JP2015168581A - Oxygen reduction device, and refrigerator - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide an oxygen reduction device and a refrigerator which are produced inexpensively by a polymer electrolyte membrane method.SOLUTION: An oxygen reduction device 106 comprises: a polymer electrolyte membrane 116; an anode catalytic layer 112 for carrying a catalyst for reducing water electrolytic voltage, and performing electrolysis of water supplied from a water supply part 130 for generating hydrogen ion; a cathode catalytic layer 114 for generating water from the hydrogen ion generated by the anode catalytic layer 112 and oxygen; an anode electrode 118 for turning on electricity to the anode catalytic layer 112; and a cathode electrode 120 for turning on electricity to the cathode catalytic layer 114. The anode electrode 118, anode catalytic layer 112, polymer electrolyte membrane 116, cathode catalytic layer 114, and the cathode electrode 120 are sequentially laminated. A carrying amount of the catalyst carried by the anode catalytic layer 112 is larger than that carried by the anode electrode 118.

Description

  Embodiments described herein relate generally to an oxygen reduction device and a refrigerator.

  As a deterioration factor of stored products such as food stored in the refrigerator, there is oxidation due to oxygen present in the air. Then, the refrigerator which can suppress the oxidation of stored goods and maintain the freshness of stored goods by reducing the oxygen of the space which stores a foodstuff is known.

  As a method for reducing oxygen, a vacuum method in which the inside of the storage container is decompressed, an oxygen adsorption method in which oxygen in the storage container is adsorbed by an oxygen adsorbent, and a high pressure in which oxygen in the storage container is reduced using a polymer electrolyte membrane. Various methods such as a molecular electrolyte membrane method are known.

  The vacuum method is a method of depressurizing as a method of reducing oxygen in order to prevent oxidation of food. Since the performance correlates with the degree of vacuum, the strength of the storage container and the capacity of the vacuum pump are required, which makes the apparatus relatively large.

  The method using an oxygen adsorbent is also widely used in the distribution process of confectionery and the like as in the gas replacement method. However, if the adsorbent breaks through adsorption, the effect is lost and the life is short.

  In the polymer electrolyte membrane method, hydrogen is electrolyzed at the anode to form hydrogen ions, which move through the polymer electrolyte membrane and reach the cathode, and react with oxygen in the storage container to produce water. By consuming oxygen. Therefore, there is a merit that the pressure change is small and the strength of the storage container is not necessary (see, for example, Patent Documents 1 to 3).

  However, in the polymer electrolyte membrane method, a catalyst for lowering the electrolysis voltage of water is supported on the anode electrode or an anode catalyst layer provided between the anode electrode and the polymer electrolyte membrane. There is a problem that costs are increased.

JP 2010-210171 A JP 2010-243072 A Japanese Patent No. 3056578

  Then, embodiment of this invention aims at providing the oxygen reduction apparatus and refrigerator by the polymer electrolyte membrane method which can be manufactured cheaply.

  The oxygen reduction device of the present embodiment includes a polymer electrolyte membrane, an anode catalyst layer that carries a catalyst for reducing the electrolysis voltage of water and electrolyzes water supplied from a water supply unit to generate hydrogen ions, and the anode A cathode catalyst layer for generating water from hydrogen ions and oxygen generated in the catalyst layer, an anode electrode for energizing the anode catalyst layer, and a cathode electrode for energizing the cathode catalyst layer, the anode electrode, In the oxygen reduction device in which the anode catalyst layer, the polymer electrolyte membrane, the cathode catalyst layer, and the cathode electrode are sequentially stacked, the amount of the catalyst supported by the anode catalyst layer is the catalyst supported by the anode electrode. It is more than the amount of supported.

It is sectional drawing of the refrigerator which concerns on one Embodiment. It is the front view which abbreviate | omitted the door and storage container of the refrigerator shown in FIG. It is sectional drawing of an oxygen reduction apparatus.

  Hereinafter, an embodiment of the present invention will be described with reference to the drawings. This embodiment demonstrates the refrigerator 10 provided with the oxygen reduction apparatus 106 which reduces the oxygen in a storage container.

  As shown in FIG. 1, the refrigerator 10 according to the present embodiment includes a cabinet 11 that opens to the front surface in which a heat insulating material is disposed between an outer box that forms an outer shell and an inner box that forms a storage space. The space is partitioned into an upper refrigerated space 20 and a lower refrigerated space 40 by a heat insulating partition wall 12.

  The refrigerated space 20 is a space that is cooled to a refrigerated temperature (for example, 2 to 3 ° C.), and the interior is further partitioned vertically by a partition plate 21, and a refrigerated chamber in which a plurality of mounting shelves are provided in the upper space. 22 is provided, and a vegetable compartment 24 in which a drawer-type storage container 25 is arranged is provided in the lower space.

  A freezing space 40 disposed below the vegetable room 24 is a space cooled to a freezing temperature (for example, −18 ° C. or lower), and an ice making room 42 having a relatively small volume automatic ice making machine and a small freezer room. 44 are provided on the left and right sides, and a freezer compartment 46 is provided below them.

  The opening of the refrigerator compartment 22 is closed by a refrigerator compartment door 22a pivotally supported by hinges provided on the upper and lower sides of one side of the cabinet 11.

  Openings of the vegetable compartment 24, the ice making compartment 42, the small freezer compartment 44 and the freezer compartment 46 are closed by pull-out doors 24a, 42a and 46a. The pair of left and right support frames fixed to the back side of each pull-out door 24a, 42a, 46a holds the storage containers 25, 43, 47, and is configured to be pulled out of the cabinet as the door opens. Yes.

  A machine room 30 is provided at the bottom of the back surface of the cabinet 11, and a compressor 51 and the like constituting the refrigeration cycle are placed thereon.

  An evaporator chamber 26 is defined between the evaporator cover 14 and the rear surface of the cabinet 11 on the rear surface of the refrigerated space 20, and a refrigerator evaporator 52 and a refrigerator fan 53 are arranged in the evaporator chamber 26. It is installed. The refrigeration evaporator 52 exchanges heat with the air in the evaporator chamber 26 to cool the refrigeration evaporator 52, and the cold air generated in the refrigeration evaporator 52 by the rotational drive of the refrigeration fan 53 is supplied from the blowout port to the refrigeration chamber 22 and vegetables. By introducing into the chamber 24, the refrigerated space 20 is cooled to a predetermined temperature. The cold air that has finished cooling the refrigerated space 20 is returned to the evaporator chamber 26 through the suction port, and is cooled by exchanging heat with the refrigerated evaporator 52.

  Further, as shown in FIG. 2, a drain pan 27 that is inclined so as to become lower toward the one side in the width direction is provided in the evaporator chamber 26, below the refrigeration evaporator 52. The drain pan 27 receives dew condensation water (defrost water) generated from the refrigeration evaporator 52 during the defrosting operation, flows to the one side in the width direction, and passes through the drain passage 29 connected to one end of the machine room 30. It supplies to the evaporating dish 32 provided in the inside (refer FIG. 1).

  An evaporator chamber 34 is defined between the evaporator cover 33 and the rear surface of the cabinet 11 on the rear surface of the refrigeration space 40, and a refrigeration evaporator 54 and a blower fan 55 are arranged in the evaporator chamber 34. It is installed. The refrigeration evaporator 54 is cooled by exchanging heat with the air in the evaporator chamber 34, and the cold air generated by the refrigeration evaporator 54 by the rotational drive of the blower fan 55 is supplied to the ice making chamber 42 and the small freezer chamber 44 from the blowout port. And, the freezing space 40 is cooled to a predetermined temperature by being introduced into the freezer compartment 46. The cold air that has finished cooling the refrigeration space 40 is returned to the evaporator chamber 34 from the suction port and is cooled by exchanging heat with the refrigeration evaporator 54.

  The refrigeration evaporator 52 and the refrigeration evaporator 54 constitute a refrigeration cycle together with a compressor 51, a condenser (not shown) and a switching valve (not shown) provided in the machine room 30, and are discharged from the compressor 51. It is cooled by the refrigerant.

  In the refrigerator 10 having such a configuration, the oxygen reduction chamber 100 including the container storage portion 102 and the storage container 104 and the oxygen in the oxygen reduction chamber 100 are provided at the rear portion of the partition plate 21 constituting the ceiling portion of the vegetable compartment 24. And an oxygen reduction device 106 for reducing the above.

  Specifically, the container storage portion 102 has a box shape having an opening on the front surface, and is fixed in a suspended state on the lower surface of the partition plate 21. A storage container 104 is housed inside the container housing part 102 so that it can be pulled out from the front opening.

  The storage container 104 is a container body in which a storage unit for food or the like is stored from the upper opening. The front surface of the storage container 104 forms a lid 105 that closes the front opening of the container storage portion 102, and the periphery of the front opening via a gasket while the storage container 104 is stored in the container storage portion 102. The container storage portion 102 is closed in an airtight state.

  As shown in FIG. 3, an air vent 110 that opens to the rear is formed in the back surface of the container housing portion 102, and the oxygen storage device 106 provided on the back surface of the vegetable compartment 24 via the air vent 110 and the container housing. The part 102 is connected.

  As shown in FIG. 3, the oxygen reduction device 106 includes an oxygen reduction unit 107 that reduces oxygen in the container storage unit 102 and a water storage unit 111 that stores water to be supplied to the oxygen reduction unit 107. It is disposed below the evaporator 52 and to the side of the evaporator chamber 26.

  The oxygen reduction unit 107 includes a polymer electrolyte membrane 116, an anode catalyst layer 112 provided on one side of the polymer electrolyte membrane 116, a cathode catalyst layer 114 provided on the other side of the polymer electrolyte membrane 116, an anode An anode electrode 118 disposed outside the catalyst layer 112, a cathode electrode 120 disposed outside the cathode catalyst layer 114, a vaporization layer 122 disposed outside the anode electrode 118, and an outside of the vaporization layer 122 The water supply part 130 arrange | positioned in this.

  The polymer electrolyte membrane 116 is a thin film made of a polymer in which only cations move inside and anions and electrons do not move in the inside. For example, the polymer electrolyte membrane 116 becomes a thin film made of an organic polymer material having a sulfonic acid group. A thin film made of a perfluorocarbon sulfonic acid polymer is preferred because of its high conductivity. Specifically, as a polymer constituting the polymer electrolyte membrane 116, Nafion (registered trademark: manufactured by DuPont), Flemion (registered trademark: manufactured by Asahi Kasei Co., Ltd.), Aciplex (registered trademark: manufactured by Asahi Glass Co., Ltd.), etc. Examples thereof include a fluororesin having a sulfonic acid group. The film thickness of the polymer electrolyte membrane 116 is preferably 10 μm to 150 μm considering the membrane resistance. A more preferable film thickness is 30 μm to 100 μm.

  The anode catalyst layer 112 has a capability of oxidizing water and contains a catalyst (anode catalyst) that reduces the electrolysis voltage of water. The anode catalyst layer 112 generates hydrogen ions by electrolyzing the water supplied from the water supply unit 130. The anode catalyst is preferably supported on a base material. For example, the anode catalyst can be supported on a polymer constituting the polymer electrolyte membrane 116 as a base material.

  As described above, by adopting the polymer (proton conductive binder) constituting the polymer electrolyte membrane 116 as the base material for supporting the anode catalyst in the anode catalyst layer 112, adhesion between the anode catalyst layer 112 and the polymer electrolyte membrane 116 is achieved. Can be improved.

As the anode catalyst, for example, a composite oxide of a conductive metal oxide and a matrix oxide can be used. Examples of the conductive metal oxide include ruthenium oxide (RuO ₂ ) and iridium oxide (IrO ₂ ). Examples of the matrix oxide include titanium oxide (TiO ₂ ), tin oxide (SnO ₂ ), and tantalum oxide (Ta ₂ O ₅ ). The anode catalyst may be selected in consideration of its activity, durability, cost and the like. In addition to the above, the composite oxide that forms this catalyst includes, for example, RuO ₂ —Ta ₂ O, RuO ₂ —IrO ₂ , RuO ₂ —IrO ₂ —TiO ₂ , RuO ₂ —SnO ₂ , RuO ₂ —Ta ₂ O _5. , IrO ₂ —Ta ₂ O _{5 and the} like.

  In addition, as shown in FIG. 3, a mesh shape made of a metal such as titanium is provided between the side surfaces of the anode catalyst layer 112 that are not in contact with the polymer electrolyte membrane 116, that is, between the anode catalyst layer 112 and the anode electrode 118. A dimensionally stable electrode (DSA) 113 having an anode catalyst supported on a base material may be provided. The supported amount of the anode catalyst supported by the dimensionally stable electrode 113 is preferably smaller than the supported amount of the anode catalyst in the anode catalyst layer 112.

  Further, the anode catalyst layer 112 may include fine particles of a metal (for example, gold (Au)) having a lower electrical resistivity than the anode catalyst in addition to the above-described anode catalyst. By adding such metal fine particles, the electrical resistance of the anode catalyst layer 112 can be reduced, and the operating efficiency of the oxygen reduction unit 107 can be increased.

  The cathode catalyst layer 114 contains a catalyst (cathode catalyst) having an ability to reduce oxygen. The cathode catalyst layer 114 is preferably a porous layer formed of a cathode catalyst and a proton conductive binder. As the cathode catalyst, it is preferable that at least one of noble metal particles and noble metal alloy particles is supported on a conductive carrier.

  As the noble metal particles, particles composed of at least a noble metal selected from the group consisting of platinum (Pt), ruthenium (Ru), rhodium (Rh), palladium (Pd), and iridium (Ir) are preferable.

  When noble metal alloy particles are used as the cathode catalyst, it is possible to improve the dissolution resistance and activity of the cathode catalyst. Examples of such noble metal alloy particles include, but are not particularly limited to, the following description, alloys including only two or more kinds of noble metal elements, alloys including noble metal elements and other metal elements, and the like.

  The noble metal alloy particles can obtain a high catalytic activity effect. For this reason, noble metal alloy particles based on platinum Pt may be used. Specifically, an alloy of one or more noble metal elements and platinum Pt is preferable. The one or more noble metal elements include noble metals other than platinum (Pt) such as ruthenium (Ru), rhodium (Rh), palladium (Pd), iridium (Ir), such as titanium (Ti), vanadium (V), chromium ( Cr), manganese (Mn), iron (Fe), cobalt (Co), and nickel (Ni).

  The conductive support of the cathode catalyst layer 114 carries noble metal particles and / or noble metal alloy particles (that is, at least one of these particles). This conductive carrier is selected in consideration of electron conductivity, gas diffusibility, adhesion to the cathode catalyst, and the like. For example, carbon black, activated carbon, graphite and the like can be used, and a nanocarbon material can also be used. Examples of carbon black include furnace black, channel black, acetylene black, Vulcan (registered trademark; Cabot Corporation), and ketjen black. The nanocarbon material may be any of a fiber shape, a tube shape, a coil shape, and a sheet shape, for example.

  In addition, as shown in FIG. 3, a porous surface made of a water repellent and carbon particles is provided between the side surfaces of the cathode catalyst layer 114 that are not in contact with the polymer electrolyte membrane 116, that is, between the cathode catalyst layer 114 and the cathode electrode 120. And a gas diffusion layer (GDL: Gas Diffusion Layer) 119 made of an electrically conductive sheet material having moisture permeability and waterproof properties obtained by subjecting a carbon porous body such as carbon paper to a water repellent treatment. .

  The anode electrode 118 includes a mesh-shaped substrate 118a and a coating layer 118b that covers the surface of the substrate 118a. The substrate 118a constituting the anode electrode 118 is preferably formed of a material that does not elute when water is electrolyzed. For example, an oxide film such as titanium (Ti), aluminum (Al), or iron (Fe) is formed. It can be formed of an insulating material such as a metal, ceramics, resin, or glass.

  The coating layer 118b is made of a metal having a lower electrical resistivity than the anode catalyst of the anode catalyst layer 112 such as gold (Au). The coating layer 118b may be provided on both the surface of the substrate 118a facing the vaporization layer 122 and the surface facing the anode catalyst layer 112, and without providing the coating layer 118b on the surface facing the vaporization layer 122, It may be provided only on the surface facing the anode catalyst layer 112.

  As with the anode electrode 118, the cathode electrode 120 includes a mesh substrate 120a formed of an insulating material such as a metal or ceramic that forms an oxide film such as titanium (Ti), and platinum (Pt) that covers the surface of the substrate 120a. ) And gold (Au) and other coating layers 120b made of a metal.

  The anode electrode 118 and the cathode electrode 120 are connected to an external power supply device, the anode electrode 118 performs positive energization to the anode catalyst layer 112, the cathode electrode 120 performs minus energization to the cathode catalyst layer 114, and the anode catalyst layer 112 A voltage is applied between the cathode catalyst layer 114.

  In addition, an insulator 125 is provided between the electrodes 118 and 120 in order to prevent a short circuit due to contact between the anode electrode 118 and the cathode electrode 120. The insulator 125 is provided in a frame shape surrounding the periphery of the anode catalyst layer 112 and the cathode catalyst layer 114 that sandwich the polymer electrolyte membrane 116.

  The vaporized layer 122 is a material having excellent thermal conductivity, in other words, a material having high thermal responsiveness, for example, a moisture-permeable waterproof property obtained by subjecting a carbon porous body such as carbon paper, carbon cloth, carbon felt or the like to a water repellent treatment. Only the vaporized water vapor out of the water supplied from the water supply unit 130 is supplied to the anode electrode 118 side.

  The water supply unit 130 is made of a fabric such as a woven fabric or a non-woven fabric having water absorption, and one end portion (the lower end portion in the present embodiment) is immersed in water stored in the water storage unit 111, and water is sucked up from the water storage unit 111 to serve as an anode. The sucked water is held outside the water repellent layer 124 on the catalyst layer 112 side.

  The pair of fixing members 132 and 134 includes a water supply unit 130, a vaporization layer 122, an anode electrode 118, an anode catalyst layer 112, a polymer electrolyte membrane 116, a cathode catalyst layer 114, and a cathode electrode 120 that are sequentially stacked to sandwich the oxygen reduction unit 107. And fix. As shown in FIG. 3, the fixing member 134 disposed on the cathode electrode 120 side is provided with an opening 128 that penetrates in the front-rear direction at a position corresponding to the vent 110 of the storage container 104.

  The water storage part 111 has a concave shape for storing condensed water generated inside the cabinet 11 below the oxygen reduction unit 107. In the water storage part 111, the water supply path 35 for supplying the condensed water generated in the refrigeration evaporator 52 during the defrosting operation, and the condensed water overflowing from the water storage part 111 are discharged to the evaporation tray 32 provided in the machine room 30. The overflow path 36 is connected. The water supply path 35 extends from the drainage path 29 to one side in the width direction in the vicinity of the drain pan 27, is drawn to the side of the evaporator chamber 26, passes through the side of the evaporator chamber 26, and the water storage section of the oxygen reduction device 106. 111 is connected.

  In the oxygen reduction device 106 having such a configuration, when the defrost water generated in the refrigeration evaporator 52 is supplied to the water storage unit 111 via the water supply path 35 and stored, the water supply unit 130 removes the water storage unit 111. The frost water is sucked up and held outside the vaporized layer 122.

  Then, when a voltage is applied between the anode electrode 118 and the cathode electrode 120 in a state where water is held outside the vaporization layer 122, the water vapor that has passed through the vaporization layer 122 is electrolyzed in the anode catalyst layer 112 to form hydrogen. Ions are generated. Hydrogen ions generated in the anode catalyst layer 112 move to the cathode catalyst layer 114 through the polymer electrolyte membrane 116 and react with oxygen contained in the air in the oxygen reduction chamber 100 to generate water. The oxygen concentration in the oxygen reduction chamber 100 is decreased.

  According to the present embodiment having the above-described configuration, the anode catalyst 118 is not supported on the anode electrode 118 of the oxygen reduction device 106, and the anode catalyst 118 supports the anode catalyst supported by the anode catalyst layer 112. Therefore, the amount of the anode catalyst used in the anode electrode 118 can be suppressed, and the manufacturing cost can be reduced.

  Moreover, in the present embodiment, a large amount of anode catalyst is supported at a position close to the polymer electrolyte membrane 116, and water electrolysis occurs at a position close to the polymer electrolyte membrane 116, and hydrogen ions are likely to be generated. Therefore, the movement path until the hydrogen ions generated on the anode side reach the cathode side through the polymer electrolyte membrane 116 is shortened, and the concentration overvoltage on the anode side is lowered, so that the anode electrode 118 and the cathode electrode 120 are applied. Thus, the life of the oxygen reduction unit 107 can be extended.

  In the present embodiment, a dimensionally stable electrode 113 supporting an anode catalyst is provided between the anode catalyst layer 112 and the anode electrode 118, and the amount of anode catalyst supported by the dimensionally stable electrode 113 is set to the amount supported by the anode catalyst layer 112. By setting the amount smaller, the adhesion between the anode catalyst layer 112 and the anode electrode 118 can be enhanced while suppressing the amount of anode catalyst used.

  According to this embodiment, since the anode electrode 118 is provided with a metal having a lower electrical resistivity than the anode catalyst on the surface on the anode catalyst layer 112 side, the contact resistance with the anode catalyst layer 112 can be reduced. .

  Further, only the surface of the substrate 118a on the anode catalyst layer 112 side of the anode electrode 118 is coated with a metal having a lower electrical resistivity than the anode catalyst, and the amount of expensive metal such as gold (Au) is suppressed. Can be manufactured at low cost.

  Moreover, the substrate 118a constituting the anode electrode 118 can be formed of a metal forming an oxide film such as titanium (Ti), aluminum (Al), or iron (Fe), or an insulator such as ceramics, resin, or glass. Thus, ions are not eluted from the anode electrode 118 during electrolysis of water, and deterioration of the polymer electrolyte membrane 116 can be suppressed.

  In the above-described embodiment, the case where the anode catalyst 118 is not supported on the anode electrode 118 has been described. However, the present invention is not limited to this, and the anode electrode 118 is within a range smaller than the anode catalyst supported by the anode catalyst layer 112. An anode catalyst may be supported on the substrate. As described above, by supporting the anode catalyst on the anode electrode 118 in a range smaller than the anode catalyst layer 112, the adhesion between the anode catalyst layer 112 and the anode electrode 118 can be improved while suppressing the amount of the anode catalyst used. .

  As mentioned above, although embodiment of this invention was described, these embodiment was shown as an example and is not intending limiting the range of invention. These embodiments can be implemented in various other forms, and various omissions, replacements, and changes can be made without departing from the spirit of the invention. These embodiments and modifications thereof are included in the invention described in the claims and equivalents thereof as well as included in the scope and gist of the invention.

DESCRIPTION OF SYMBOLS 100 ... Hypoxic chamber, 102 ... Container storage part, 104 ... Storage container, 105 ... Lid, 106 ... Hypoxic device, 107 ... Hypoxic unit, 110 ... Vent, 111 ... Water storage part, 112 ... Anode catalyst layer, DESCRIPTION OF SYMBOLS 113 ... Stable electrode, 114 ... Cathode catalyst layer, 116 ... Polymer electrolyte membrane, 117 ... Porous membrane, 118 ... Anode electrode, 118a ... Substrate, 118b ... Cover layer, 119 ... Gas diffusion layer, 120 ... Cathode electrode, 120a ... substrate, 120b ... coating layer, 122 ... water repellent layer, 130 ... water supply part

Claims (7)

A polymer electrolyte membrane; an anode catalyst layer that carries a catalyst that lowers the electrolysis voltage of water and that electrolyzes water supplied from a water supply unit to generate hydrogen ions; and hydrogen ions generated in the anode catalyst layer; A cathode catalyst layer for generating water from oxygen; an anode electrode for energizing the anode catalyst layer; and a cathode electrode for energizing the cathode catalyst layer, the anode electrode, the anode catalyst layer, and the polymer electrolyte membrane In the oxygen reduction device in which the cathode catalyst layer and the cathode electrode are sequentially laminated,
The oxygen reduction device, wherein the amount of the catalyst supported by the anode catalyst layer is larger than the amount of the catalyst supported by the anode electrode.   The oxygen reduction apparatus according to claim 1, wherein the anode electrode includes a substance having an electric resistivity lower than that of the catalyst on a surface on the anode catalyst layer side.   3. The oxygen reduction device according to claim 2, wherein the anode electrode includes a substrate and a substance having an electric resistivity lower than that of the catalyst, and only the surface on the anode catalyst layer side of the substrate is coated with the substance.   The oxygen reduction device according to any one of claims 1 to 3, wherein the anode catalyst layer includes the catalyst and a substance having a lower electrical resistivity than the catalyst. The anode electrode includes a substrate and a coating layer that covers the surface of the substrate,
The oxygen reduction device according to any one of claims 1 to 4, wherein the substrate is made of a metal that forms an oxide film. The anode electrode includes a substrate and a coating layer that covers the surface of the substrate,
The oxygen reduction device according to any one of claims 1 to 4, wherein the substrate is formed of an insulator.   An oxygen reduction device according to any one of claims 1 to 6 and a storage container, wherein the oxygen reduction device supplies water from oxygen in the storage container and hydrogen ions generated in the anode catalyst layer. A refrigerator that generates and reduces oxygen in the storage container.

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