution may be prepared by dissolving the resin (R) in a solvent in advance, and the resin solution and the dispersion may be mixed. good. Among them, a method of preparing the resin solution and mixing the resin solution and the dispersion to obtain a resin mixed solution is preferred because the inorganic particles and the resin (R) can be more uniformly dispersed and mixed. preferable.

The solvent used for preparing the resin mixture is not particularly limited as long as it has the property of dissolving the resin (R). Examples include N-methyl-2-pyrrolidone and N,N-dimethyl. Acetamide, N,N-dimethylformamide, dimethylsulfoxide, methyl ethyl ketone, toluene and the like. Among them, the same solvent as the solvent used for preparing the dispersion liquid is preferable in that the inorganic particles and the resin (R) can be dispersed and mixed more uniformly.

The content of the resin (R) in the resin solution is preferably 5 to 50% by mass, more preferably 10 to 45% by mass, even more preferably 15 to 40% by mass.
Examples of the mixing method include the same means as the mixing and dispersing means described in the dispersion liquid preparation step.

The dispersion liquid and the resin (R) are preferably 10 to 40 parts by mass, more preferably 12 to 35 parts by mass, still more preferably 15 to 33 parts by mass, based on 100 parts by mass of the inorganic particles. It is preferable to mix so that it becomes a mass part. When the content ratio of the inorganic particles and the resin (R) is within the range described above, the elution of inorganic components in the resulting diaphragm for alkaline water electrolysis in an alkaline solution is further suppressed, and higher ion conductivity is exhibited. In addition, it is possible to produce a diaphragm for alkaline water electrolysis that is more excellent in ion permeability, gas barrier properties, heat resistance and alkali resistance.

When the dispersion of the inorganic particles and the solution of the resin (R) are mixed, the total content of the solvent in the dispersion of the inorganic particles and the solvent in the solution of the resin (R) is the dispersion of the inorganic particles. It is preferably 30 to 75 mass % with respect to 100 mass % of the total mass of the liquid and the solution of the resin (R). More preferably 35 to 70% by mass, still more preferably 40 to 65% by mass. In order to adjust the porosity of the diaphragm for alkaline water electrolysis to a preferable range, it is preferable to use the solvent in such a ratio.

2-3 Film Formation Step In the film formation step, a film is formed using the resin mixture obtained in the resin mixture preparation step.
As a method for forming the membrane, the following steps (a) and (b) can be used in that a diaphragm for alkaline water electrolysis in which the elution of inorganic components in an alkaline solution is further suppressed can be easily produced. is preferably included.
(a) forming a coating film of the resin mixture, and
(b) contacting the coating film with a non-solvent to solidify the coating film to obtain a porous film;

(a) Step of forming a coating film of the resin mixed solution Examples of the method of forming a coating film of the resin mixed solution include a method of applying the resin mixed solution obtained above on a substrate, and a method of applying the resin mixed solution A method of obtaining a base material impregnated with the above-mentioned mixed resin liquid by immersing the base material in the liquid can be used. Among them, the method of applying the above-mentioned resin mixed solution onto a base material is preferable in that a coating film can be easily formed.

The method of applying the resin mixture onto the substrate is not particularly limited, and known coating means such as methods using die coating, spin coating, gravure coating, curtain coating, spray, applicator, bar coater, etc. are applied. can do.

The substrate is not particularly limited as long as it can be coated with the resin mixture to form a coating film. Examples of the substrate include polyethylene terephthalate, polyethylene naphthalate, polypropylene, polyethylene, polyvinyl chloride, and polyvinyl. Examples thereof include films or sheets made of resins such as acetal, polymethyl methacrylate, and polycarbonate, and glass plates. Among them, polyethylene terephthalate is preferable because it is easy to handle and the material cost can be reduced.
Moreover, when manufacturing the diaphragm for alkaline water electrolysis containing the porous support mentioned above, you may use the said porous support as said base material.

In the case of producing a diaphragm for alkaline water electrolysis, which is a composite in which a membrane containing inorganic particles, the resin (R), and a porous support are integrated, the resin mixed solution is applied onto the base material. Then, the porous support may be placed on the coating liquid to impregnate the porous support with the coating liquid.

The amount of the resin mixed solution to be applied is not particularly limited, and may be appropriately set so that the diaphragm has a thickness capable of exhibiting the above-described effects.

(b) a step of solidifying the coating film by contacting the coating film with a non-solvent, thereby causing the non-solvent to diffuse in the coating film and not dissolving in the non-solvent; Resin (R) solidifies. On the other hand, the solvent in the coating film that is soluble in the non-solvent is eluted from the coating film. Due to the occurrence of phase separation in this manner, the resin (R) (and the inorganic particles) is solidified to form a porous film.

Examples of the method of bringing the coating film into contact with the non-solvent include a method of immersing the coating film in the non-solvent (coagulation bath), and a method of exposing the coating film to the non-solvent vapor atmosphere. Alternatively, after the coating film is exposed to the non-solvent vapor atmosphere, it may be subsequently immersed in the non-solvent. In this case, the exposure time to the non-solvent vapor atmosphere can be about 3 to 60 seconds, and the time to be immersed in the non-solvent can be about 1 to 15 minutes.

The temperature of the non-solvent in which the coating film is immersed is preferably 10°C or higher, more preferably 15°C or higher, and even more preferably 20°C or higher. Moreover, 55 degrees C or less is preferable, 50 degrees C or less is more preferable, and 45 degrees C or less is more preferable. By setting such a temperature, more ion paths can be formed in the manufactured diaphragm, and a diaphragm for alkaline water electrolysis that exhibits high ionic conductivity, higher gas barrier properties, and higher durability can be more easily manufactured. can.

The non-solvent is not particularly limited as long as it has the property of not substantially dissolving the resin (R). A mixed solvent or the like can be preferably used. Ion-exchanged water is preferable from the viewpoint of economy and waste liquid treatment. In addition to the components described above, the non-solvent may contain a small amount of the same solvent as the solvent contained in the coating film.

The amount of the non-solvent used is preferably 50 to 10,000 parts by mass with respect to 100 parts by mass of the coating film, ie, 100 parts by mass of the solid content of the resin mixture used for forming the coating film. It is more preferably 100 to 5000 parts by mass, still more preferably 200 to 1000 parts by mass. It is preferable to use the non-solvent in such a ratio in order to adjust the porosity of the membrane to be obtained within a preferable range and to completely extract the solvent in the coating film into the non-solvent.

Furthermore, in order to remove the non-solvent, the coating film solidified in the above step may be dried to obtain the diaphragm.
The drying temperature for the coating film is preferably 60 to 120°C.
The drying time is preferably 0.5 to 120 minutes, more preferably 1 to 60 minutes, even more preferably 1 to 30 minutes.

In the method for producing a diaphragm for alkaline water electrolysis of the present invention, polyvinylpyrrolidone having a molecular weight of 200,000 or more and 1,300,000 or less remains in the non-solvent without partially eluting in the film forming step, thereby densifying the surface of the coating film, and We believe that by making it easier to get wet with the electrolyte, the porosity of the surface layer of the membrane is suppressed to a low value near the surface of the membrane, resulting in a dense structure and the production of a membrane that can improve both ion conductivity and gas barrier properties. be done.

As described above, the diaphragm for alkaline water electrolysis of the present invention can be easily produced by the steps described above.

3. Applications The diaphragm for alkaline water electrolysis of the present invention exhibits high ion conductivity, and simultaneously achieves higher gas barrier properties and higher durability. Therefore, the diaphragm for alkaline water electrolysis of the present invention can be suitably used as a diaphragm for water electrolysis using an alkaline aqueous solution as an electrolyte. In addition to the diaphragm for alkaline water electrolysis described above, it can also be used for battery separators such as alkaline fuel cell separators, primary battery separators, secondary battery separators, and salt electrolysis separators.

4. Alkaline Water Electrolysis Apparatus The diaphragm for alkaline water electrolysis of the present invention is used as a member of an alkaline water electrolysis apparatus. Examples of the alkaline water electrolysis apparatus include those including an anode, a cathode, and the diaphragm for alkaline water electrolysis arranged between the anode and the cathode. More specifically, the alkaline water electrolysis apparatus has an anode chamber in which an anode exists and a cathode chamber in which a cathode exists, which are separated by the diaphragm for alkaline water electrolysis.
The anode and cathode include known electrodes such as conductive substrates containing nickel, nickel alloys, and the like.

5. Electrolysis method The method of electrolyzing water using the alkaline water electrolysis apparatus provided with the diaphragm for alkaline water electrolysis of the present invention is not particularly limited, and a known method can be used. For example, it can be carried out by filling an electrolytic solution into an alkaline water electrolysis apparatus provided with the above-described diaphragm for alkaline water electrolysis of the present invention and applying an electric current in the electrolytic solution.
As the electrolytic solution, an alkaline aqueous solution in which an electrolyte such as potassium hydroxide or sodium hydroxide is dissolved is used. Although the concentration of the electrolyte in the electrolytic solution is not particularly limited, it is preferably 20 to 40% by mass from the viewpoint of further improving the electrolysis efficiency.
The temperature for electrolysis is preferably 50 to 120° C., more preferably 80 to 90° C., since the ion conductivity of the electrolytic solution can be further improved and the electrolysis efficiency can be further improved. Current application conditions can be performed by known conditions and methods.

EXAMPLES The present invention will be described in more detail with reference to examples below, but the present invention is not limited only to these examples. Unless otherwise specified, "part" means "mass part" and "%" means "mass %".

<Example 1>
(1. Preparation of magnesium hydroxide dispersion)
Magnesium hydroxide (average particle size 0.54 μm) and N-methyl-2-pyrrolidone (manufactured by FUJIFILM Wako Pure Chemical Industries, Ltd.) are mixed so that the mass ratio is 1:1, and magnesium hydroxide particles are 100% by mass. Then, 6% by mass of polyvinylpyrrolidone having a molecular weight of 1,200,000 was added, and dispersion treatment was performed at room temperature for 6 hours using a pot mill containing zirconia media balls to prepare a magnesium hydroxide dispersion.

(2. Preparation of polysulfone resin solution)
Polysulfone resin (manufactured by BASF, product number Ultrason S3010) was thermally dissolved in N-methyl-2-pyrrolidone (manufactured by FUJIFILM Wako Pure Chemical Industries, Ltd.) at a concentration of 30% by mass at 80 to 100°C. After that, they were mixed at room temperature for about 10 minutes at 1000 rpm in a rotation-revolution mixer (product number Awatori Mixer ARE-500, manufactured by THINKY Co., Ltd.) to prepare a polysulfone resin solution.

(3. Preparation of coating liquid)
Weigh the magnesium hydroxide dispersion and the polysulfone resin solution obtained above so that the solid content is 40% by mass and the polysulfone resin (PSU) is 33 parts by mass with respect to 100 parts by mass of magnesium hydroxide, Mixing was performed at room temperature at 1000 rpm for about 10 minutes using a rotation/revolution mixer (manufactured by THINKY Co., Ltd., product number Awatori Mixer ARE-500). The resulting mixed liquid was filtered through SUS 200 mesh to obtain a coating liquid.

(4. Formation of coating film)
A polyphenylene sulfide nonwoven fabric (Torcon Paper #100, manufactured by Toray Industries, Inc.) was coated with the solution so that the thickness of the membrane after drying was 250 μm in total, and the nonwoven fabric was completely impregnated with the coating liquid. Thereafter, the nonwoven fabric impregnated with the coating liquid was subjected to a water bath at room temperature for 10 minutes to solidify the coating liquid and form a film. After the water bath, the obtained membrane was dried in a dryer at 80° C. for 30 minutes to obtain a diaphragm for alkaline water electrolysis comprising a composite of a nonwoven fabric, a membrane containing magnesium hydroxide and a polysulfone resin.

(5. Film thickness measurement method)
The thickness of the obtained diaphragm for alkaline water electrolysis was measured using a digimatic micrometer (manufactured by Mitutoyo Corporation). Ten arbitrary points were measured, and the average value was used as the film thickness. The film thickness was 250 μm.

(6. Measurement and calculation method of organic polymer composition ratio in film surface layer)
With respect to the cross section perpendicular to the surface of the obtained diaphragm for alkaline water electrolysis, from both ends in the longitudinal direction toward the center, in a range separated by 0.4 a or more with respect to the width a of the cross section, the surface of the membrane and the surface A cross-sectional observation image (magnification: 20,000 times) was obtained by FE-SEM (manufactured by JEOL Ltd., model number: JSM-7600F) measurement in a range between positions separated by 1 μm.
Analysis software (Image-Pro Premier) is used for the obtained cross-sectional observation image to divide the image into a bright portion, a semi-bright portion, and a dark portion from the brightness histogram, and the area of the semi-bright portion corresponding to the polysulfone resin is calculated. A total value Pa and a total value Sa of the areas of the light and semi-light portions corresponding to the polysulfone resin and magnesium hydroxide were calculated. Then, the ratio A (Pa/Sa) of the sum (Pa) of the area of the polysulfone resin to the sum (Sa) of the areas of the magnesium hydroxide and the polysulfone resin was determined.

Similarly, in the cross section perpendicular to the surface of the obtained diaphragm for alkaline water electrolysis, from both ends in the longitudinal direction toward the center, in a range separated by 0.4 a or more with respect to the width a of the cross section, from the surface of the membrane A cross-sectional observation image (magnification: 20,000 times) was obtained by FE-SEM (manufactured by JEOL Ltd., model number: JSM-7600F) in a range between a position separated by 2 μm and a position separated by 15 μm in the depth direction. .
Analysis software (Image-Pro Premier) was used to divide the image into bright, semi-bright, and dark areas from the brightness histogram of the obtained cross-sectional observation image, and the total area of the semi-bright areas corresponding to the polysulfone resin was calculated. A value Pb and a total value Sb of the areas of the bright and semi-bright portions corresponding to the polysulfone resin and magnesium hydroxide were calculated. Then, the ratio B (Pb/Sb) of the sum of the areas of the polysulfone resin (Pb) to the sum of the areas of the magnesium hydroxide and the polysulfone resin (Sb) was determined.

From the ratios A and B obtained above, the ratio B/A was calculated. As a result, the ratio B/A was 1.0.

(7. Method for measuring residual nitrogen amount)
The nitrogen/carbon element atm% was measured on the surface of the obtained diaphragm for alkaline water electrolysis by X-ray photoelectron spectroscopy (ESCA). As a result, the nitrogen/carbon element was 3.7 atm %.

(8. Measurement and calculation method of porosity ratio in membrane surface layer)
With respect to the cross section perpendicular to the surface of the obtained diaphragm for alkaline water electrolysis, from both ends in the longitudinal direction toward the center, in a range separated by 0.4 a or more with respect to the width a of the cross section, the surface of the membrane and the surface A cross-sectional observation image (magnification: 20,000 times) was obtained by FE-SEM (manufactured by JEOL Ltd., model number: JSM-7600F) measurement in a range between positions separated by 1 μm.
Analysis software (Image-Pro Premier) is used for the obtained cross-sectional observation image to divide the image into bright and dark areas from the brightness histogram, and from the area ratio of the total area of the dark areas corresponding to the voids, A porosity C was determined.

Similarly, in the cross section perpendicular to the surface of the obtained diaphragm for alkaline water electrolysis, from both ends in the longitudinal direction toward the center, in a range separated by 0.4 a or more with respect to the width a of the cross section, from the surface of the membrane A cross-sectional observation image (magnification: 20,000 times) was obtained by FE-SEM (manufactured by JEOL Ltd., model number: JSM-7600F) in a range between a position separated by 2 μm and a position separated by 15 μm in the depth direction. .
Analysis software (Image-Pro Premier) is used for the obtained cross-sectional observation image to divide the image into bright and dark areas from the brightness histogram, and from the area ratio of the total area of the dark areas corresponding to the voids, A porosity D was determined.

A ratio D/C was calculated from the porosities C and D obtained above. As a result, the ratio D/C was 2.2.

(9. Measurement of bubble point value)
The bubble point value of the obtained diaphragm for alkaline water electrolysis was measured using a liquid porosimeter (manufactured by Porous Materials). Specifically, a diaphragm of 2.5 cmφ was immersed in deionized water at room temperature for 1 hour to be sufficiently wet, and then the diaphragm was filled with Galwick (manufactured by Porous Materials), which is a fluorine-based solvent. The gas pressure against the diaphragm was increased, the liquid film of water was broken, Galwick permeated the film, and the gas pressure at the time when the weight was observed with a balance was taken as the bubble point value. The bubble point value of the diaphragm was 1000 kPa or more, which is the upper limit of measurement.

(10. Measurement of Gurley value)
The Gurley value of the obtained diaphragm for alkaline water electrolysis was measured using a digital Oken type air permeability tester EGBO-S-1 (manufactured by Asahi Seiko Co., Ltd.).
The Gurley value of the diaphragm was 600s.

(11. Method for measuring ionic conductivity)
The ionic conductivity of the obtained diaphragm for alkaline water electrolysis was measured by the following measuring method. As a result, it was 160 mS/cm.
(Measuring method)
Prepare two diaphragm samples for measurement.
Using each diaphragm sample, a cell formed with the following cell configuration was allowed to stand in a constant temperature bath at 25° C. for 30 minutes, and then AC impedance was measured under the following measurement conditions. The ionic conductivity is measured by the following formula using the intercept component (Rb) in the absence of a measurement sample and the film thickness value obtained by the film thickness measurement method described above.
The above measurement is performed on two membrane samples, and the average value of the obtained measured values (two points) is calculated and taken as the ionic conductivity of the membrane.
[Ionic conductivity (mS / cm)] = [film thickness (cm)] ÷ [(Ra-Rb) × 1000 × 1.77]
(Measurement condition)
・Cell configuration Working electrode: Ni plate Counter electrode: Ni plate Electrolyte solution: 30% by mass potassium hydroxide aqueous solution Sample pretreatment: immersed overnight in the above electrolyte solution Effective area for measurement: 1.77 cm ²
- AC impedance measurement conditions Applied voltage: 10 mV vs. Open circuit voltage Frequency range: 100kHz to 100Hz

<Example 2>
A diaphragm for alkaline water electrolysis was obtained in the same manner as in Example 1, except that the amount of polyvinylpyrrolidone used was changed to 10% by mass with respect to 100% by mass of magnesium hydroxide particles. The film thickness is 270 μm, the ratio B/A is 0.8, the ratio D/C is 3.1, the bubble point value is 1000 kPa or more, which is the upper limit, the Gurley value is 10600 S, and the nitrogen/carbon elements on the film surface are 6.5 atm. %Met.
As a result of measuring the ionic conductivity of the obtained diaphragm for alkaline water electrolysis in the same manner as in Example 1, it was 140 mS/cm.

<Comparative Example 1>
A diaphragm for alkaline water electrolysis was obtained in the same manner as in Example 1, except that polyvinylpyrrolidone was not used. The film thickness is 240 μm, the ratio B/A is 1.3, the ratio D/C is 1.5, the bubble point value is 1000 kPa or more, which is the upper limit of measurement, the Gurley value is 69 S, and the nitrogen/carbon elements on the film surface are 0 atm %. Met.
As a result of measuring the ionic conductivity of the obtained diaphragm for alkaline water electrolysis in the same manner as in Example 1, it was 135 mS/cm.

<Comparative Example 2>
A diaphragm for alkaline water electrolysis was obtained in the same manner as in Example 1, except that the molecular weight of polyvinylpyrrolidone was changed to 100,000 and 3% by mass was added to 100% by mass of magnesium hydroxide particles. The film thickness was 260 μm, the ratio B/A was 1.1, the ratio D/C was 1.5, the bubble point value was 490 kPa, the Gurley value was 279 S, and the nitrogen/carbon elements on the film surface were 1.8 atm %. rice field.
As a result of measuring the ion conductivity of the obtained diaphragm for alkaline water electrolysis in the same manner as in Example 1, it was 150 mS/cm.

Comparing Example 1 and Comparative Example 1, the bubble point value was the same, exceeding the upper limit, but Example 1 had a larger Gurley value and improved denseness (improved gas barrier properties). The ionic conductivity values of both the examples and the comparative examples were all good values, but in the examples, both the ionic conductivity and the gas barrier property could be achieved at a higher level.

1 Diaphragm for alkaline water electrolysis 2 Single membrane layer 3 Support layer 10 Cross section of diaphragm for alkaline water electrolysis 11 Surface a of diaphragm for alkaline water electrolysis Width S of cross section perpendicular to surface of diaphragm for alkaline water electrolysis Diaphragm for alkaline water electrolysis Depth direction Ta, Tb measurement range from the surface of

Claims (3)

A diaphragm for alkaline water electrolysis containing an organic polymer and inorganic particles,
In the cross section perpendicular to the surface of the film, from both ends in the longitudinal direction toward the center, in a range separated by 0.4 a or more with respect to the width a of the cross section, the surface of the film and the depth direction from the surface of the film The ratio A (Pa/Sa) of the sum of the areas of the organic polymer to the sum of the areas of the inorganic particles and the organic polymer (Sa) in the range between the position 1 μm away and the depth from the surface of the film The ratio B (Pb/Sb) of the sum of the areas of the organic polymer (Pb) to the sum of the areas of the inorganic particles and the organic polymer (Sb) in the range between the positions separated by 2 μm and the positions separated by 15 μm in the direction A diaphragm for alkaline water electrolysis having a ratio B/A of 0.6 or more and 1.0 or less. In the cross section perpendicular to the surface of the diaphragm for alkaline water electrolysis, from both ends in the longitudinal direction toward the center, in a range separated by 0.4 a or more with respect to the width a of the cross section, the surface of the membrane and the surface of the membrane The ratio D of the porosity C in the range between the position 1 μm away in the depth direction and the porosity D in the range between the position 2 μm away in the depth direction and the position 15 μm away from the surface of the film /C is 1.8 or more,
The diaphragm for alkaline water electrolysis according to claim 1. a dispersion preparation step of preparing a dispersion containing inorganic particles, polyvinylpyrrolidone having a weight average molecular weight of 200,000 or more and 1,300,000 or less, and a solvent;
a resin mixture preparation step of mixing the dispersion and the organic polymer resin (R) to prepare a resin mixture;
including a film forming step of forming a film using the resin mixture;
In the dispersion liquid adjustment step, the amount of the polyvinylpyrrolidone added is 1 to 10 parts by mass with respect to 100 parts by mass of the inorganic particles.
A method for producing a diaphragm for alkaline water electrolysis.

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