WO2016042801A1 - Unité d'électrode, bain électrolytique muni de l'unité d'électrode, dispositif d'électrolyse, et procédé de fabrication d'électrode de l'unité d'électrode - Google Patents

Unité d'électrode, bain électrolytique muni de l'unité d'électrode, dispositif d'électrolyse, et procédé de fabrication d'électrode de l'unité d'électrode Download PDF

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WO2016042801A1
WO2016042801A1 PCT/JP2015/056388 JP2015056388W WO2016042801A1 WO 2016042801 A1 WO2016042801 A1 WO 2016042801A1 JP 2015056388 W JP2015056388 W JP 2015056388W WO 2016042801 A1 WO2016042801 A1 WO 2016042801A1
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electrode
electrode unit
hole
porous
unit according
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PCT/JP2015/056388
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English (en)
Japanese (ja)
Inventor
内藤　勝之
典裕 吉永
梅　武
富松　師浩
亮介 八木
横田　昌広
英男 太田
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株式会社 東芝
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Priority to JP2016505346A priority Critical patent/JP6441308B2/ja
Priority to CN201580043891.1A priority patent/CN106661743B/zh
Priority to US15/065,170 priority patent/US20160186335A1/en
Publication of WO2016042801A1 publication Critical patent/WO2016042801A1/fr

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    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/46104—Devices therefor; Their operating or servicing
    • C02F1/46109—Electrodes
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B1/00—Electrolytic production of inorganic compounds or non-metals
    • C25B1/01—Products
    • C25B1/24—Halogens or compounds thereof
    • C25B1/26—Chlorine; Compounds thereof
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B11/00—Electrodes; Manufacture thereof not otherwise provided for
    • C25B11/02—Electrodes; Manufacture thereof not otherwise provided for characterised by shape or form
    • C25B11/03—Electrodes; Manufacture thereof not otherwise provided for characterised by shape or form perforated or foraminous
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B11/00—Electrodes; Manufacture thereof not otherwise provided for
    • C25B11/04—Electrodes; Manufacture thereof not otherwise provided for characterised by the material
    • C25B11/051—Electrodes formed of electrocatalysts on a substrate or carrier
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B11/00—Electrodes; Manufacture thereof not otherwise provided for
    • C25B11/04—Electrodes; Manufacture thereof not otherwise provided for characterised by the material
    • C25B11/051—Electrodes formed of electrocatalysts on a substrate or carrier
    • C25B11/055—Electrodes formed of electrocatalysts on a substrate or carrier characterised by the substrate or carrier material
    • C25B11/057—Electrodes formed of electrocatalysts on a substrate or carrier characterised by the substrate or carrier material consisting of a single element or compound
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B11/00—Electrodes; Manufacture thereof not otherwise provided for
    • C25B11/04—Electrodes; Manufacture thereof not otherwise provided for characterised by the material
    • C25B11/051—Electrodes formed of electrocatalysts on a substrate or carrier
    • C25B11/073—Electrodes formed of electrocatalysts on a substrate or carrier characterised by the electrocatalyst material
    • C25B11/075—Electrodes formed of electrocatalysts on a substrate or carrier characterised by the electrocatalyst material consisting of a single catalytic element or catalytic compound
    • C25B11/077—Electrodes formed of electrocatalysts on a substrate or carrier characterised by the electrocatalyst material consisting of a single catalytic element or catalytic compound the compound being a non-noble metal oxide
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B13/00—Diaphragms; Spacing elements
    • C25B13/02—Diaphragms; Spacing elements characterised by shape or form
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B13/00—Diaphragms; Spacing elements
    • C25B13/04—Diaphragms; Spacing elements characterised by the material
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B9/00—Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
    • C25B9/17—Cells comprising dimensionally-stable non-movable electrodes; Assemblies of constructional parts thereof
    • C25B9/19—Cells comprising dimensionally-stable non-movable electrodes; Assemblies of constructional parts thereof with diaphragms
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/467—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction
    • C02F1/4672—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction by electrooxydation
    • C02F1/4674—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction by electrooxydation with halogen or compound of halogens, e.g. chlorine, bromine
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/46104—Devices therefor; Their operating or servicing
    • C02F1/46109—Electrodes
    • C02F2001/46152—Electrodes characterised by the shape or form
    • C02F2001/46157—Perforated or foraminous electrodes
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/46104—Devices therefor; Their operating or servicing
    • C02F1/46109—Electrodes
    • C02F2001/46152—Electrodes characterised by the shape or form
    • C02F2001/46157—Perforated or foraminous electrodes
    • C02F2001/46161—Porous electrodes
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00—Apparatus for treatment of water, waste water or sewage
    • C02F2201/46—Apparatus for electrochemical processes
    • C02F2201/461—Electrolysis apparatus
    • C02F2201/46105—Details relating to the electrolytic devices
    • C02F2201/46115—Electrolytic cell with membranes or diaphragms

Definitions

  • Embodiment described here is related with the manufacturing method of the electrode of an electrode unit, an electrolytic cell provided with an electrode unit, an electrolysis apparatus, and an electrode unit.
  • This electrolysis apparatus includes an electrolysis tank and an electrode unit provided in the electrolysis tank.
  • an electrolyzer having a three-chamber type electrolytic cell has been proposed.
  • the inside of the electrolytic cell is divided into three chambers, an intermediate chamber, and an anode chamber and a cathode chamber located on both sides of the intermediate chamber, by a cation exchange membrane and an anion exchange membrane constituting the electrode unit.
  • the anode chamber and the cathode chamber the anode and cathode of the electrode unit are provided, respectively.
  • an electrode a porous electrode in which a large number of through holes are processed on a metal plate base material by expanding, etching, or punching is used.
  • salt water is passed through the intermediate chamber, and water is circulated through the anode chamber and the cathode chamber, respectively.
  • hypochlorous acid water is generated from the chlorine gas generated at the anode
  • sodium hydroxide water is generated in the cathode chamber.
  • the produced hypochlorous acid water is used as sterilizing / disinfecting water
  • sodium hydroxide water is used as washing water.
  • the anion exchange membrane is easily deteriorated by chlorine or hypochlorous acid. Further, when the porous electrode and the ion exchange membrane (electrolyte membrane) are brought into close contact with each other, stress tends to concentrate on the edge portion of the hole of the electrode, and the membrane such as a thin electrolyte membrane having a low mechanical strength tends to deteriorate. Therefore, a technique has been proposed in which a non-woven fabric with an overlap or a cut is inserted between the porous electrode and the electrolyte membrane to reduce the deterioration of the electrode due to chlorine. Also known is an electrode unit in which a porous inorganic oxide film is formed of sol or gel on a flat valve electrode.
  • the problem to be solved by the present invention is to provide a long-life electrode unit, an electrolysis apparatus, and a method for producing an electrode for an electrode unit that can maintain electrolytic performance over a long period of time.
  • the electrolysis apparatus includes an electrode unit.
  • the electrode unit includes a first electrode having a first surface, a second surface located on the opposite side of the first surface, and a plurality of through holes opening in the first surface and the second surface, respectively.
  • a second electrode provided opposite to the first surface of the first electrode, and a porous hole formed on the first surface of the first electrode and containing the inorganic oxide and covering the first surface and the through hole And a membrane.
  • FIG. 1 is a cross-sectional view showing an electrolysis apparatus according to the first embodiment.
  • FIG. 2 is an exploded perspective view showing an electrode unit of the electrolysis apparatus according to the first embodiment.
  • FIG. 3A is an enlarged cross-sectional view showing an electrode and a porous membrane of the electrode unit.
  • FIG. 3B is an enlarged cross-sectional view showing an electrode and a porous film of the electrode unit.
  • FIG. 3C is a cross-sectional view schematically showing a porous film composed of a laminated film.
  • FIG. 3D is a cross-sectional view schematically showing a porous film made of an inorganic oxide film having pores that are irregular in a plane or three-dimensionally.
  • FIG. 4 is a cross-sectional view showing an electrode unit according to a first modification.
  • FIG. 5 is a cross-sectional view showing an electrode and a porous membrane of an electrode unit according to a second modification.
  • FIG. 6 is a perspective view showing an electrolysis apparatus according to the second embodiment.
  • FIG. 7 is an exploded perspective view showing an electrode unit of the electrolysis apparatus according to the second embodiment.
  • FIG. 8 is a cross-sectional view showing an electrode unit according to the second embodiment.
  • FIG. 9 is a cross-sectional view illustrating a manufacturing process of an electrode of an electrode unit according to the second embodiment.
  • FIG. 10 is a cross-sectional view showing a manufacturing process of the electrode and the porous membrane.
  • FIG. 11 is a cross-sectional view showing an electrode unit according to a third modification.
  • FIG. 12 is a cross-sectional view of an electrolysis apparatus according to a third embodiment.
  • FIG. 13 is a cross-sectional view showing an electrolysis apparatus according to a fourth embodiment.
  • FIG. 14 is a cross-sectional view showing an electrode unit according to a fourth modification.
  • each drawing is a schematic diagram for promoting the embodiment and its understanding, and its shape, dimensions, ratio, etc. are different from the actual device, but these are considered in consideration of the following description and known techniques.
  • the design can be changed as appropriate.
  • the electrodes are drawn on a plane, but may be curved in accordance with the shape of the electrode unit or may be cylindrical.
  • FIG. 1 is a diagram schematically showing an electrolysis apparatus according to the first embodiment.
  • the electrolysis apparatus 10 includes, for example, a two-chamber type electrolytic cell 11 having an electrode unit 12.
  • the electrolytic cell 11 is formed in a flat rectangular box shape, and the inside thereof is partitioned into two chambers, an anode chamber 16 and a cathode chamber 18, by a partition wall 14 and an electrode unit 12.
  • the electrode unit 12 is provided between a first electrode (anode) 20 positioned in the anode chamber 16, a second electrode (counter electrode, cathode) 22 positioned in the cathode chamber 18, and the first and second electrodes.
  • a porous membrane 24 is provided between a first electrode (anode) 20 positioned in the anode chamber 16, a second electrode (counter electrode, cathode) 22 positioned in the cathode chamber 18, and the first and second electrodes.
  • a porous membrane 24 is provided between a first electrode (anode) 20 positioned in the anode chamber 16 positioned in the anode chamber 16, a second electrode (counter electrode, cathode) 22 positioned in the cathode chamber 18, and the first and second electrodes.
  • the electrolysis apparatus 10 includes a power supply 30 that applies a voltage to the first and second electrodes 20 and 22 of the electrode unit 12, an ammeter 32, a voltmeter 34, and a control device 36 that controls them.
  • a liquid channel may be provided in the anode chamber 16 and the cathode chamber 18. You may connect the anode chamber 16 and the cathode chamber 18 with piping, a pump, etc. for supplying and discharging a liquid from the outside.
  • a porous spacer may be provided between the electrode unit 12 and the anode chamber 16 or the cathode chamber 18.
  • FIG. 2 is an exploded perspective view of the electrode unit.
  • the first electrode 20 has a porous structure in which a large number of through holes 13 are formed in a base material 21 made of, for example, a rectangular metal plate.
  • the plate-like base material 21 has a first surface 21a and a second surface 21b facing the first surface 21a substantially in parallel. The distance between the first surface 21a and the second surface 21b, that is, the plate thickness is formed at T1.
  • the first surface 21 a faces the porous film 24, and the second surface 21 b faces the anode chamber 16.
  • a large number of through-holes 13 are formed over the entire surface of the first electrode 20.
  • Each through hole 13 opens to the first surface 21a and the second surface 21b.
  • the through hole 13 is formed of a tapered wall surface or a curved wall surface so that the opening diameter on the first surface 21a side is larger than the opening diameter on the second surface 21b side.
  • the through-hole 13 can use various shapes such as a square, a rectangle, a rhombus, a circle, and an ellipse. The vertices of squares, rectangles and rhombuses may be rounded.
  • the through holes 13 are not limited to regular shapes, and may be formed side by side at random.
  • a valve metal such as titanium, chromium, aluminum or an alloy thereof, or a conductive metal can be used. Of these, titanium is preferred.
  • an electrolytic catalyst (catalyst layer) on the first surface 21 a and the second surface 21 b of the first electrode 20.
  • the catalyst is preferably a noble metal catalyst such as platinum or an oxide catalyst such as iridium oxide. You may form so that the quantity per unit area of an electrocatalyst may differ on both surfaces of a 1st electrode. Thereby, a side reaction etc. can be suppressed.
  • the surface roughness of the substrate 21 is preferably 0.01 to 3 ⁇ m.
  • the surface roughness of the substrate 21 is more preferably 0.02 ⁇ m to 2 ⁇ m, and further preferably 0.03 ⁇ m to 1 ⁇ m.
  • the second electrode (counter electrode) 22 is configured in the same manner as the first electrode 20. That is, the 2nd electrode 22 has the porous structure which formed many through-holes 15 in the base material 23 which consists of a rectangular metal plate, for example.
  • the base material 23 has a first surface 23a and a second surface 23b that faces the first surface 23a substantially in parallel.
  • the first surface 23 a faces the porous film 24, and the second surface 23 b faces the cathode chamber 18.
  • the continuous porous film 24 is formed on the first surface 21 a of the first electrode 20 and covers the entire first surface 21 a and the through hole 13.
  • the porous film 24 is formed, for example, in a rectangular shape having substantially the same dimensions as the first electrode 20, and between the first surface 21 a of the first electrode 20 and the first surface 23 a of the second electrode 22. Is sandwiched between.
  • the second electrode 22 may not be in direct contact with the porous film 24, or another structure may be provided between the second electrode 22 and the porous film 24. .
  • a uniform inorganic oxide porous film containing a chemically stable inorganic oxide is used.
  • Various inorganic oxides can be used.
  • titanium oxide, silicon oxide, aluminum oxide, niobium oxide, tantalum oxide, nickel oxide, tungsten oxide, zircon, and zeolite can be used, and among these, titanium oxide, silicon oxide, and aluminum oxide are preferable.
  • Inorganic oxides may contain hydroxides, alkoxides, oxyhalides, and hydrates. When an inorganic oxide is produced through hydrolysis of a metal halide or metal alkoxide, it tends to be a mixture of these depending on the post-treatment temperature.
  • the inorganic oxide of the porous film 24 is preferable because titanium oxide, aluminum oxide, and zircon that tend to have a positive zeta potential in the acidic region exhibit an anion exchange function.
  • the inorganic oxide of the porous membrane 24 is cation exchange of titanium oxide, aluminum oxide, silicon oxide, tungsten oxide, zircon, and zeolite, in which the zeta potential tends to be negative in the alkaline region. It is preferable because of its function.
  • the inorganic oxide porous film 24 is formed in a non-planar and three-dimensional form as schematically shown in FIG. 3D by forming a film by applying nanoparticles or by forming it with a sol-gel. Can have regular holes. In this case, the porous film 24 is resistant to bending and the like.
  • the porous film 24 may contain a polymer in addition to the inorganic oxide.
  • the polymer gives the membrane flexibility.
  • a chemically stable main chain substituted with a halogen atom is preferable, and polyvinylidene chloride, polyvinylidene fluoride, Teflon (registered trademark) and the like are preferable. Of these, Teflon is particularly preferred.
  • so-called engineering plastics such as polyimide and polyphenylene sulfide can be used as the polymer.
  • the pore diameter of the porous membrane 24 may be different from the opening diameter on the first electrode 20 side and the opening diameter on the second electrode 22 side.
  • the opening diameter of the hole on the second electrode 22 side By making the opening diameter of the hole on the second electrode 22 side larger than the opening diameter on the first electrode 20 side, it becomes easier to move ions and reduce stress concentration due to the through hole 13 of the first electrode 20. Can do. This is because ion movement by diffusion becomes easier when the opening diameter on the second electrode 22 side is larger.
  • the first electrode 20 is used as an anode, it has a positive potential, so that anions are easily attracted to the first electrode 20 even if the opening diameter on the first electrode 20 side is small.
  • the pore diameter on the first electrode 20 side is large, the generated chlorine, hypochlorous acid, or the like is likely to diffuse to the porous membrane 24 side.
  • the pore diameter on the surface of the porous membrane 24 can be measured by using a high-resolution scanning electron microscope (SEM). Further, the pores in the porous membrane can be measured by cross-sectional SEM observation.
  • SEM scanning electron microscope
  • the porous film 24 includes a first region 24 a that covers the first surface 21 a portion of the first electrode 20, and a second region 24 b that covers the opening of the through hole 13. ing.
  • the generated gas such as chlorine is difficult to be discharged from the first surface 21a portion of the first electrode 20. Therefore, the electrode unit 12 tends to deteriorate. Therefore, as described above, in the porous film 24, the surface holes in the first region 24a are eliminated, that is, the first region 24a is formed to be non-porous, or the diameter of the surface hole in the first region 24a is changed to the hole in the second region 24b.
  • the electrolytic reaction in the region in contact with the first region 24a can be suppressed, and deterioration of the electrode unit 12 can be prevented.
  • a thin non-porous film 29a or a small pore diameter is formed on the first surface 21a of the first electrode 20 by screen printing or the like.
  • the material film 29b may be formed.
  • the reaction area of the first electrode 20 decreases, it is necessary to cause a sufficient reaction to occur in the electrode region where gas tends to escape. Also.
  • By covering the surface of the first electrode 20 opposite to the porous film 24 (second surface 21b) with an electrically insulating film side reactions can be reduced.
  • the porous film 24 may be a laminated film of a plurality of porous films 28a and 28b having different pore diameters.
  • the pore diameter of the porous membrane 28b located on the second electrode 22 side larger than the pore diameter of the porous membrane 28a located on the first electrode 20 side, the movement of ions is further facilitated and the electrode The stress concentration due to the through holes can be reduced.
  • the first electrode 20 and the porous film 24, and the second electrode are pressed. 22 contacts, and the electrode unit 12 is obtained.
  • the electrode unit 12 is disposed in the electrolytic cell 11 and attached to the partition wall 14.
  • the electrolytic cell 11 is partitioned into an anode chamber 16 and a cathode chamber 18 by the partition wall 14 and the electrode unit 12.
  • the electrode unit 12 is arrange
  • the first electrode 20 of the electrode unit 12 is disposed facing the anode chamber 16, and the second electrode 22 is disposed facing the cathode chamber 18.
  • both electrodes of the power supply 30 are electrically connected to the first electrode 20 and the second electrode 22.
  • the power supply 30 applies a voltage to the first and second electrodes 20 and 22 under the control of the control device 36.
  • the voltmeter 34 is electrically connected to the first electrode 20 and the second electrode 22 and detects a voltage applied to the electrode unit 12.
  • the detection information is supplied to the control device 36.
  • the ammeter 32 is connected to the voltage application circuit of the electrode unit 12 and detects the current flowing through the electrode unit 12.
  • the detection information is supplied to the control device 36.
  • the control device 36 controls voltage application or load on the electrode unit 12 by the power supply 30 according to the detection information in accordance with a program stored in the memory.
  • the electrolyzer 10 applies an electric voltage or loads between the first electrode 20 and the second electrode 22 in a state in which the reaction target substance is supplied to the anode chamber 16 and the cathode chamber 18, and performs electrochemistry for electrolysis. Allow the reaction to proceed.
  • the electrolyzer 10 of this embodiment preferably electrolyzes an electrolyte containing chloride ions.
  • the electrolytic apparatus and the electrode unit configured as described above, by providing the porous film 24 containing a chemically stable inorganic oxide so as to cover the first surface and the through hole of the first electrode 20.
  • the distance between the first electrode 20 and the second electrode 22 can be kept as constant as possible and the liquid flow can be made uniform.
  • the electrolytic reaction can occur uniformly at the electrode interface. Since the electrolytic reaction occurs uniformly, catalyst deterioration and electrode metal deterioration occur uniformly, and combined with the use of a chemically stable inorganic oxide, the life of the electrode unit can be made very long.
  • the contact angle between the opening of the through hole and the porous film 24 becomes an obtuse angle by forming the through hole with a tapered surface or a curved surface where the opening on the first surface side becomes wide, Stress concentration on the porous film 24 can be reduced. From the above, it is possible to obtain a long-life electrode unit that can maintain electrolytic performance over a long period of time and an electrolysis apparatus including the electrode unit.
  • the second electrode 22 has a porous structure having a large number of through holes.
  • the present invention is not limited to this, and may be a flat electrode having no through holes.
  • FIG. 4 shows an electrode unit according to a first modification.
  • the electrode unit 12 may include a diaphragm 26 that transmits at least one of ions and liquid.
  • the diaphragm 26 is formed in a rectangular shape having substantially the same dimensions as the first electrode 20, and is sandwiched between the porous film 24 and the first surface 23 a of the second electrode 22.
  • the diaphragm 26 is in close contact with the porous film 24, and is in close contact with the entire surface of the first surface 23 a of the second electrode 22.
  • electrolyte membranes and porous membranes having nanopores can be used.
  • a polymer electrolyte membrane for example, a cation exchange solid polymer electrolyte membrane, specifically, a cation exchange membrane, an anion exchange membrane, or a hydrocarbon membrane can be used.
  • the cation exchange membrane include NAFION (EI DuPont: Trademark) 112, 115, 117, Flemion (Asahi Glass Co., Ltd .: Trademark), ACIPLEX (Asahi Kasei Corporation: Trademark), Gore Select (W.L. Gore and). Associates Inc .: trademark).
  • anion-exchange membrane examples include A201 manufactured by Tokuyama Corporation.
  • porous membranes having nanopores include porous ceramics such as porous glass, high-quality alumina, porous titania, and porous zeolite, porous polymers such as porous polyethylene, porous propylene, and porous Teflon. .
  • porous ceramics such as porous glass, high-quality alumina, porous titania, and porous zeolite
  • porous polymers such as porous polyethylene, porous propylene, and porous Teflon.
  • FIG. 5 shows a part of the electrode unit according to the second modification.
  • the porous membrane 24 of the electrode unit 12 is also applied to the wall surface (side wall surface of the through hole) defining the through hole 15 of the first electrode 20. May be present. That is, the porous film 24 may be formed so as to cover part or all of the first surface 21 a of the first electrode 20 and the wall surface of the at least one through hole 15.
  • the joining of the 1st electrode 20 and the porous film 24 is strengthened, and even if there exists a thermal cycle etc., the porous film 24 becomes difficult to peel off.
  • FIG. 6 is a cross-sectional view schematically showing an electrolysis apparatus according to the second embodiment
  • FIG. 7 is an exploded perspective view of the electrode unit
  • FIG. 8 is a cross-sectional view of the electrode unit.
  • the first electrode 20 of the electrode unit 12 has a porous structure, and the through-holes have different opening diameters on the first surface 21a side and the second surface 21b side.
  • the first electrode 20 has a porous structure in which a large number of through holes are formed in a base material 21 made of, for example, a rectangular metal plate.
  • the substrate 21 has a first surface 21a and a second surface 21b that faces the first surface 21a substantially in parallel.
  • the distance between the first surface 21a and the second surface 21b, that is, the plate thickness is formed at T1.
  • the first surface 21 a faces the porous film 24, and the second surface 21 b faces the anode chamber 16.
  • a plurality of first holes 40 are formed in the first surface 21a of the base material 21 and open to the first surface 21a.
  • a plurality of second holes 42 are formed in the second surface 21b and open to the second surface 21b.
  • Each first hole 40 communicates with the opposing second hole 42 and forms a through-hole penetrating the base material 21.
  • the opening diameter R1 of the first hole 40 on the porous membrane 24 side is smaller than the opening diameter R2 of the second hole 42, and the number of holes is such that the first hole 40 is the second hole 42. More are formed. That is, the opening area of the second hole 42 is larger than the opening area of the first hole 40.
  • the second hole portion 42 is formed in, for example, a rectangular shape, and is provided side by side in a matrix on the second surface 21b.
  • the peripheral wall defining each second hole portion 42 is formed by a tapered surface 42a or a curved surface whose diameter increases from the bottom of the hole portion toward the opening, that is, toward the second surface side. Also good.
  • the interval between the adjacent second hole portions 42, that is, the width of the linear portion of the electrode is set to W2.
  • the second hole portion 42 is not limited to a rectangular shape, and may have other various shapes. Further, the second hole portions 42 are not limited to regular, and may be formed side by side at random.
  • the first hole 40 is, for example, formed in a rectangular shape, and is provided in a matrix on the first surface 21a.
  • the peripheral wall defining each first hole portion 40 may be formed by a tapered surface or a curved surface whose diameter increases from the bottom of the hole portion toward the opening, that is, toward the first surface 21a. Good.
  • a plurality of, for example, nine first hole portions 40 are provided so as to face one second hole portion 42. Each of these nine first hole portions 40 communicates with the second hole portion 42 to form a through hole that penetrates the base material 21 together with the second hole portion 42.
  • the interval W1 between the adjacent first hole portions 40 is set to be smaller than the interval W2 between the second hole portions 42.
  • the number density of the 1st hole 40 in the 1st surface 21a is sufficiently larger than the number density of the 2nd hole 42 in the 2nd surface 21b.
  • the base material 21, the catalyst layer, and the like of the first electrode 20 are formed in the same manner as in the first embodiment described above.
  • a smaller opening diameter of the first hole portion 40 is preferable in order to make the pressure uniform, but a certain size is necessary to inhibit the material diffusion.
  • the thickness is preferably 1 to 2 mm, more preferably 0.3 to 1 mm.
  • the opening various shapes such as a square, a rectangle, a rhombus, a circle, an ellipse and the like can be used, but the opening area is preferably 0.01 to 4 mm 2 which is the same as the opening area of the square.
  • the opening area is more preferably 0.1 mm 2 to 1.5 mm 2 . More preferably, it is 0.2 mm 2 to 1 mm 2 .
  • the ratio (opening ratio) of the opening area to the electrode area including the opening is preferably 0.05 to 0.5, more preferably 0.1 to 0.4, and further preferably 0.15 to 0.3. If the aperture ratio is too small, it will be difficult to outgas. If the aperture ratio is too large, the electrode reaction is hindered.
  • the 1st hole part 40 is good also as another shape, without being limited to a rectangular shape.
  • the 1st hole part 40 may be formed not only regularly but in a line.
  • not only the structure which all the 1st hole parts 40 are connected to the 2nd hole part 42 but the 1st hole part which is not connected to the 2nd hole part 42 may be included. That is, there may be a first hole 40 that is not in communication with the anode chamber 16.
  • the first hole 40 may be a rectangle that extends from the vicinity of one end of the electrode to the vicinity of the other end, and a plurality of opening portions that communicate with the second hole 42 may be disposed at intervals.
  • the first hole portion not communicating with the second hole portion has an effect of increasing the electrode area.
  • the first hole portion having an opening area of 0.01 mm 2 to 4 mm 2 is preferably 85% or more of all the first hole portions, more preferably 90% or more, Preferably it is 95% or more.
  • Various shapes such as a square, a rectangle, a rhombus, a circle, and an ellipse can be used for the opening of the second hole portion 42.
  • a larger opening diameter of the second hole portion 42 is preferable in order to improve gas escape, but it cannot be so large because electric resistance increases.
  • one side is preferably 1 to 40 mm, more preferably 2 to 20 mm.
  • the opening square, rectangular, rhombic, circular may be used an elliptical or the like and the various shapes, as the opening area equal to the opening area of the square, preferably those from 1 mm 2 of 1600 mm 2.
  • the opening area of the second hole portion 42 is more preferably 4 mm 2 to 900 mm 2 , and further preferably 9 mm 2 to 400 mm 2 .
  • An opening that extends in one direction and connects from one end of the electrode to the other is also possible, such as a rectangle or an ellipse.
  • the porous film 24 containing an inorganic oxide is formed on the first surface 21 a of the first electrode 20 and covers the entire surface of the first surface 21 a and the first hole 40.
  • the porous film 24 is the same porous film as that of the first embodiment described above.
  • the second electrode (counter electrode) 22 is configured in the same manner as the first electrode 20. That is, the second electrode 22 has a porous structure in which a large number of through holes are formed in the base material 23 made of, for example, a rectangular metal plate.
  • the base material 23 has a first surface 23a and a second surface 23b that faces the first surface 23a substantially in parallel.
  • the first surface 23 a faces the diaphragm 26, and the second surface 23 b faces the cathode chamber 18.
  • a plurality of first holes 44 are formed in the first surface 23a of the base material 23 and open to the first surface 23a.
  • a plurality of second holes 46 are formed in the second surface 23b and open to the second surface 23b.
  • the opening diameter of the first hole 44 on the diaphragm 26 side is smaller than the opening of the second hole 46, and the number of holes is such that the first hole 44 is formed more than the second hole 46. ing.
  • the depth of the first hole 44 is formed to be smaller than the depth of the second hole 46.
  • a plurality of, for example, nine first hole portions 44 are provided to face one second hole portion 46.
  • Each of these nine first holes 44 communicates with the second hole 46 to form a through hole that penetrates the base material 23 together with the second hole 46.
  • the interval between the adjacent first hole portions 44 is set to be smaller than the interval between the second hole portions 46.
  • the electrolyzer 10 of the present embodiment preferably electrolyzes an electrolyte containing chlorine ions.
  • the first electrode 20 can be produced by, for example, an etching method using a mask.
  • a single flat substrate 21 is prepared, and resist films 50a and 50b are applied to the first surface 21a and the second surface 21b of the substrate 21, respectively.
  • the resist films 50a and 50b are exposed using an optical mask (not shown) to produce etching masks 52a and 52b, respectively.
  • FIG. 9A an optical mask (not shown) to produce etching masks 52a and 52b, respectively.
  • the first surface portion 21a and the second surface 21b of the base material 21 are wet-etched with a solution through the masks 52a and 52b, so that the plurality of first hole portions 40 and the plurality of first hole portions 40 The second hole 42 is formed. Thereafter, the first electrode 20 is obtained by removing the masks 52a and 52b.
  • the taper of the first and second holes 40 and 42 and the shape of the curved surface can be controlled by the material of the base material 21 and the etching conditions.
  • the depth of the first hole 40 is T2, and the depth of the second hole 42 is T3.
  • the first and second holes are formed so that T2 ⁇ T3.
  • both surfaces of the base material 21 may be etched simultaneously, or one surface may be etched.
  • the type of etching is not limited to wet etching, and dry etching or the like may be used.
  • the first electrode 20 can be manufactured not only by etching but also by an expanding method, a punching method, or processing by laser or precision cutting.
  • the porous film 24 is formed on the first surface 21 a of the first electrode 20.
  • a solution containing inorganic oxide particles and / or an inorganic oxide precursor is applied to the first surface 21a to produce a pretreatment film 24c.
  • the pretreatment film 24c is sintered to produce a porous film 24 having porosity.
  • a method for preparing a solution containing an inorganic oxide precursor for example, when a metal alkoxide is dissolved in alcohol and a high-boiling solvent such as glycerin is added or sintered in order to prepare a porous structure.
  • a solution is prepared by mixing an organic substance such as a fatty acid that easily oxidizes into carbon dioxide.
  • a dispersion containing inorganic oxide particles may be applied. These may be combined.
  • the sintering temperature is preferably about 150 to 600 ° C.
  • the first hole 40 and the second hole 42 of the first electrode 20 are previously made of organic matter.
  • a pretreatment film 24 c may be formed on the first surface 21 a of the first electrode 20.
  • the pretreatment film 24 c is baked to form the porous film 24. Or you may bake, leaving the organic substance 55 left.
  • the diameter of the first hole 40 formed in the first surface 21 a on the porous membrane 24 side is made smaller than the diameter of the second hole 42, By increasing the number density of the portions, stress concentration acting on the porous film 24 from the first electrode 20 side can be reduced.
  • the porous membrane 24 By making the porous membrane 24 into a continuous membrane and contacting the entire first surface 21a of the first electrode 20, the pores of the first electrode 20 are covered with the porous membrane 24, and the first electrode 20 and the diaphragm 26 are covered. Can be easily maintained over the entire surface. That is, it is possible to prevent a distribution from occurring in the film thickness of the porous film 24 and to maintain the film thickness of the porous film 24 uniform. Thereby, it is possible to uniformly generate the electrolytic reaction uniformly, and to improve the reaction efficiency of the electrolytic device and prevent the electrolyte membrane from being deteriorated.
  • FIG. 11 shows an electrode unit according to a third modification.
  • the electrode unit 12 may include a diaphragm 26 that transmits at least one of ions and liquid.
  • the diaphragm 26 is formed in a rectangular shape having substantially the same dimensions as the first electrode 20, and is sandwiched between the porous film 24 and the first surface 23 a of the second electrode 22.
  • the diaphragm 26 is in close contact with the porous film 24, and is in close contact with the entire surface of the first surface 23 a of the second electrode 22.
  • a diaphragm similar to the diaphragm shown in the first modification can be used.
  • FIG. 12 is a cross-sectional view showing an electrolysis apparatus according to the third embodiment.
  • the electrolytic cell 11 of the electrolysis apparatus 10 is configured as a one-chamber electrolytic cell having a single electrolytic chamber 17.
  • the electrode unit 12 is disposed in the electrolysis chamber 17.
  • the electrolysis chamber 17 may be connected with piping, a pump, and the like for supplying and discharging the electrolyte from the outside.
  • the second electrode (counter electrode) 22 of the electrode unit 12 is preferably formed in a porous structure like the first electrode 20.
  • the electrode area can be increased.
  • FIG. 13 is a cross-sectional view showing an electrolysis apparatus according to the fourth embodiment.
  • the electrolysis apparatus 10 includes a three-chamber type electrolytic cell 11 and an electrode unit 12.
  • the electrolytic cell 11 is formed in a flat rectangular box shape, and the inside thereof is partitioned into three chambers by a partition wall 14 and an electrode unit 12, an anode chamber 16, a cathode chamber 18, and an intermediate chamber 19 formed between the electrodes. It has been.
  • the electrode unit 12 includes a first electrode (anode) 20 located in the anode chamber 16, a second electrode (counter electrode, cathode) 22 located in the cathode chamber 18, and a first surface 21 a of the first electrode 20.
  • the formed porous film 24 and the porous film 27 formed on the first surface 23 a of the second electrode 22 are included.
  • the first electrode 20 and the second electrode 22 face each other in parallel with a gap therebetween, and form an intermediate chamber (electrolyte chamber) 19 for holding an electrolyte solution between the porous films 24 and 24b. .
  • a holding body 25 that holds the electrolytic solution may be provided in the intermediate chamber 19.
  • the first electrode 20 and the second electrode 22 may be connected to each other by a plurality of bridges 60 having insulating properties.
  • the electrolysis apparatus 10 includes a power supply 30 for applying a voltage to the first and second electrodes 20 and 22 of the electrode unit 12, an ammeter 32, a voltmeter 34, and a control device 36 for controlling them.
  • a liquid channel may be provided in the anode chamber 16 and the cathode chamber 18. You may connect the anode chamber 16 and the cathode chamber 18 with piping, a pump, etc. for supplying and discharging a liquid from the outside.
  • a porous spacer may be provided between the electrode unit 12 and the anode chamber 16 or the cathode chamber 18.
  • the first electrode 20 and the second electrode 22 are configured to have the same porous structure as that of the second embodiment described above.
  • the continuous porous film 24 is formed in, for example, a rectangular shape having substantially the same dimensions as the first electrode 20, and faces the entire surface of the first surface 21a.
  • the continuous porous film 27 is formed in a rectangular shape having substantially the same dimensions as the second electrode 22 and faces the entire surface of the first surface 23a. As these porous films 24 and 27, the same porous film as in the first embodiment described above can be used, and various materials can be used.
  • porous films 24 and 27 are inorganic oxide films having pores that are irregular in a plane or three-dimensionally, it is also possible to serve as a diaphragm.
  • a laminated film of a plurality of porous films having different pore diameters may be used.
  • the same operational effects as those of the first embodiment described above can be obtained, and an electrode unit and an electrolysis apparatus having a high reaction efficiency and a long life can be obtained.
  • FIG. 14 shows an electrode unit according to a fourth modification.
  • the electrode unit 12 may include diaphragms 26a and 26b that transmit at least one of ions and liquid.
  • the diaphragm 26 a is formed in a rectangular shape having substantially the same dimensions as the first electrode 20, and faces the first surface 21 a of the first electrode 20.
  • the porous membrane 24 is sandwiched between the first surface 21a of the first electrode 20 and the diaphragm 26a, and is in close contact with the first electrode 20 and the diaphragm 26a.
  • the diaphragm 26 b is formed in a rectangular shape having substantially the same dimensions as the second electrode 22, and faces the first surface 23 a of the second electrode 22.
  • a porous membrane 27 is sandwiched between the first surface 23a of the second electrode 22 and the diaphragm 26b, and is in close contact with the second electrode 22 and the diaphragm 26b.
  • electrolyte membranes and porous membranes having nanopores can be used.
  • a polymer electrolyte membrane for example, a cation exchange solid polymer electrolyte membrane, specifically, a cation exchange membrane, an anion exchange membrane, or a hydrocarbon membrane can be used.
  • the cation exchange membrane include NAFION (EI DuPont: Trademark) 112, 115, 117, Flemion (Asahi Glass Co., Ltd .: Trademark), ACIPLEX (Asahi Kasei Corporation: Trademark), Gore Select (W.L. Gore and). Associates Inc .: trademark).
  • anion-exchange membrane examples include A201 manufactured by Tokuyama Corporation.
  • porous film having nanopores porous ceramics such as porous glass, high-quality alumina, and porous titania, porous polymers such as porous polyethylene, porous propylene, and porous Teflon can be used.
  • the electrode base material 21 uses a flat titanium plate having a thickness T1 of 0.5 mm, and the titanium plate is etched as shown in FIG. 9 to produce the electrode 20 shown in FIGS.
  • the thickness (the first hole depth) T2 of the region including the small-diameter first hole 40 is 0.15 mm
  • the thickness (second hole) of the region including the large-diameter second hole 42 is selected.
  • Part depth) T3 is 0.35 mm.
  • the first hole 40 is square, its one-side diameter R1 is 0.57 mm, the second hole 42 is square, and the square apex is rounded but the one-side diameter R2 of the square obtained by extrapolating the straight line is 2 mm. It is.
  • the width W1 of the linear portion formed between the adjacent first hole portions 40 is 0.1 mm, and the width W2 of the wide linear portion formed between the adjacent second hole portions 42 is 1.0 mm.
  • the etched electrode substrate 21 is treated at 80 ° C. for 1 hour in a 10 wt% oxalic acid aqueous solution.
  • a solution prepared by adding 1-butanol to 0.25 M (Ir) to iridium chloride (IrCl3 ⁇ nH2O) is applied to the first surface 21a of the electrode substrate 21, and then dried and fired. In this case, drying is performed at 80 ° C. for 10 minutes, and baking is performed at 450 ° C. for 10 minutes.
  • the electrode base material in which such coating, drying, and baking are repeated five times is cut into a reaction electrode area of 3 cm ⁇ 4 cm to form a first electrode (anode) 20.
  • Ethanol and diethanolamine are added to tetraisopropoxy titanium (IV) in an ice bath, and ethanol mixed water is added dropwise with stirring to prepare a sol.
  • Polyethylene glycol (molecular weight 5000) that makes the thin film porous by heat treatment and increases the viscosity of the sol is added to the sol returned to room temperature, and the first surface 21a of the electrode 20 is coated with a brush.
  • the coated film is baked at 500 ° C. for 7 minutes. After repeating coating and baking three times, baking is performed at 500 ° C. for 1 hour to obtain a porous film 24 made of titanium oxide.
  • the electrode unit 12 shown in FIG. 13 is produced using the first electrode 20 and the second electrode 22.
  • the holding body 25 for holding the electrolytic solution porous polystyrene having a thickness of 5 mm is used.
  • the first and second electrodes, the porous membrane, the partition walls, and the porous polystyrene are overlapped and fixed using a silicone sealant and screws to form an electrode unit 12.
  • the electrolysis apparatus 10 shown in FIG. 13 is produced using this electrode unit 12.
  • the anode chamber 16 and the cathode chamber 18 of the electrolytic cell 11 are each formed of a vinyl chloride container in which straight channels are formed.
  • a control device 36, a power source 30, a voltmeter 34, and an ammeter 32 are installed.
  • Pipes and pumps for supplying water to the anode chamber 16 and the cathode chamber 18 are connected to the electrolytic cell 11, and saturated saline for circulating and supplying saturated saline 25 to the holder (porous polystyrene) 25 of the electrode unit 12.
  • the tank, piping and pump are connected to the electrode unit.
  • Electrolysis is performed at a voltage of 4 V and a current of 1.5 A using the electrolyzer 10, and hypochlorous acid water is generated on the first electrode (anode) 20 side, and sodium hydroxide water is generated on the second electrode (cathode) 22 side. To do. Even after 1000 hours of continuous operation, there is almost no increase in voltage or change in product concentration, and stable electrolytic treatment can be performed.
  • Example 2 (Example 2) Implementation is performed except that A201 made by Tokuyama, which is an anion exchange membrane, is used as the diaphragm 26a, and Nafion 117 is installed between the porous membranes 24 and 27 and the holding body 25 holding the electrolyte as the diaphragm 26b.
  • the electrolytic device 10 is produced. Using this electrolyzer 10, electrolysis was performed at a voltage of 5.2 V and a current of 1.5 A. Hypochlorous acid water was used on the first electrode (anode) 20 side, and sodium hydroxide was used on the second electrode (cathode) 22 side. Produce water.
  • Example 2 compared with Example 1, it is stable even after 1000 hours of continuous operation in which the concentration of sodium chloride contained in hypochlorous acid water decreases, and almost no increase in voltage or change in product concentration is observed ( Example 3)
  • the electrolysis apparatus 10 is produced in the same manner as in Example 1 except that tetraethoxysilane is used instead of tetraisopropoxy titanium (IV). Using this electrolyzer, electrolysis is performed at a voltage of 4.3 V and a current of 1.5 A. Hypochlorous acid water is used on the first electrode (anode) 20 side, and sodium hydroxide water is used on the second electrode (cathode) 22 side. Is generated. Even after 1000 hours of continuous operation, there is almost no increase in voltage or change in product concentration, and stable electrolytic treatment can be performed.
  • Example 4 The electrolytic device 10 is produced in the same manner as in Example 1 except that triisopropoxyaluminum is used instead of tetraisopropoxytitanium (IV). Using this electrolyzer, electrolysis was performed at a voltage of 4.0 V and a current of 1.5 A, hypochlorous acid water was used on the first electrode (anode) 20 side, and sodium hydroxide water was used on the second electrode (cathode) 22 side. Is generated. Even after 1000 hours of continuous operation, there is almost no increase in voltage or change in product concentration, and stable electrolytic treatment can be performed.
  • Example 5 The electrolytic device 10 is manufactured in the same manner as in Example 1 except that tetraisopropoxyzirconium (IV) is used instead of tetraisopropoxytitanium (IV). Using this electrolyzer, electrolysis is performed at a voltage of 4.2 V and a current of 1.5 A. Hypochlorous acid water is used on the first electrode (anode) 20 side, and sodium hydroxide water is used on the second electrode (cathode) 22 side. Is generated. Even after 1000 hours of continuous operation, there is almost no increase in voltage or change in product concentration, and stable electrolytic treatment can be performed.
  • Example 6 The first electrode and the second electrode are produced in the same manner as in Example 1.
  • a porous film 24 made of titanium oxide is produced on the first electrode 20 in the same manner as in Example 1. These are overlapped with a silicone sealant and screws to form an electrode unit 12.
  • the electrolysis apparatus 10 shown in FIG. 12 is produced using this electrode unit 12.
  • a control device 36, a power source 30, a voltmeter 34, and an ammeter 32 are installed, and a pipe and a pump for supplying saline to the electrolysis chamber 17 are installed.
  • electrolysis is performed at a voltage of 3.7 V and a current of 1.5 A to produce sodium hypochlorite water. Even after 1000 hours of continuous operation, there is almost no increase in voltage or change in product concentration, and stable electrolytic treatment can be performed.
  • Example 7 The first electrode 20 and the second electrode 22 are produced in the same manner as in Example 1.
  • the second holes 42 and 46 of the electrode are spin-coated with an ethyl acetate solution of PMMA on the second surface 21b of the first electrode 20 and filled with PMMA.
  • An aqueous dispersion of titanium oxide nanoparticles having a particle diameter of 50 nm is applied on the first surface 21a of the first electrode 20 by screen printing.
  • PMMA is removed with ethyl acetate.
  • it is put in water and titanium tetrachloride is dropped. After leaving it at room temperature for 5 hours, it is washed with water and fired at 450 ° C. to obtain a porous film 24 made of titanium oxide.
  • the electrode unit 12 shown in FIG. 13 is manufactured using these first and second electrodes 20 and 22.
  • As the holding body 25 for holding the electrolytic solution porous polystyrene having a thickness of 5 mm is used.
  • the first and second electrodes, the porous membrane, the partition walls, and the porous polystyrene are overlapped and fixed using a silicone sealant and screws to form an electrode unit 12.
  • the electrolysis apparatus 10 shown in FIG. 13 is produced using this electrode unit 12.
  • the anode chamber 16 and the cathode chamber 18 of the electrolytic cell 11 are each formed of a vinyl chloride container in which straight channels are formed.
  • a control device 36, a power source 30, a voltmeter 34, and an ammeter 32 are installed.
  • Pipes and pumps for supplying tap water to the anode chamber 16 and the cathode chamber 18 are connected to the electrolytic cell 11, and saturated saline for circulating and supplying saturated saline to the holder (porous polystyrene) 25 of the electrode unit 12.
  • a water tank, piping, and pump are connected to the electrode unit.
  • Electrolysis is performed at a voltage of 4 V and a current of 1.5 A using the electrolyzer 10, and hypochlorous acid water is generated on the first electrode (anode) 20 side, and sodium hydroxide water is generated on the second electrode (cathode) 22 side. To do. Even after 1000 hours of continuous operation, there is almost no increase in voltage or change in product concentration, and stable electrolytic treatment can be performed.
  • Example 8 The first electrode and the second electrode are produced in the same manner as in Example 1.
  • An aqueous dispersion of titanium oxide nanoparticles having a particle diameter of 50 nm is dip-coated on the first surface of the first electrode on a cloth having a thickness of 200 ⁇ m made of polyvinylidene chloride fibers. After baking at 150 ° C., it is placed in water and titanium tetrachloride is added dropwise. After leaving it at room temperature for 5 hours, it is washed with water and fired at 150 ° C. to obtain a porous film 24 containing titanium oxide.
  • the electrode unit 12 shown in FIG. 14 is produced using these first electrode and second electrode.
  • A201 made by Tokuyama, which is an anion exchange membrane, is used, and Nafion 117 is used as the diaphragm 26b.
  • porous polystyrene having a thickness of 5 mm is used. These are overlapped and bonded using a silicone sealant and screws to form an electrode unit 12.
  • An electrolytic apparatus is manufactured using the electrode unit 12.
  • the anode chamber 16 and the cathode chamber 18 of the electrolytic cell 11 are each formed of a vinyl chloride container in which straight channels are formed.
  • a control device 36, a power source 30, a voltmeter 34, and an ammeter 32 are installed.
  • Pipes and pumps for supplying tap water to the anode chamber 16 and the cathode chamber 18 are connected to the electrolytic cell 11, and saturated saline for circulating and supplying saturated saline to the holder (porous polystyrene) 25 of the electrode unit 12.
  • a water tank, piping, and pump are connected to the electrode unit.
  • electrolysis was performed at a voltage of 5.5 V and a current of 1.5 A, hypochlorous acid water was used on the first electrode (anode) 20 side, and sodium hydroxide was used on the second electrode (cathode) 22 side. Produce water. Even after 1000 hours of continuous operation, there is almost no increase in voltage or change in product concentration, and stable electrolytic treatment can be performed.
  • Example 9 The first electrode and the second electrode are produced in the same manner as in Example 1. Place a hydrophilic Teflon filter in water and add titanium tetrachloride dropwise. After being left at 50 ° C. for 2 hours, washed with water and baked at 250 ° C., a porous film 24 containing titanium oxide is obtained.
  • the electrode unit 12 shown in FIG. 14 is produced using these first electrode and second electrode.
  • A201 made by Tokuyama, which is an anion exchange membrane, is used, and Nafion 117 is used as the diaphragm 26b.
  • porous polystyrene having a thickness of 5 mm is used. These are overlapped and bonded using a silicone sealant and screws to form an electrode unit 12.
  • An electrolytic apparatus is manufactured using the electrode unit 12.
  • the anode chamber 16 and the cathode chamber 18 of the electrolytic cell 11 are each formed of a vinyl chloride container in which straight channels are formed.
  • a control device 36, a power source 30, a voltmeter 34, and an ammeter 32 are installed.
  • Pipes and pumps for supplying tap water to the anode chamber 16 and the cathode chamber 18 are connected to the electrolytic cell 11, and saturated saline for circulating and supplying saturated saline to the holder (porous polystyrene) 25 of the electrode unit 12.
  • a water tank, piping, and pump are connected to the electrode unit.
  • electrolysis was performed at a voltage of 5.7 V and a current of 1.5 A, hypochlorous acid water was used on the first electrode (anode) 20 side, and sodium hydroxide was used on the second electrode (cathode) 22 side. Produce water. Even after 1000 hours of continuous operation, there is almost no increase in voltage or change in product concentration, and stable electrolytic treatment can be performed.
  • the electrode base material 21 uses a flat titanium plate having a plate thickness T1 of 0.5 mm, and the titanium plate is etched as shown in FIG. 9 to produce an electrode.
  • the thickness (the first hole depth) T2 of the region including the small-diameter first hole 40 is 0.15 mm
  • the thickness (second hole) of the region including the large-diameter second hole 42 is selected.
  • Part depth) T3 is 0.35 mm.
  • the 1st hole part 40 is made into a rhombus, and makes a long diagonal line 0.69mm and a short diagonal line 0.4mm.
  • the 2nd hole 42 is made into a rhombus, a long diagonal is 6.1 mm, and a short diagonal is 3.5 mm.
  • the width W1 of the linear portion formed between the adjacent first hole portions 40 is 0.15 mm, and the width W2 of the wide linear portion formed between the adjacent second hole portions 42 is 1 mm.
  • Other configurations are the same as in Example 1, and the electrode unit 12 and the electrolyzer 10 are produced.
  • electrolysis is performed at a voltage of 5.3 V and a current of 1.5 A to generate hypochlorous acid water on the anode 20 side and sodium hydroxide water on the cathode 22 side. Even after 1000 hours of continuous operation, there is almost no increase in voltage or change in product concentration, and stable electrolytic treatment can be performed.
  • Example 1 An electrolysis apparatus was produced in the same manner as in Example 1 except that a porous polystyrene film was used instead of the continuous inorganic porous film. Using this electrolyzer, electrolysis is performed at a voltage of 4 V and a current of 1.5 A, and hypochlorous acid water is generated on the anode side and sodium hydroxide water is generated on the cathode side. After 1000 hours of continuous operation, the voltage increased significantly and the product concentration decreased, and the long-term stability was lacking.
  • Comparative Example 2 An electrode unit and an electrolysis device were produced in the same manner as in Example 7 without coating with PMMA. In this electrode unit, the through hole is not covered with the inorganic porous film.
  • hypochlorous acid water is generated on the anode side and sodium hydroxide water is generated on the cathode side.
  • Hypochlorous acid water contains a large amount of salt.
  • the present invention is not limited to the above-described embodiments as they are, and can be embodied by modifying the constituent elements without departing from the scope of the invention in the implementation stage.
  • various inventions can be formed by appropriately combining a plurality of components disclosed in the embodiment. For example, some components may be deleted from all the components shown in the embodiment.
  • constituent elements over different embodiments may be appropriately combined.
  • the first electrode and the second electrode are not limited to a rectangular shape, and other various shapes can be selected.
  • the first hole and the second hole of the first electrode are not limited to a rectangular shape, and may have various other shapes such as a circle and an ellipse.
  • the material of each constituent member is not limited to the above-described embodiments and examples, and other materials can be appropriately selected.
  • the electrolytic cell of the electrode device is not limited to a 1 to 3 chamber type electrolytic cell, and can be applied to all electrolytic cells using electrodes. Electrolytes and products are not limited to salts and hypochlorous acid, and may be applied to various electrolytes and products.

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  • Water Treatment By Electricity Or Magnetism (AREA)

Abstract

L'invention concerne une unité d'électrode (12) d'un dispositif d'électrolyse munie : d'une première électrode (20), comprenant une première surface (21a), une seconde surface (21b) positionnée à l'opposé de la première surface, et de multiples trous traversants (13) chacun s'ouvrant vers la première surface et la seconde surface ; d'une seconde électrode (22) disposée à l'opposé de la première surface de la première électrode ; et d'un film poreux (24) formé sur la première surface de la première électrode, recouvrant la première surface et les trous traversants, et contenant un oxyde minéral.
PCT/JP2015/056388 2014-09-19 2015-03-04 Unité d'électrode, bain électrolytique muni de l'unité d'électrode, dispositif d'électrolyse, et procédé de fabrication d'électrode de l'unité d'électrode WO2016042801A1 (fr)

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JP2016505346A JP6441308B2 (ja) 2014-09-19 2015-03-04 電極ユニット、電極ユニットを備える電解槽、電解装置、電極ユニットの電極の製造方法
CN201580043891.1A CN106661743B (zh) 2014-09-19 2015-03-04 电极单元、具备电极单元的电解槽、电解装置、电极单元的电极的制造方法
US15/065,170 US20160186335A1 (en) 2014-09-19 2016-03-09 Electrode unit, electrolytic cell comprising electrode unit, electrolytic device and method of manufacturing electrode of electrode unit

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JP2014-191992 2014-09-19
JP2014191992 2014-09-19

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US15/065,170 Continuation US20160186335A1 (en) 2014-09-19 2016-03-09 Electrode unit, electrolytic cell comprising electrode unit, electrolytic device and method of manufacturing electrode of electrode unit

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WO2017158832A1 (fr) * 2016-03-18 2017-09-21 株式会社 東芝 Électrode pour électrolyse, unité électrode et dispositif de production d'eau électrolytique
JP2023065251A (ja) * 2021-10-27 2023-05-12 株式会社イープラン 水素発生装置
WO2023119730A1 (fr) * 2021-12-24 2023-06-29 住友電気工業株式会社 Électrode et dispositif d'électrolyse de l'eau

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DE102018116508A1 (de) * 2018-07-09 2020-01-09 Friedrich-Alexander-Universität Erlangen-Nürnberg Katalysatorsystem, Elektrode, sowie Brennstoffzelle oder Elektrolyseur
CN111018061B (zh) * 2019-12-30 2021-08-24 江苏大学 一种在含锂的水溶液中提取锂的电解池用离子筛阴极及其制造方法
WO2022215903A1 (fr) * 2021-04-06 2022-10-13 원동학 Dispositif de génération d'eau électrolysée
KR102365667B1 (ko) * 2021-04-06 2022-02-23 원동학 전기 분해 모듈을 포함하는 전해수 제조 장치
CN113044933A (zh) * 2021-04-07 2021-06-29 湖南满缘红水科技有限公司 低盐eow电解槽、低盐eow电解装置及低盐eow制备方法

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CN106661743B (zh) 2019-12-10

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