JP2008144262A - Ion permeable diaphragm - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide an ion permeable diaphragm used for an alkaline water electrolytic apparatus and having low electric resistance. <P>SOLUTION: The ion permeable diaphragm 1 is formed by incorporating a calcium phosphate compound or a calcium fluoride as a hydrophilic inorganic material in a diaphragm material 1A and the calcium phosphate compound is preferably fluoroapatite or hydroxyapatite. The diaphragm material 1A is prepared by making a stretched organic fiber cloth inherent in a diaphragm forming mixture formed from the hydrophilic inorganic material and an organic binder material selected from polysulfone, polypropylene, polyvinylidene fluoride and the like. <P>COPYRIGHT: (C)2008,JPO&INPIT

Description

  The present invention relates to an ion permeable diaphragm for use in an alkaline water electrolysis apparatus, and more particularly to an ion permeable diaphragm for use in an alkaline water electrolysis apparatus having a structure in which an ion permeable diaphragm is sandwiched between electrodes.

  Reflecting the recent energy situation, hydrogen is attracting attention from various fields as a new energy source to replace oil. Examples of such an industrial production method of hydrogen include coke and petroleum gasification methods and water electrolysis methods.

  The former method has a problem that the operation is complicated and a very large-scale facility is required, so that the initial cost is considerably increased.

  On the other hand, the latter method uses readily available water as a raw material, and a plurality of electrode pairs are provided in an electrolytic cell, and an alkaline electrolyte such as KOH is circulated between these electrodes and ion permeation is performed. The membrane is divided by a permeable membrane to generate hydrogen on the cathode side and oxygen on the anode side of the ion permeable membrane, but there is an ion permeable membrane and an electrolyte solution between the electrodes. Therefore, there are problems that electric resistance is large and electrolysis efficiency is poor. However, since this water electrolysis method can generate hydrogen even in a relatively small facility and is practical, improvement in electrolysis efficiency is desired.

By the way, the following performance is required for a diaphragm used in an electrochemical electrolytic cell represented by such an alkaline water electrolysis apparatus.
(1) Pass only ions through the membrane and do not allow gas to pass or diffuse (2) Be physically and chemically durable in the electrolyte (3) Low electrical resistance

  As a diaphragm for electrolysis having such performance, asbestos cloth is widely used practically. However, despite the fact that the electrolyte solution sometimes exceeds 100 ° C, asbestos cloth cannot be used due to corrosion at temperatures of 100 ° C or higher, and in recent years there have been many reports of health damage caused by asbestos. There is a big problem with its use.

Therefore, while satisfying the above performances (1) and (2), and (3) a polymer porous membrane, an ion exchange membrane, or a metal oxide membrane such as NiO as an ion permeable membrane having a lower electrical resistance. (See Patent Document 1) and ion-permeable diaphragms (see Patent Document 2) using a composite material of an inorganic substance and an organic polymer as a diaphragm material have been proposed.
Japanese Examined Patent Publication No. 62-50557 Japanese Patent No. 2607734

  However, among the ion permeable membranes made of each of the above membrane materials, the polymer porous membrane has the advantage that it is flexible and highly resistant to mechanical damage, but the polymer material used here is Since it is hydrophobic, there is a problem that even if it is porous, movement of ions solvated in the electrolyte is not easy, electric resistance increases, and the performance of the electrolytic cell is severely degraded. In addition, in a polymer porous membrane or an ion exchange membrane, in an alkaline water electrolysis device that generates gas, there is a problem that gas bubbles adhere to the surface of the membrane and electrical resistance increases, and in particular, bubbles are concentrated. In particular, when the electrical resistance greatly increases, there is a problem that a high temperature portion called a so-called hot spot is generated and the diaphragm is deteriorated.

  Further, a metal oxide film such as NiO described in Patent Document 1 is manufactured by sintering, but a dense sintered diaphragm without gas diffusion or permeation has a limit in size. Therefore, there is a problem that it is not suitable for application to a large electrolytic cell.

  And the ion-permeable membrane which used the composite material of the inorganic substance and organic polymer described in patent document 2 as a membrane uses zirconium oxide, polyantimonic acid as an inorganic wettable material, fluorocarbon polymer, polysulfone, etc. Are formed as a binder to form fine pores. An ion-permeable diaphragm using this composite material exhibits excellent smoothness and very good ion conductivity, and is suitable as a diaphragm for an alkaline water electrolysis apparatus.

  However, although the inorganic wettable material used for the ion permeable diaphragm described in Patent Document 2 has wettability, an inorganic material having higher hydrophilicity is used to reduce the electric resistance of the ion permeable diaphragm. There is a need, and there is still room for improvement.

  An object of the present invention is to solve the above-mentioned conventional problems and to provide an ion-permeable diaphragm having a low electrical resistance for use in an alkaline water electrolysis apparatus.

  In order to solve the above-mentioned problems, the present invention provides an ion permeable diaphragm used for alkaline water electrolysis, wherein the membrane material of the ion permeable diaphragm contains a calcium phosphate compound or calcium fluoride as a hydrophilic inorganic material. An ion-permeable diaphragm is provided (claim 1).

  According to the above invention (invention 1), ions in alkaline water electrolysis can quickly pass through the ion-permeable diaphragm with increased hydrophilicity, and therefore the electrical resistance of the membrane itself can be reduced, and this Since the porous structure of the ion-permeable diaphragm is dense and bubbles cannot pass through this hole, oxygen generated on the anode side is not mixed with hydrogen generated on the cathode side of the ion-permeable diaphragm. High purity can be maintained.

  In the said invention (invention 1), it is preferable that the said calcium phosphate compound as said hydrophilic inorganic material is a fluoroapatite (FAP) or a hydroxyapatite (HAP) (inventions 2 and 3). In the invention described above (Inventions 1 to 3), the membrane material contains an organic fiber cloth in a mixture of the hydrophilic inorganic material and an organic binder selected from polysulfone, polypropylene, and polyvinylidene fluoride. It is preferable that it is made (claim 4). Furthermore, in the said invention (invention 4), it is preferable that the said organic fiber cloth is a mesh of polypropylene (invention 5).

  According to the above inventions (Inventions 2 to 5), the membrane material itself has a very good hydrophilicity and exhibits excellent ionic conductivity, so that it is suitable as a diaphragm for an alkaline water electrolysis device. be able to.

  Furthermore, in the said invention (invention 1-5), it is preferable that the thickness of the said film | membrane material is 100 micrometers or more (invention 6). By increasing the thickness of the film material, the desired film strength can be secured, while the electric resistance of the film may increase. According to the invention (invention 6), the film material Since it has good hydrophilicity and excellent ionic conductivity, the electrical resistance of the film does not increase even if the thickness of the film material is increased to some extent, and the desired film strength can be secured. it can.

  According to the ion permeable membrane of the present invention, ions in alkaline water electrolysis can quickly pass through the ion permeable membrane with increased hydrophilicity, so that the electrical resistance in the membrane can be reduced. Reduction of power consumption and improvement of electrolysis efficiency are achieved. In addition, oxygen generated on the anode side is not mixed with hydrogen generated on the cathode side of the ion-permeable diaphragm, and there is no possibility that the hydrogen production efficiency is reduced.

Embodiments of the present invention will be described below in detail with reference to the drawings.
FIG. 1 is an enlarged cross-sectional view showing one unit of an electrolysis unit of an alkaline water electrolysis apparatus using an ion permeable diaphragm according to an embodiment of the present invention.

  In FIG. 1, the ion-permeable diaphragm 1 is held in a form sandwiched between mesh-like electrodes 2 and 3, and these mesh-like electrodes 2 and 3 are connected via conductive members 2A and 3A. The bipolar electrodes 4 and 5 are respectively connected to the anode side 4A and the cathode side 5A. Thereby, a voltage is applied between the ion permeable diaphragms 1. In FIG. 1, 6 is an electrolytic cell, and W is a potassium hydroxide (KOH) solution as an alkaline solution.

  As the membrane material 1A for forming the ion-permeable diaphragm 1, only ions are allowed to pass through the membrane, there is no gas passage or diffusion, and the material is physically and chemically durable in an alkaline solution. There is no particular limitation.

  For example, as the membrane material 1A, a stretched organic fiber cloth is contained in a film-forming mixture containing a hydrophilic inorganic material and an organic binding material selected from polysulfone, polypropylene, polyvinylidene fluoride, and the like. It is preferable.

  As the hydrophilic inorganic material, a calcium phosphate compound such as fluoroapatite (FAP) or hydroxyapatite (HAP) is preferably used, and these hydrophilic inorganic materials are preferably used in the form of granules. The particles of the hydrophilic inorganic material preferably have a particle size of 5 μm or less, particularly preferably fine particles having a particle size of 1 μm or less. Therefore, you may grind | pulverize this granular material finely with a mortar beforehand.

In addition, calcium fluoride (CaF ₂ ) is suitable as the hydrophilic inorganic material other than the calcium phosphate compound. This calcium fluoride is also preferably fine particles of 1 μm or less, like the above-mentioned calcium phosphate compound. Moreover, this calcium fluoride can utilize what is marketed as an industrial chemical, and can utilize what is collect | recovered industrially. For example, in the treatment process of fluorine-containing wastewater, fluorine is removed after being fixed as CaF _{2 and} can be reused.

Further, as the organic fiber cloth, a mesh made of polypropylene, a mesh made of a pre-halogenated ethylene copolymer such as ethylene and monochlorotrifluoroethylene, or the like can be used. As this organic fiber cloth, a woven fabric or a non-woven fabric can be used. The fiber diameter is preferably 1 mm or less, and particularly preferably the fiber diameter is 0.5 mm or less. The size of the weave of the organic fiber cloth is not particularly limited, but is preferably 4 mm ² or less, and particularly preferably 1 mm ² or less.

The film material 1A composed of the hydrophilic inorganic material, the organic binding material, and the organic fiber cloth as described above can be manufactured as follows, for example.
First, an organic binder is dissolved in an organic solvent, and a hydrophilic inorganic material is dispersed therein to prepare a suspension (slurry). A wet sheet is manufactured by uniformly applying this suspension (slurry) to a predetermined thickness on a smooth surface made of an inert material such as a glass plate. Then, the organic fiber cloth is immersed in this wet sheet in a stretched state, and the organic solvent is removed by evaporation or leaching in a water bath while maintaining the stretch of the organic fiber cloth. 1A is peeled off.

  Here, as the organic solvent, for example, dimethylformamide, dimethylacetamide, dimethylsulfoxide, N-methyl-2-pyrrolidone, mono- and diethers of ethylene glycol, or ketones such as methyl ethyl ketone can be used.

Moreover, it is preferable that the blending ratio of the hydrophilic inorganic material (FAP, HAP, CaF ₂ ) and the organic binding material in the film material 1A is 10 to 95% by mass. When the blending ratio of the hydrophilic inorganic material is less than 10% by mass, the electric resistance of the obtained membrane material 1A itself is increased, which is not preferable from the viewpoint of the electric resistance of the ion-permeable diaphragm 1 using the same. On the other hand, if the blending ratio of the hydrophilic inorganic material exceeds 95% by mass, the mechanical strength of the film material 1A, particularly the brittleness, becomes too low, and it may be difficult to maintain the form as a film. A preferable blending ratio of the hydrophilic inorganic material is 40 to 90% by mass, particularly 75 to 85% by mass.

  As the blending ratio of the hydrophilic inorganic material is larger than that of the organic binding material, the wettability (hydrophilicity) of the film material increases and the electric resistance of the film tends to decrease.

  Hydroxyapatite (HAP) as a hydrophilic inorganic material has a lower electrical resistance as the blending ratio is higher, but it is poor in miscibility with an organic binder and an organic solvent, and has the same mass as fluoroapatite (FAP). %, The slurry has a high viscosity and is easily separated. For this reason, when using a hydroxyapatite (HAP) as a hydrophilic inorganic material, it is preferable to prepare a slurry with a blending ratio of hydroxyapatite (HAP) of at most about 60 to 70% by mass.

  Fluoroapatite (FAP) as a hydrophilic inorganic material has a good mixing property with an organic binder and an organic solvent, and can prepare a slurry at the above-mentioned blending ratio of 10 to 95% by mass. It is preferable to prepare a slurry at a blending ratio of 75 to 85% by mass.

  Therefore, it is preferable to use fluoroapatite (FAP) from the viewpoint of handling as the hydrophilic inorganic material used for the membrane material.

  In addition, the compounding ratio of the organic solvent should just be 40 mass% or more in a total of 100 mass% with the organic binder which is a film formation substance. In addition, the thickness of the wet sheet to be manufactured is preferably 2 mm or less, and particularly preferably 1.5 mm or less.

  The thickness (t) of the film material 1A produced in this way is preferably 100 μm or more, particularly 300 to 600 μm. If the thickness of the membrane material 1A is less than 100 μm, the strength as the membrane material 1A for alkaline water electrolysis may not be sufficient. Even if the thickness of the film material 1A is 100 μm or more, the electric resistance of the film does not increase.

Ion-permeable membrane 1 as described above, KOH solution of 1 mol / L, under the conditions of 25 ℃, 1.75Ωcm ² below, in particular a 1.40Omucm ² below the membrane resistance (electrical resistance).

In the electrolysis unit shown in FIG. 1 using such an ion-permeable diaphragm 1, when a current is passed through the bipolar electrodes 4 and 5, a voltage is generated between the conductive members 2A and 3A and the mesh-like electrodes 2 and 3, Electrolysis of the potassium hydroxide solution W generates oxygen (O ₂ ) at the interface between the ion permeable diaphragm 1 and the mesh electrode 2 (anode).

Then, twice the amount of hydrogen (H ₂ ) is generated at the interface between the ion permeable diaphragm 1 and the mesh electrode 3 (cathode). Since the electrolytic cell 6 in this electrolysis unit is divided into the cathode side and the anode side by the ion permeable diaphragm 1, hydrogen gas can be produced by recovering only hydrogen generated on the cathode side.

  At this time, the ion permeable diaphragm 1 contains an inorganic material (inorganic wettable substance) excellent in hydrophilicity, and the membrane material 1A has a porous structure, so that a potassium hydroxide solution is obtained. Since ions therein move quickly, the electrical resistance of the ion-permeable diaphragm 1 is reduced, and alkaline water electrolysis can be performed efficiently.

  Moreover, the porous structure of the membrane material 1A is dense, and the solution passes through, but the oxygen gas bubbles generated on the anode side and the hydrogen gas bubbles generated on the cathode side pass through the ion-permeable diaphragm 1. Since this is not possible, there is no possibility that these gases will be mixed with each other. Therefore, the purity of the hydrogen gas obtained from the cathode side can be kept high.

  The embodiment described above is described for facilitating understanding of the present invention, and is not described for limiting the present invention. Therefore, each element disclosed in the above embodiment is intended to include all design changes and equivalents belonging to the technical scope of the present invention.

  EXAMPLES Hereinafter, although this invention is demonstrated further in detail based on an Example and a comparative example, this invention is not limited to the following Example at all.

Example 1 Production of Fluoroapatite (FAP) -Containing Membrane Material N-methyl-2-pyrrolidone (NMP) 60% by mass (30 g), average particle size of 5 μm fluoroapatite (FAP, manufactured by Kanto Chemical Co.) 32% by mass (16 g) and polysulfone (PSF, manufactured by Solvay Advanced Polymers, Inc., trade name: UDEL) 8% by mass (4 g) are mixed and sufficiently stirred to dissolve polysulfone (PSF), and FAP is dispersed and suspended. A liquid was prepared.

  This suspension was made of 10 cm × 10 cm glass with a 200 mesh polypropylene fiber cloth (fiber diameter: 87 μm, manufactured by NBC, trade name: nip (polypropylene) strong net) placed at a position 400 μm from the bottom. 10 mL was poured onto the frame body of No. 1 to prepare a wet sheet having a surface area of 100 cm 2 and a thickness of about 500 μm.

  Immediately after pouring the suspension, the frame was transferred into a water bath and allowed to stand at room temperature for 5 minutes, and N-methyl-2-pyrrolidone (NMP) as a solvent was leached from the wet sheet. Thereafter, the sheet remaining on the frame was peeled off and held for 5 minutes in water to obtain a sheet-like film material. The obtained sheet-like membrane material had a thickness of about 400 μm.

[Example 2] Production of membrane material containing hydroxyapatite (HAP) N-methyl-2-pyrrolidone (NMP) 65% by mass (30 g), hydroxyapatite having an average particle size of 5 μm (HAP, manufactured by Kishida Chemical Co., Ltd.) 26% by mass (12 g) and 9% by mass (4 g) of polysulfone (PSF, manufactured by Solvay Advanced Polymers, Inc., trade name: UDEL) are mixed and sufficiently stirred to dissolve the polysulfone (PSF) and disperse the hydroxyapatite (HAP). To prepare a suspension.

  From this suspension, a sheet-like membrane material having a thickness of about 400 μm was produced in the same manner as in Example 1.

[Example 3] Manufacture of calcium fluoride (CaF ₂ ) -containing membrane material Calcium fluoride (CaF ₂ , manufactured by Kishida Chemical Co., Ltd.) with 65% by mass (30 g) of N-methyl-2-pyrrolidone (NMP) and an average particle size of 5 μm ) 26 mass% (12 g) and polysulfone (PSF, manufactured by Solvay Advanced Polymers, Inc., trade name: UDEL) 9 mass% (4 g) are mixed and stirred sufficiently to dissolve polysulfone (PSF) and calcium fluoride. (CaF ₂ ) was dispersed to prepare a suspension.

  From this suspension, a sheet-like membrane material having a thickness of about 400 μm was produced in the same manner as in Example 1.

[Comparative Example 1] Production of zirconia oxide-containing membrane material (a membrane corresponding to the permeable membrane described in Japanese Patent No. 2607734) Oxidation with 60 mass% (30 g) of N-methyl-2-pyrrolidone (NMP) and an average particle size of 5 µm Zirconium (ZrO ₂ , manufactured by Kishida Chemical Co., Ltd.) 32% by mass (16 g) and polysulfone (PSF, manufactured by Solvay Advanced Polymers Co., Ltd., trade name: UDEL) 8% by mass (4 g) were mixed and stirred sufficiently to prepare polysulfone (PSF). ) Was dissolved and zirconium oxide was dispersed to prepare a suspension.

  From this suspension, a sheet-like membrane material having a thickness of about 400 μm was produced in the same manner as in Example 1.

<Measurement of electrical resistance>
The ion permeable membranes of Examples 1 to 3 and Comparative Example obtained as described above were immersed in a 1 mol / L KOH solution, and the resistance of these ion permeable membranes was measured at 25 ° C. and an alternating current of 1000 Hz. Membrane resistance was measured using a vessel (manufactured by Yana Core Scientific).
The results are shown in Table 1.

As shown in Table 1, the ion-permeable membranes of Examples 1 to 3 all had a membrane resistance of 1.00 Ωcm ² or less, whereas the ion-permeable membrane of Comparative Example 1 corresponding to Japanese Patent No. 2607734 The diaphragm had a membrane resistance of 6.02 Ωcm ² . In particular, the ion permeable membranes of Example 1 and Example 3 containing FAP and CaF ₂ had a very low film resistance of 0.400 Ωcm ² or less.

<Measurement of electrolysis voltage>
Using a 25% KOH solution, the electrolysis unit as shown in FIG. 1 is subjected to water electrolysis at 80 ° C. using the ion-permeable diaphragms of Examples 1 to 3 and Comparative Example 1, and the electrolysis voltage is measured. Was calculated.
The results are shown in Table 2.

  As shown in Table 2, the electrolysis voltage when performing electrolysis using each ion-permeable diaphragm is lower in the electrolysis voltage of the diaphragm of each example than the diaphragm of the comparative example, and has better energy efficiency. And the result was obtained.

It is an expanded sectional view showing one unit of an electrolysis unit of an alkaline water electrolysis device using an ion permeable diaphragm concerning one embodiment of the present invention.

Explanation of symbols

DESCRIPTION OF SYMBOLS 1 ... Ion-permeable diaphragm 1A ... Membrane material 2 ... Electrode (anode)
2A ... conductive member 3 ... electrode (cathode)
3A ... conductive members 4, 5 ... bipolar electrode 6 ... electrolytic cell W ... potassium hydroxide (KOH) solution (alkali solution)
t: thickness of membrane material

Claims (6)

An ion permeable membrane used for alkaline water electrolysis,
An ion permeable membrane characterized in that the membrane material of the ion permeable membrane contains a calcium phosphate compound or calcium fluoride as a hydrophilic inorganic material.   The ion-permeable membrane according to claim 1, wherein the calcium phosphate compound as the hydrophilic inorganic material is fluoroapatite.   The ion-permeable membrane according to claim 1, wherein the calcium phosphate compound as the hydrophilic inorganic material is hydroxyapatite.   The membrane material is a mixture of the hydrophilic inorganic material and an organic binding material selected from polysulfone, polypropylene, and polyvinylidene fluoride, and an organic fiber cloth is contained therein. 4. The ion permeable membrane according to any one of 3 above.   The ion-permeable diaphragm according to claim 4, wherein the organic fiber cloth is a polypropylene mesh.   The ion permeable membrane according to any one of claims 1 to 5, wherein the membrane material has a thickness of 100 µm or more.

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