JP6104670B2 - Electrode and metal-air secondary battery - Google Patents

Description

The present invention is an electrode for use in metal-air secondary battery, and to a metal-air secondary battery using the electrode.

  2. Description of the Related Art Conventionally, metal-air batteries using a metal as a negative electrode active material and oxygen in the air as a positive electrode active material are known. For example, in Patent Document 1, in a metal-air battery, a metal carbonate is formed on a positive electrode by using a perovskite oxide having conductivity and a positive electrode containing a catalyst that promotes an oxygen reduction reaction and not containing carbon. A technique for preventing generation is disclosed.

Further, Patent Document 2 discloses an electrode for a secondary battery using a composition that works effectively for oxygen reduction and a composition that works effectively for oxygen generation by changing the composition of the perovskite oxide. Patent Document 3 discloses a method of forming an electrode catalyst made of perovskite LaMnO _3.00 by a reverse micelle method.

JP 2011-253789 A JP-A-2005-190833 JP 2000-67877 A

  As described above, Patent Document 2 discloses a method of combining a perovskite oxide having excellent oxygen generation characteristics and a perovskite oxide having excellent oxygen reduction characteristics. However, freedom of development of a secondary battery is disclosed. In order to increase the degree, other methods for efficiently charging and discharging are also required. Further, in the secondary battery, it is required to improve the durability of the electrode. However, since the electrode of Patent Document 2 contains conductive carbon, the conductive carbon is corroded (deteriorated) by oxygen generated during charging. Problems arise in the durability of the electrode.

  This invention is made | formed in view of the said subject, and makes it the main objective to perform charging and discharge efficiently in a secondary battery.

The invention according to claim 1 is an electrode used in a metal-air secondary battery, comprising a conductive layer having conductivity, and a catalyst layer laminated on the conductive layer, Kinds of perovskite-type oxide particles and manganese dioxide particles are dispersed , the one kind of perovskite-type oxide is conductive, has an oxygen generation reaction superior to that of manganese dioxide, and the conductive layer and The catalyst layer does not contain conductive carbon .

  A second aspect of the present invention is the electrode according to the first aspect, wherein particles of another type of perovskite oxide are further dispersed in the catalyst layer.

Invention of Claim 3 is an electrode used for a metal air secondary battery, Comprising: It has the conductive layer which has electroconductivity, and the catalyst layer laminated | stacked on the said conductive layer, In the said catalyst layer, One kind of perovskite oxide particles and one other kind of perovskite oxide particles are dispersed, the one kind of perovskite oxide is conductive, and the other kind of perovskite oxide is conductive. The oxygen generation reaction is superior to that of the perovskite oxide, the other kind of perovskite oxide is conductive, the oxygen reduction reaction is superior to the one kind of perovskite oxide, and the conductive layer and The catalyst layer does not contain conductive carbon.

Invention of Claim 4 is a metal air secondary battery, Comprising: Between the positive electrode layer which is an electrode in any one of Claim 1 thru | or 3 , a negative electrode layer, the said negative electrode layer, and the said positive electrode layer And an electrolyte layer disposed on the substrate.

According to the present invention, charging and discharging can be efficiently performed in a secondary battery. Further, it is possible to improve the durability of the electrodes.

It is a figure which shows the structure of a metal air battery. It is a figure which shows the other example of a metal air battery.

  FIG. 1 is a diagram showing a configuration of a metal-air battery 1 according to an embodiment of the present invention. The main body 11 of the metal-air battery 1 has a substantially cylindrical shape centered on the central axis J1, and FIG. As shown in FIG. 1, the metal-air battery 1 is a secondary battery including a positive electrode layer 2, a negative electrode layer 3, and an electrolyte layer 4, and the negative electrode layer 3, the electrolyte layer from the central axis J1 toward the outside in the radial direction. 4 and the positive electrode layer 2 are arranged concentrically in order.

  The negative electrode layer 3 (also referred to as a metal electrode) is a cylindrical porous member centered on the central axis J1, and is made of a metal such as magnesium (Mg), aluminum (Al), zinc (Zn), iron (Fe), etc. Or an alloy containing any one of the metals. In the present embodiment, the negative electrode layer 3 is made of zinc and has a cylindrical shape with an outer diameter of 11 millimeters (mm) and an inner diameter of 5 mm. As shown in FIG. 1, a negative electrode current collecting terminal 33 is connected to the end of the negative electrode layer 3 in the direction of the central axis J1. A space 31 (hereinafter referred to as “filling portion 31”) surrounded by the inner surface of the negative electrode layer 3 is filled with an aqueous electrolyte solution (also referred to as an electrolyte solution).

  An electrolyte layer 4 surrounding the periphery of the negative electrode layer 3 is provided outside the negative electrode layer 3. The electrolyte layer 4 has a cylindrical porous member 41, and the inner surface of the porous member 41 faces the outer surface of the negative electrode layer 3. The electrolyte layer 4 communicates with the filling portion 31 through the pores of the porous negative electrode layer 3, and the porous member 41 is also filled with the electrolytic solution. The porous member 41 is formed of ceramic, metal, inorganic material, organic material, or the like, and is preferably a sintered body (that is, integrally molded) of highly insulating ceramic such as alumina, zirconia, or hafnia. . From the viewpoint of preventing an increase in the distance between the negative electrode layer 3 and the positive electrode layer 2 described later while securing a certain degree of mechanical strength, the thickness of the porous member 41 is 0.5 mm or more and 4 mm or less. It is preferable. The electrolytic solution in the present embodiment is a high-concentration alkaline aqueous solution (for example, an 8M (mol / L) potassium hydroxide (KOH) aqueous solution), and is obtained by saturating zinc oxide as necessary. The electrolytic solution may be another aqueous electrolytic solution or a non-aqueous (for example, organic solvent based) electrolytic solution.

  The positive electrode layer 2 (also referred to as an air electrode) includes a gas diffusion layer 22 that is a porous conductive layer and a porous catalyst layer 23. The gas diffusion layer 22 has a cylindrical shape surrounding the porous member 41, and the catalyst layer 23 is provided in a cylindrical shape between the gas diffusion layer 22 and the porous member 41. In other words, the electrolyte layer 4 containing the electrolytic solution is disposed between the positive electrode layer 2 and the negative electrode layer 3. A current collecting layer 24 is formed by winding a mesh sheet of metal such as nickel around the gas diffusion layer 22 having conductivity, and a positive electrode current collector is formed at the end of the current collecting layer 24 in the central axis J1 direction. The electric terminal 25 is connected. An interconnector that contacts only a part of the outer surface of the gas diffusion layer 22 may be provided as the current collecting layer 24.

From the viewpoint of preventing deterioration due to oxidation during charging, which will be described later, the gas diffusion layer 22 preferably does not contain conductive carbon (for example, carbon black such as acetylene black) as a conductive auxiliary agent. Then, the gas diffusion layer 22 is mainly formed of a conductive perovskite oxide (for example, LaNiO ₃ ). The gas diffusion layer 22 includes a water-repellent material, for example, a fluorine-based resin such as PFA (perfluoroalkoxyalkane) or PTFE (polytetrafluoroethylene), and the electrolyte leaks to the outside of the gas diffusion layer 22. Is prevented. In principle, in the metal-air battery 1, an interface between air and the electrolytic solution is formed in the vicinity of the porous catalyst layer 23, and most of the gas diffusion layer 22 does not touch the electrolytic solution.

  Such a gas diffusion layer 22 is prepared by mixing, for example, perovskite oxide particles, fluorine resin particles, a surfactant and water, and drying and heat-treating to produce a gas diffusion layer powder. The gas diffusion layer powder is formed by pressure bonding onto a mesh sheet (current collection layer) made of nickel or nickel-plated copper. At this time, the fluorine-based resin also functions as a binder for the gas diffusion layer powder.

Similar to the gas diffusion layer 22, the catalyst layer 23 preferably does not contain conductive carbon from the viewpoint of preventing deterioration due to oxidation during charging, which will be described later. In the catalyst layer 23, and the particles of the conductive perovskite oxide superior in the oxygen evolution reaction _{(LaNiO 3, La x Sr 1} -x Mn y Co 1-y O 3 , etc.), the oxygen reduction reaction and has a conductivity Excellent manganese dioxide (MnO ₂ ) particles are dispersed. The catalyst layer 23 is formed, for example, by applying a powder for a catalyst layer in which perovskite oxide particles and manganese dioxide particles are highly dispersed on the gas diffusion layer 22 and pressurizing it. Note that the catalyst layer 23 may contain a fluorine-based resin.

  Preferably, in the catalyst layer powder, perovskite oxide particles are supported (fixed) in a highly dispersed manner using perovskite oxide particles as a carrier, or perovskite oxide particles using manganese dioxide particles as a carrier. Is supported in a highly dispersed state. When the manganese dioxide particles are supported on the perovskite oxide particles, for example, a well-known hydrothermal synthesis method is used. When the perovskite oxide particles are supported on manganese dioxide particles, for example, the reverse micelle method is used. The catalyst layer powder in which both are highly dispersed may be produced by mechanically pulverizing and mixing the perovskite oxide particles and manganese dioxide particles.

The crystal structure of the manganese dioxide is not limited and may be any of α, β, γ, λ, and δ types. The method for synthesizing manganese dioxide may be any of EMD (electrolytic method), CMD (chemical synthesis method), hydrothermal synthesis method, solution method, and sol-gel method. Moreover, it is preferable that it is 1-500 m < ² > / g, and, as for the BET surface area (surface area by a gas adsorption method) of manganese dioxide to be used, it is more preferable that it is 10-100 m < ² > / g.

Various methods can be used for the synthesis and fine particle formation of perovskite oxides. For example, when producing a perovskite oxide having a particle size of 500 nanometers (nm) or less, a method described in JP-A-2005-190833 (Patent Document 2) or a method of directly synthesizing an oxide is used. Can be used. Preferably, a reverse homogeneous precipitation method or a reverse micelle method is used, whereby a perovskite oxide having a particle size of 100 nm or less and a specific surface area of about 10 m ² / g can be easily obtained.

  As shown in FIG. 1, disk-shaped blocking members 51 are fixed to both end surfaces (upper end surface and lower end surface in FIG. 1) of the negative electrode layer 3, the electrolyte layer 4, and the positive electrode layer 2 in the central axis J1 direction. The A through hole 511 is provided in the center of each closing member 51, and the through hole 511 opens toward the filling portion 31.

  One end of the supply pipe 61 is connected to the through hole 511 of one closing member 51, and the other end of the supply pipe 61 is connected to the supply / recovery unit 6. One end of the recovery pipe 62 is connected to the through hole 511 of the other closing member 51, and the other end of the recovery pipe 62 is connected to the supply / recovery unit 6. The supply / recovery unit 6 includes an electrolytic solution storage tank and a pump, and recovers the electrolytic solution in the filling unit 31 to the storage tank at a flow rate (volume per unit time) indicated by a control unit (not shown). At the same time, the electrolytic solution in the storage tank can be supplied to the filling unit 31 at the same flow rate. That is, the electrolytic solution can be circulated between the filling unit 31 and the storage tank of the supply and recovery unit 6. The supply and recovery unit 6 is provided with a filter, and unnecessary substances contained in the electrolytic solution are removed by the filter when the electrolytic solution is circulated.

  In the metal-air battery 1 according to the present embodiment, the central axis J1 of the main body 11 is parallel to the vertical direction (gravity direction), and the through hole 511 connected to the recovery pipe 62 is a through hole connected to the supply pipe 61. It is located vertically below 511. The supply pipe 61 and the recovery pipe 62 are provided with a supply valve and a recovery valve (not shown). In normal operation in this operation example, the electrolyte solution is circulated at a constant flow rate. The supply valve and the recovery valve can be regarded as a part of the supply recovery unit 6. The central axis J1 of the metal-air battery 1 does not necessarily need to be parallel to the vertical direction. For example, the metal-air battery 1 may be arranged so that the central axis J1 is parallel to the horizontal direction.

  When discharging is performed in the metal-air battery 1 of FIG. 1, the negative current collector terminal 33 and the positive current collector terminal 25 are electrically connected via a load (for example, a lighting fixture). The metal contained in the negative electrode layer 3 is oxidized to generate metal ions, and the electrons are supplied to the positive electrode layer 2 through the negative electrode current collector terminal 33, the positive electrode current collector terminal 25, and the current collector layer 24. In the porous positive electrode layer 2, oxygen in the air that has passed through the current collecting layer 24 is reduced by the electrons supplied from the negative electrode layer 3, and is eluted into the electrolyte as hydroxide ions. In the positive electrode layer 2, the oxygen reduction reaction is promoted by the catalyst contained in the catalyst layer 23.

  On the other hand, when the metal-air battery 1 is charged, a voltage is applied between the negative electrode current collector terminal 33 and the positive electrode current collector terminal 25, and electrons are supplied from the hydroxide ions to the positive electrode layer 2. And oxygen is generated. In the negative electrode layer 3, metal ions are reduced by electrons supplied to the negative electrode current collector terminal 33 via the current collector layer 24 and the positive electrode current collector terminal 25, and metal is deposited on the surface (outer surface). In the positive electrode layer 2, the generation of oxygen is promoted by the catalyst contained in the catalyst layer 23.

  As described above, in the metal-air battery 1, the electrolytic solution is circulated by the supply and recovery unit 6, and the electrolytic solution (hereinafter also referred to as “lower through-hole 511”) in the vicinity of the lower through-hole 511. Most of the electrolyte solution is in the filling portion 31, but the electrolyte solution in the negative electrode layer 3 and the electrolyte layer 4 is also slightly contained.) Is recovered from the through hole 511. In addition, a part of the electrolytic solution supplied into the filling portion 31 from the upper through hole 511 (hereinafter also referred to as “upper through hole 511”) passes through the pores of the negative electrode layer 3 to the electrolyte layer 4 ( It also diffuses into the porous member 41). In this way, the electrolyte solution from the supply and recovery unit 6 is also mixed in the electrolyte layer 4. Thereby, while discharging or charging in the metal-air battery 1, the electrolyte contained in the electrolyte layer 4 is gradually replaced with the electrolyte in the storage tank of the supply and recovery unit 6.

  In the metal-air battery 1, the operation of sequentially collecting the predetermined amount of electrolyte from the lower through-hole 511 and supplying the same amount of electrolyte from the upper through-hole 511 may be repeated. Thereby, the electrolytic solution contained in the electrolyte layer 4 is replaced with the electrolytic solution in the storage tank of the supply and recovery unit 6 while discharging or charging. It is also possible to intermittently replace the electrolyte. For example, after the electrolytic solution is circulated for a predetermined time, the supply valve and the recovery valve are closed, and the recovery and supply of the electrolytic solution are stopped until the diffusion of the new electrolytic solution reaches an equilibrium state. As a result, the electrolyte solution in the main body 11 is exchanged (mixing of the deteriorated electrolyte solution and a new electrolyte solution) while discharging or charging. Of course, the electrolytic solution in the main body 11 may be exchanged by stopping discharging or charging.

  As described above, in the metal-air battery 1, the catalyst layer 23 in which one kind of perovskite oxide particles and manganese dioxide particles are dispersed with respect to the gas diffusion layer 22 having conductivity. Laminated. Thereby, the metal air battery 1 which can perform charging and discharging efficiently can be manufactured at low cost without using an expensive noble metal or the like. Moreover, since the gas diffusion layer 22 and the catalyst layer 23 which are conductive layers do not contain conductive carbon, the durability of the positive electrode layer 2 which is a gas diffusion electrode can be improved.

In addition, in the catalyst layer 23 of the metal-air battery 1, in addition to the perovskite oxide and manganese dioxide, other types of conductive perovskite oxides (preferably excellent in oxygen reduction reaction) (LaNiO ₃ , La _{x). Sr 1-x Mn y Co 1} -y O 3, La x Sr 1-x Mn y Fe 1-y O 3, La x Sr 1-x (Mn z Co 1-z) y Fe 1-y O 3, La _x Sr _1-x MnO ₃ etc.) may be further dispersed.

  In such a catalyst layer 23, for example, particles of one perovskite oxide (hereinafter referred to as “first perovskite oxide”) and other perovskite oxide (hereinafter referred to as “second perovskite oxide”). Is carried out). In this case, first, the first perovskite-type oxide particles are prepared by a coprecipitation method, a reverse uniform precipitation method, a sol-gel method, an organic complex method, a solid phase method, a reverse micelle method, or the like. Subsequently, when the second perovskite oxide particles are produced by the reverse micelle method, the second perovskite oxide particles are added to the first perovskite oxide particles by adding the first perovskite oxide particles. Particles are highly dispersed and supported. Preferably, the average particle diameter of the first perovskite oxide particles is 500 nm or more, and the average particle diameter of the second perovskite oxide particles is 500 nm or less. Then, a high specific surface area manganese dioxide is supported or mixed in a highly dispersed state by hydrothermal synthesis or mechanical mixing to the particles (perovskite oxide composite) to produce catalyst layer powder. Is done.

  As described above, in the catalyst layer 23, in addition to the one kind of perovskite oxide and manganese dioxide particles, the other one kind of perovskite oxide particles are further dispersed. The battery 1 can be charged and discharged more efficiently.

  Next, a production example of the positive electrode layer 2 will be described. First, preparation examples of the perovskite-type oxide particles contained in the catalyst layer powder by the reverse micelle method and reverse uniform precipitation method will be described, and subsequently, an preparation example of the electrode using the perovskite-type oxide particles will be described.

(Reverse micelle method)
To 108 g of cyclohexane, 90 g of hexaethylene glycol nonylphenyl ether as a surfactant was added and stirred at 10 ° C. Subsequently, 10 mL of a metal nitrate aqueous solution in which La (NO ₃ ) ₃ and Mn (NO ₃ ) ₂ are mixed so as to have a concentration of 0.2 M (mol / L) is added to the solution. Reverse micelle solution A was prepared by stirring at 0 ° C. In addition, 270 g of hexaethylene glycol nonylphenyl ether as a surfactant and 30 mL of a 10 wt% tetramethylammonium hydroxide aqueous solution were added to 324 g of cyclohexane and stirred at 10 ° C. for 2 hours to prepare a reverse micelle solution B. did.

The reverse micelle solution B was slowly added to the reverse micelle solution A, and after confirming that the solution changed to brown, the mixture was stirred for 2 hours. Moreover, 200 mL of ethanol was added to the mixed solution, and sonication was performed for 10 minutes. Thereafter, the product was filtered off and washed with ethanol. The obtained residue was dried at 120 ° C. for 12 hours or more to obtain an oxide precursor. The obtained precursor was pulverized in a mortar and then calcined at 550 to 650 ° C. for 5 hours in air or nitrogen atmosphere to obtain particles of a perovskite oxide LaMnO ₃ .

(Reverse homogeneous precipitation method)
1 × 10 ⁻² mol of lanthanum nitrate hexahydrate and manganese nitrate hexahydrate were mixed in 100 mL of distilled water to prepare a mixed solution of metal nitrate. Subsequently, a hydroxide generated in a stoichiometric ratio, an equivalent amount of tetrapropylammonium bromide, and an aqueous solution of 1 to 20% by weight of tetramethylammonium hydroxide were mixed to prepare an alkaline precipitation solution. While vigorously stirring the alkaline precipitation solution, a metal nitrate aqueous solution was added dropwise at 1 to 10 mL per minute, and the whole was further stirred for 1 hour after dropping. Subsequently, aging was performed by standing for 1 hour, and the product was separated by suction filtration, and then the residue was washed with distilled water and 2-propanol. After washing, the resulting residue was dried at 120 ° C. for 12 hours or longer to obtain an oxide precursor. The obtained precursor was pulverized in a mortar and then calcined at 650 to 950 ° C. for 5 hours in an air or nitrogen atmosphere to obtain particles of a perovskite oxide LaMnO ₃ .

(Production of electrodes)
A nickel mesh (100 mesh manufactured by Nilaco Co., Ltd.) was laid on the bottom of a hot press mold having an inner diameter of 15 mm, and 40 mg of separately prepared powder for gas diffusion layer was filled on the nickel mesh and uniaxially pressurized at 1.3 MPa. . Subsequently, 25 mg of the catalyst layer powder in which the perovskite oxide particles and separately prepared manganese dioxide particles were highly dispersed was filled on a nickel mesh, and uniaxially pressurized at 2.6 MPa. The mold was heated to 360 ° C., uniaxially pressurized at 5.2 MPa, and then rapidly cooled to obtain a gas diffusion electrode.

  Next, a preparation example of the positive electrode layer 2 in the case where the catalyst layer powder further includes particles of other types of perovskite oxides will be described. In this production example, one of two types of perovskite oxides is used as the other of the above-described electrode production examples (examples of production of electrodes in which the catalyst layer includes particles of perovskite oxide and manganese dioxide). Since the treatment to be carried (that is, the production of particles of the supported perovskite oxide) is added, only the treatment will be described.

(Preparation of supported perovskite oxide particles)
To 40 g of cyclohexane, 41 g of polyoxyethylene nonylphenyl ether as a surfactant was added and stirred at 10 ° C. Subsequently, 2.5 mL of a metal nitrate aqueous solution in which La (NO ₃ ) ₃ and Mn (NO ₃ ) ₂ are mixed so as to have a concentration of 0.2 M is added to the solution, and the mixture is kept at 10 ° C. until the mixed solution becomes transparent. A reverse micelle solution A was prepared by stirring. In addition, 123 g of polyoxyethylene nonylphenyl ether and 15 mL of a 10 wt% tetramethylammonium hydroxide aqueous solution as surfactants were added to 120 g of cyclohexane and stirred at 10 ° C. for 2 hours to prepare reverse micelle solution B. After 240 mg of LaNiO ₃ was added to the reverse micelle solution A and stirred for 1 hour, the reverse micelle solution B was slowly added and stirred for another 2 hours. Subsequently, 200 mL of ethanol was added to the mixed solution, and sonication for 10 minutes was performed. Thereafter, the product was filtered off and washed with ethanol. The obtained residue was dried at 120 ° C. for 12 hours or more. Then, after grinding the product in a mortar and calcined 5 hours at 550 to 650 ° C. in an air or nitrogen atmosphere to obtain a perovskite-type oxide LaNiO ₃ carrying the perovskite oxide LaMnO _3.

  FIG. 2 is a diagram illustrating another example of the metal-air battery 1. In the metal-air battery 1 of FIG. 2, the structure of the positive electrode layer 2a is different from that of the metal-air battery 1 of FIG.

  The positive electrode layer 2 a includes a porous conductive layer 22 a having conductivity, and the conductive layer 22 a is formed (laminated) on the outer surface of the porous member 41 in the electrolyte layer 4. A catalyst layer 23 is formed on the outer surface of the conductive layer 22a. A current collecting layer 24 is formed around the catalyst layer 23, and a positive electrode current collecting terminal 25 is connected to an end of the current collecting layer 24 in the direction of the central axis J1. A porous layer made of a water repellent material is formed as the liquid repellent layer 29 outside the current collecting layer 24. In principle, the metal-air battery 1 forms an interface between air and an electrolyte near the porous catalyst layer 23. The material for forming the conductive layer 22a and the catalyst layer 23 is the same as that of the metal-air battery 1 of FIG.

  Also in the metal-air battery 1 of FIG. 2, the catalyst layer 23 is laminated on the conductive layer 22 a having conductivity. In the catalyst layer 23, one kind of perovskite oxide particles and manganese dioxide particles are dispersed. Therefore, charging and discharging can be performed efficiently. Further, since the conductive layer 22a and the catalyst layer 23 do not contain conductive carbon, the durability of the positive electrode layer 2a can be improved. Of course, in the catalyst layer 23 of the metal-air battery 1 of FIG. 2, particles of another type of perovskite oxide may be further dispersed.

  The metal-air battery 1 can be variously modified. For example, manganese dioxide may be omitted in the catalyst layer 23 in which manganese dioxide particles, one kind of perovskite oxide particles, and another kind of perovskite oxide particles are dispersed. . Even in this case, one perovskite oxide is superior in oxygen generation reaction than the other perovskite oxide, and the other perovskite oxide is superior in oxygen reduction reaction than the one perovskite oxide. As a result, the metal-air battery 1 can be charged and discharged efficiently. Further, since the conductive layer (the gas diffusion layer 22 or the conductive layer 22a) and the catalyst layer 23 do not contain conductive carbon, the durability of the positive electrode layers 2 and 2a that are electrodes can be improved.

  In the metal-air battery 1, it is not always necessary to circulate the electrolytic solution. The electrode including the conductive layer (the gas diffusion layer 22 or the conductive layer 22a) and the catalyst layer 23 may be used in a metal-air battery other than a zinc-air battery, and further used in other secondary batteries. It's okay.

  The configurations in the above-described embodiments and modifications may be combined as appropriate as long as they do not contradict each other.

DESCRIPTION OF SYMBOLS 1 Metal-air battery 2, 2a Positive electrode layer 3 Negative electrode layer 4 Electrolyte layer 22 Gas diffusion layer 22a Conductive layer 23 Catalyst layer

Claims (4)

An electrode used in a metal-air secondary battery,
A conductive layer having conductivity;
A catalyst layer laminated on the conductive layer;
With
In the catalyst layer, one kind of perovskite oxide particles and manganese dioxide particles are dispersed ,
The one kind of perovskite oxide is conductive and has an oxygen generation reaction superior to that of the manganese dioxide,
The electrode, wherein the conductive layer and the catalyst layer do not contain conductive carbon . The electrode according to claim 1,
In the catalyst layer, another kind of perovskite oxide particles are further dispersed. An electrode used in a metal-air secondary battery,
A conductive layer having conductivity;
A catalyst layer laminated on the conductive layer;
With
In the catalyst layer, one kind of perovskite oxide particles and another kind of perovskite oxide particles are dispersed,
The one kind of perovskite oxide is electrically conductive, has an oxygen generation reaction superior to that of the other kind of perovskite oxide, and the other kind of perovskite oxide is electrically conductive. The oxygen reduction reaction is superior to the one kind of perovskite oxide,
The electrode, wherein the conductive layer and the catalyst layer do not contain conductive carbon. A metal-air secondary battery,
A positive electrode layer which is the electrode according to any of claims 1 to 3,
A negative electrode layer;
An electrolyte layer disposed between the negative electrode layer and the positive electrode layer;
A metal-air secondary battery comprising:

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