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WO2013179807A1 - Metal-air secondary battery - Google Patents

Metal-air secondary battery Download PDF

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Publication number
WO2013179807A1
WO2013179807A1 PCT/JP2013/061705 JP2013061705W WO2013179807A1 WO 2013179807 A1 WO2013179807 A1 WO 2013179807A1 JP 2013061705 W JP2013061705 W JP 2013061705W WO 2013179807 A1 WO2013179807 A1 WO 2013179807A1
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Prior art keywords
electrode member
secondary battery
metal
positive electrode
air secondary
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French (fr)
Japanese (ja)
Inventor
心 ▲高▼橋
孝亮 馮
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Hitachi Ltd
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Hitachi Ltd
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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M12/00Hybrid cells; Manufacture thereof
    • H01M12/08Hybrid cells; Manufacture thereof composed of a half-cell of a fuel-cell type and a half-cell of the secondary-cell type
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/86Inert electrodes with catalytic activity, e.g. for fuel cells
    • H01M4/8605Porous electrodes
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/38Selection of substances as active materials, active masses, active liquids of elements or alloys
    • H01M4/381Alkaline or alkaline earth metals elements
    • H01M4/382Lithium
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/86Inert electrodes with catalytic activity, e.g. for fuel cells
    • H01M4/90Selection of catalytic material
    • H01M4/9016Oxides, hydroxides or oxygenated metallic salts
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

Definitions

  • the present invention relates to a chargeable and dischargeable metal air secondary battery.
  • HEVs hybrid electric vehicles
  • the performance of these motor vehicles depends largely on the characteristics of the storage battery, which is a source of electrical energy. Therefore, development of a storage battery having excellent characteristics is in progress.
  • Lithium ion secondary batteries are characterized by their light weight and high output compared to other conventional secondary batteries, and are widely used in storage batteries mounted in various other devices including electric vehicles. It is done. At present, the weight energy density of the lithium ion secondary battery actually obtained is about 100 Wh / kg, and the theoretical upper limit thereof is considered to be about 400 Wh / kg. However, for the full-scale spread of electric vehicles, a storage battery with a further large capacity is required, and it is also said that a weight energy density of at least about 500 Wh / kg is required. Therefore, there is a demand for development of an innovative battery that can be expected to have a greater weight energy density than a lithium ion secondary battery.
  • a lithium-containing transition metal oxide represented by lithium cobaltate is used as a positive electrode material. That is, since the transition metal element which is the constituent element is a heavy metal, when it is incorporated into a storage battery as a positive electrode material, the weight increases and as a result, the weight energy density decreases. Therefore, in order to avoid such limitations, metal-air batteries that use oxygen in the air as the positive electrode material and metal in the negative electrode material have recently attracted attention. When power storage is performed using a metal-air battery as a storage battery, the weight can be reduced as compared with a conventional lithium ion battery, and therefore, cost reduction can be expected.
  • metal-air batteries using zinc have been put to practical use and used as a power source for hearing aids and the like.
  • the metal-air battery so far has remained in practical use as a primary battery, and has not been put into practical use as a chargeable / dischargeable secondary battery.
  • Patent Document 1 discloses the following technology.
  • Patent Document 1 discloses a configuration using a composite oxide having an alkali metal or an alkaline earth metal, a transition metal, and oxygen in a lithium-air battery as a catalyst.
  • the charge voltage is as high as about 4.3 V, and the charge / discharge energy efficiency is therefore low.
  • Patent Document 2 does not mention the charging voltage.
  • a metal-air secondary battery comprises a negative electrode member for absorbing and releasing metal ions, a positive electrode member for ionizing oxygen, and a separator impregnated with an electrolyte disposed between the negative electrode member and the positive electrode member.
  • the positive electrode member has pores of 2 nm or less, and a volume A of the pores and a product volume B calculated from the discharge capacity of the secondary battery. It is characterized in that the ratio (B / A) is 0.1 or less.
  • FIG. 1 is a schematic view showing a cross section of a metal air secondary battery according to an embodiment of the present invention.
  • This metal air secondary battery is a lithium air secondary battery having a battery cell of a joint structure using metal lithium (Li) for the negative electrode.
  • the positive electrode member 1 and the negative electrode member 3 are disposed with the separator 2 impregnated with the electrolytic solution interposed therebetween, and these constitute one battery cell.
  • An O-ring 4 is disposed around the negative electrode member 3. The battery cell is fixed in a state of being held between the pressure plate 5 and the current collector 6 by the clamping force that the pressure plate 5 receives from the clamping spring 7.
  • An oxygen gas acting as a positive electrode active material is enclosed between the current collector 6 and the oxygen filling valve 8.
  • the negative electrode member 3 occludes and releases metal ions with the electrolytic solution impregnated in the separator 2.
  • disc-shaped metallic lithium having a diameter of 8 mm and a thickness of 1 mm was used as the negative electrode member 3.
  • the electrode area of the negative electrode member 3 can be defined as the area of metal lithium in a portion in contact with the separator 2 and is about 0.5 cm 2 .
  • disk-shaped polyethylene having a diameter of 13 mm larger than that of the negative electrode member 3 was used.
  • the positive electrode member 1 ionizes oxygen which is a positive electrode active material.
  • FIG. 2 is a schematic view showing the configuration of the positive electrode member 1.
  • the positive electrode member 1 is configured by mixing a catalyst 1b, a binder 1c and a support 1d and applying the mixture to a substrate 1a.
  • the catalyst 1 b, the binder 1 c, and the carrier 1 d are mixed in a weight ratio of 5: 4: 1, respectively, and the mixture is applied to the substrate 1 a to form the positive electrode member 1.
  • the base material 1a is a conductive substance mainly constituting the positive electrode member 1, and for example, carbon, metal or the like is used.
  • a substrate having a large specific surface area (for example, 100 m 2 / g or more) and high electric conductivity is preferable.
  • activated carbon or a metal porous body can be used as the substrate 1a.
  • the catalyst 1 b is a powdery substance having a function of assisting the reaction of the formula (2) or the reaction of the formula (5) on the positive electrode side to thereby improve the discharge voltage and reduce the charge voltage.
  • the support 1d has a function of supporting the catalyst 1b on the base 1a, and the binder 1c has a function of binding the base 1a, the catalyst 1b and the support 1d to each other.
  • the details of the substances used as the catalyst 1b, the binder 1c, and the carrier 1d will be described in the respective examples described later.
  • the size of the positive electrode member 1 is preferably smaller than that of the separator 2 described above and larger than that of the negative electrode member 3. That is, these sizes can be set so that the separator 2 is the largest and becomes smaller in the order of the positive electrode member 1 and the negative electrode member 3.
  • the separator 2 is impregnated with an electrolytic solution using LiPF 6 as an electrolyte.
  • LiPF 6 as an electrolyte, one in which 1 mol of LiPF 6 was dissolved in propylene carbonate which is a non-aqueous solvent was used.
  • an electrolytic solution After several drops of an electrolytic solution are dropped on the surface of the positive electrode member 1 and the surface of the negative electrode member 3 respectively, the separator 2 is sandwiched between the positive electrode member 1 and the negative electrode member 3 with these surfaces inside.
  • the separator 2 was impregnated with LiPF 6 as an electrolyte.
  • the current collector 6 is a stainless steel mesh having a thickness of 1 mm.
  • the base material 1a is made into a metal porous body in the positive electrode member 1 as mentioned above, it is also possible to use this as the current collector 6.
  • the pressure plate 5 is made of stainless steel, and urges the negative electrode member 3 and the O-ring 4 in the direction of the separator 2 in accordance with the tightening force received from the tightening spring 7.
  • the negative electrode member 3, the separator 2 and the positive electrode member 1 are in close contact with each other.
  • the oxygen filling valve 8 is opened, and oxygen gas having a concentration of 99.9% is flowed at a flow rate of 500 ml / min for about 10 to 15 minutes to flow into the battery cell from the outside of the current collector 6. The Thereafter, by closing the oxygen filling valve 8, oxygen gas was filled in the battery cell.
  • manganese dioxide MnO 2
  • carbon is used as the carrier 1d
  • PVDF polyvinylidene fluoride
  • carbon was used as the carrier 1d. Specific examples thereof will be described below based on Table 1 as Examples 1 to 7 and Comparative Example 1. Table 1 shows a list of materials used in Examples 1 to 7 of the present invention and Comparative Example 1 and an average charging voltage.
  • Example 1 In Example 1, as the carrier 1d, one having a total pore volume of 15.8 mL / g (wherein g represents the weight of the carrier, and the same applies hereinafter) and a micropore volume of 2 nm or less of 0.499 mL / g The positive electrode member 1 was configured using.
  • Example 2 to 7 In Examples 2 to 7, the positive electrode member 1 was similarly configured using the carrier 1d shown in Table 1.
  • Comparative example 1 In Comparative Example 1, the positive electrode member 1 was formed of the same material as the carrier 1 d shown in Example 7.
  • each metal air secondary battery of each of Examples 1 to 7 and Comparative Example 1 was placed in a terminal-equipped desiccator, and after argon gas was sealed in the inside of the desiccator, charge / discharge evaluation of the outer terminal of the desiccator It attached to the device and measured.
  • the average charging voltage obtained by this experiment is shown in Table 1. As shown in the table, it was found that the average charge voltage increased to 4 V when the pore volume of 2 nm or less and the product volume occupancy ratio exceeded 10%.
  • the charge voltage is low when the ratio of pore volume / total pore volume at an average charge voltage of 2 nm or less is at least 15% or more.
  • the metal-air secondary battery is disposed between the negative electrode member 3 for absorbing and releasing lithium ions, the positive electrode member 1 for ionizing oxygen, the negative electrode member 3 and the positive electrode member 1.
  • the product volume B calculated from the pore volume A of the positive electrode member and the maximum discharge capacity x (Ah) of the metal-air secondary battery, the B / A ratio is provided. Since x is controlled and used so as to be equal to or less than a predetermined value, it is possible to achieve the reduction of the charge over voltage in the metal-air secondary battery.
  • the pores have pores of 2 nm or less, and charging is performed when the ratio of the product volume calculated from the pore volume to the maximum discharge capacity is 0.1 or less.
  • the voltage can be reduced.
  • the pore of 2 nm or less is defined by the BET method.
  • the present invention is not limited to this, and a conductive material such as aluminum, nickel, SUS or the like may be used. These conductive materials may themselves have pores, or may be formed by solidifying powder to form a positive electrode member.
  • solvents other than propylene carbonate for example, ethylene carbonate, butylene carbonate, vinylene carbonate, ⁇ -butyrolactone, dimethyl carbonate, diethyl carbonate, methyl ethyl carbonate, 1,2-dimethoxyethane, 2-methyltetrahydrofuran, dimethyl sulfoxide, 1,3-dioxolane, formamide, dimethylformamide, methyl propionate, ethyl propionate, phosphoric acid triester, trimethoxymethane, dioxolane, diethyl ether, sulfolane, 3-methyl-2-oxazolidinone, tetrahydrofuran, 1,2-dioxane Ethoxyethane, chloroethylene carbonate, chloropropylene carbonate and the like can be used. Desirably, among these, it is preferable to use a high boiling cyclic compound as a solvent.
  • a solid electrolyte supported by a polymer such as ethylene oxide, acrylonitrile, vinylidene fluoride, methyl methacrylate, hexafluoropropylene or the like, an ionic liquid or the like may be used instead of the non-aqueous electrolytic solution.
  • an electrolyte other than LiPF 6 it may be used other electrolytes utilized in ordinary lithium ion secondary battery or the like.
  • electrolytes utilized in ordinary lithium ion secondary battery or the like.
  • a lithium salt such as an imide salt of lithium represented by lithium trifluoromethanesulfonimide can also be used as the electrolyte.
  • a polymer of ethylene oxide, acrylonitrile, vinylidene fluoride, methyl methacrylate, or hexafluoropropylene may be used as a gel electrolyte impregnated with a non-aqueous electrolyte.
  • the negative electrode member 3 occludes and releases lithium ions by using metal lithium as the negative electrode member 3, but the negative electrode member 3 occludes and releases ions of other metals May be
  • a metal such as Na, Ca, Mg, Zn, Al, or Fe as the negative electrode member 3
  • the negative electrode member 3 can occlude and release these ions.
  • binder 1c Although the example which used PVDF as the binder 1c was demonstrated in the said embodiment, you may use the other binder (binder) used by a general lithium ion secondary battery etc.
  • a fluorine-based resin such as polytetrafluoroethylene (PTFE), styrene butadiene rubber (SBR) or the like can be used as the binder 1c.
  • PTFE polytetrafluoroethylene
  • SBR styrene butadiene rubber
  • the separator 2 can be configured using a porous separator such as polypropylene or a glass ceramic having metal ion conductivity.
  • the form of a battery cell is not limited to this.
  • battery cells such as laminate type and cylindrical type can also be used. That is, as long as the reaction of the metal-air secondary battery can be confirmed, the present invention does not depend on the form of the battery cell.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Inert Electrodes (AREA)
  • Hybrid Cells (AREA)
  • Battery Electrode And Active Subsutance (AREA)

Abstract

In order to decrease charging overvoltage, this metal-air secondary battery is provided with a negative electrode member which occludes and releases metal ions, a positive electrode member which ionizes oxygen, and a separator impregnated with an electrolyte and arranged between the negative electrode member and the positive electrode member, and is characterized by the positive electrode member having 2nm or smaller pores, and by the ratio (B/A) of the product volume B, calculated from the discharge capacity of the secondary battery, and the volume A of said pores being 0.1 or less.

Description

金属空気二次電池Metal air secondary battery

 本発明は、充放電可能な金属空気二次電池に関するものである。 The present invention relates to a chargeable and dischargeable metal air secondary battery.

 近年、自動車業界においては、ガソリン等の燃料で駆動するエンジンを用いた従来の自動車に代わって、電気で駆動するモータをエンジンと併用するハイブリッド電気自動車(HEV)や、モータのみで駆動する電気自動車(EV)の開発が進められている。モータを用いたこれらの自動車(以下では単に電気自動車と総称する)の性能は、電気エネルギーの供給源である蓄電池の特性によって大きく左右される。そのため、優れた特性を有する蓄電池の開発が進められている。 In recent years, in the automobile industry, hybrid electric vehicles (HEVs) using an electrically driven motor in combination with an engine instead of a conventional automobile using an engine driven by fuel such as gasoline, and an electric vehicle driven only by a motor Development of (EV) is in progress. The performance of these motor vehicles (hereinafter simply referred to as electric vehicles) depends largely on the characteristics of the storage battery, which is a source of electrical energy. Therefore, development of a storage battery having excellent characteristics is in progress.

 リチウムイオン二次電池は、他の従来の二次電池と比べて軽量かつ高出力という特徴を有していることから、電気自動車をはじめとする他の様々な装置に搭載される蓄電池において広く利用されている。現在、実際に得られているリチウムイオン二次電池の重量エネルギー密度は約100Wh/kg程度であり、その理論的な上限は400Wh/kg程度であると考えられている。しかし、電気自動車の本格的な普及のためにはさらなる大容量の蓄電池が求められており、少なくとも500Wh/kg程度の重量エネルギー密度が必要であるとも言われている。そのため、リチウムイオン二次電池よりも大きな重量エネルギー密度が期待できる革新型電池の開発が求められている。 Lithium ion secondary batteries are characterized by their light weight and high output compared to other conventional secondary batteries, and are widely used in storage batteries mounted in various other devices including electric vehicles. It is done. At present, the weight energy density of the lithium ion secondary battery actually obtained is about 100 Wh / kg, and the theoretical upper limit thereof is considered to be about 400 Wh / kg. However, for the full-scale spread of electric vehicles, a storage battery with a further large capacity is required, and it is also said that a weight energy density of at least about 500 Wh / kg is required. Therefore, there is a demand for development of an innovative battery that can be expected to have a greater weight energy density than a lithium ion secondary battery.

 リチウムイオン二次電池の重量エネルギー密度を制約している要因の1つに、コバルト酸リチウムに代表される含リチウム遷移金属酸化物を正極材料に用いていることがある。すなわち、その構成元素である遷移金属元素は重金属であるため、これを正極材料として蓄電池に組み込むと重量が増加し、結果として重量エネルギー密度が小さくなってしまう。そこで、こうした制約を避けるため、正極材料に大気中の酸素を利用し、負極材料に金属を利用する金属空気電池が近年注目されている。金属空気電池を蓄電池として用いて電力貯蔵を行うと、従来のリチウムイオン電池と比べて重量を低減することができるため、コスト低減が見込める。 One of the factors limiting the weight energy density of the lithium ion secondary battery is that a lithium-containing transition metal oxide represented by lithium cobaltate is used as a positive electrode material. That is, since the transition metal element which is the constituent element is a heavy metal, when it is incorporated into a storage battery as a positive electrode material, the weight increases and as a result, the weight energy density decreases. Therefore, in order to avoid such limitations, metal-air batteries that use oxygen in the air as the positive electrode material and metal in the negative electrode material have recently attracted attention. When power storage is performed using a metal-air battery as a storage battery, the weight can be reduced as compared with a conventional lithium ion battery, and therefore, cost reduction can be expected.

 従来、亜鉛を用いた金属空気電池が実用化されており、補聴器の電源等に使用されている。しかし、これまでの金属空気電池は一次電池としての実用化に留まっており、充放電可能な二次電池としての実用化は未だなされていない。 Conventionally, metal-air batteries using zinc have been put to practical use and used as a power source for hearing aids and the like. However, the metal-air battery so far has remained in practical use as a primary battery, and has not been put into practical use as a chargeable / dischargeable secondary battery.

 従来の金属空気電池の二次電池化を阻む大きな理由としては、充放電エネルギー効率が低いことが挙げられ、この主要因は充電電圧が高いためである。これに関連して、以下のような技術が特許文献1に開示されている。 A major reason for preventing the conventional metal-air battery from becoming a secondary battery is that the charge / discharge energy efficiency is low, and this is mainly because the charge voltage is high. In relation to this, Patent Document 1 discloses the following technology.

 特許文献1には、リチウム空気電池において、アルカリ金属またはアルカリ土類金属と、遷移金属と、酸素を有する複合酸化物を触媒として用いる構成が開示されている。 Patent Document 1 discloses a configuration using a composite oxide having an alkali metal or an alkaline earth metal, a transition metal, and oxygen in a lithium-air battery as a catalyst.

 また、金属空気二次電池用に限定されるものではないが、炭素材料に関して下記の技術が特許文献2に開示されている。 Moreover, although it is not limited for metal air secondary batteries, the following technique is disclosed by patent document 2 regarding a carbon material.

特開2009-252638号公報JP, 2009-252638, A 特開2006-335596号公報JP 2006-335596 A

 特許文献1に開示される電池では、充電電圧が4.3V程度といぜんとして高く、そのために充放電エネルギー効率が低い。 In the battery disclosed in Patent Document 1, the charge voltage is as high as about 4.3 V, and the charge / discharge energy efficiency is therefore low.

 また、特許文献2に開示される炭素材料は、充電電圧の言及がない。 Moreover, the carbon material disclosed in Patent Document 2 does not mention the charging voltage.

 上記に鑑みて、本発明の目的は、充電過電圧を低減した金属空気二次電池を提供することにある。 In view of the above, it is an object of the present invention to provide a metal-air secondary battery with reduced charge overpotential.

 本発明による金属空気二次電池は、金属イオンを吸蔵・放出する負極部材と、酸素をイオン化する正極部材と、前記負極部材と前記正極部材との間に設置された電解質が含浸されているセパレータと、を有する金属空気二次電池において、前記正極部材は、2nm以下の細孔を有し、前記細孔の容積Aと、前記二次電池の放電容量から算出される生成物体積Bとの比(B/A)が0.1以下であることを特徴とする。 A metal-air secondary battery according to the present invention comprises a negative electrode member for absorbing and releasing metal ions, a positive electrode member for ionizing oxygen, and a separator impregnated with an electrolyte disposed between the negative electrode member and the positive electrode member. And in the metal-air secondary battery, the positive electrode member has pores of 2 nm or less, and a volume A of the pores and a product volume B calculated from the discharge capacity of the secondary battery. It is characterized in that the ratio (B / A) is 0.1 or less.

 本発明によれば、金属空気二次電池における充電過電圧の低減を達成することができる。 According to the present invention, it is possible to achieve a reduction in charge over voltage in a metal-air secondary battery.

本発明の一実施形態による金属空気二次電池の断面を示す模式図である。It is a schematic diagram which shows the cross section of the metal air secondary battery by one Embodiment of this invention. 本発明の一実施形態による金属空気二次電池の正極部材の構成を示す模式図である。It is a schematic diagram which shows the structure of the positive electrode member of the metal air secondary battery by one Embodiment of this invention.

 以下に図面および表を用いて、本発明の一実施形態による金属空気二次電池について説明する。図1は、本発明の一実施形態による金属空気二次電池の断面を示す模式図である。この金属空気二次電池は、負極に金属リチウム(Li)を使用した継手構造の電池セルを有するリチウム空気二次電池である。 A metal-air secondary battery according to an embodiment of the present invention will be described below using the drawings and tables. FIG. 1 is a schematic view showing a cross section of a metal air secondary battery according to an embodiment of the present invention. This metal air secondary battery is a lithium air secondary battery having a battery cell of a joint structure using metal lithium (Li) for the negative electrode.

 図1に示す金属空気二次電池では、正極部材1と負極部材3とが電解液を含浸させたセパレータ2を間に挟んで配置されており、これらが1つの電池セルを構成している。負極部材3の周囲にはOリング4が配置されている。この電池セルは、押さえ板5が締め付けバネ7から受ける締め付け力により、押さえ板5と集電体6の間に挟まれた状態で固定されている。集電体6と酸素封入弁8の間には、正極活物質として作用する酸素ガスが封入されている。 In the metal air secondary battery shown in FIG. 1, the positive electrode member 1 and the negative electrode member 3 are disposed with the separator 2 impregnated with the electrolytic solution interposed therebetween, and these constitute one battery cell. An O-ring 4 is disposed around the negative electrode member 3. The battery cell is fixed in a state of being held between the pressure plate 5 and the current collector 6 by the clamping force that the pressure plate 5 receives from the clamping spring 7. An oxygen gas acting as a positive electrode active material is enclosed between the current collector 6 and the oxygen filling valve 8.

 負極部材3は、セパレータ2に含浸されている電解液との間で金属イオンを吸蔵および放出するものである。本実施形態では、直径8mm、厚さ1mmの円板状の金属リチウムを負極部材3として使用した。この負極部材3の電極面積は、セパレータ2に接する部分の金属リチウムの面積として定義することができ、約0.5cm2である。また、セパレータ2には、負極部材3よりも大きな直径13mmの円板状のポリエチレンを使用した。 The negative electrode member 3 occludes and releases metal ions with the electrolytic solution impregnated in the separator 2. In the present embodiment, disc-shaped metallic lithium having a diameter of 8 mm and a thickness of 1 mm was used as the negative electrode member 3. The electrode area of the negative electrode member 3 can be defined as the area of metal lithium in a portion in contact with the separator 2 and is about 0.5 cm 2 . Further, for the separator 2, disk-shaped polyethylene having a diameter of 13 mm larger than that of the negative electrode member 3 was used.

 正極部材1は、正極活物質である酸素をイオン化するものである。 The positive electrode member 1 ionizes oxygen which is a positive electrode active material.

 図1の金属空気二次電池では、放電時において、以下の式(1)~(3)で表される放電反応が行われる。 In the metal-air secondary battery of FIG. 1, a discharge reaction represented by the following formulas (1) to (3) is performed at the time of discharge.

 (負極側)2Li→2Li++2e-       --- (1)
 (正極側)O2+2Li++2e-→Li22    --- (2)
 (全反応)2Li+O2→Li22        --- (3)
(Negative electrode) 2Li → 2Li + + 2e - --- (1)
(Positive side) O 2 + 2Li + + 2e - → Li 2 O 2 --- (2)
(All reactions) 2Li + O 2 → Li 2 O 2 --- (3)

 一方、充電時においては、以下の式(4)~(6)で表される充電反応が行われる。 On the other hand, at the time of charging, charge reactions represented by the following formulas (4) to (6) are performed.

 (負極側)2Li←2Li++2e-       --- (4)
 (正極側)O2+2Li++2e-←Li22    --- (5)
 (全反応)2Li+O2←Li22        --- (6)
(Negative electrode) 2Li ← 2Li + + 2e - --- (4)
(Positive side) O 2 + 2Li + + 2e - ← Li 2 O 2 --- (5)
(All reactions) 2Li + O 2 ← Li 2 O 2 --- (6)

 図2は、正極部材1の構成を示す模式図である。図2に示すように、正極部材1は、触媒1b、バインダ1cおよび担体1dを混合し、これを基材1aに塗布することによって構成される。本実施形態では、触媒1b、バインダ1cおよび担体1dを、それぞれ5:4:1の重量比で混合し、これを基材1aに塗布して正極部材1とした。 FIG. 2 is a schematic view showing the configuration of the positive electrode member 1. As shown in FIG. 2, the positive electrode member 1 is configured by mixing a catalyst 1b, a binder 1c and a support 1d and applying the mixture to a substrate 1a. In the present embodiment, the catalyst 1 b, the binder 1 c, and the carrier 1 d are mixed in a weight ratio of 5: 4: 1, respectively, and the mixture is applied to the substrate 1 a to form the positive electrode member 1.

 基材1aは、正極部材1を主に構成する導電性の物質であり、たとえば炭素や金属などが用いられる。基材1aとしては、比表面積が大きく(たとえば100m2/g以上)、かつ電気伝導性が高いものが好ましい。たとえば、活性炭や金属多孔質体などを基材1aとして用いることができる。 The base material 1a is a conductive substance mainly constituting the positive electrode member 1, and for example, carbon, metal or the like is used. As the substrate 1a, a substrate having a large specific surface area (for example, 100 m 2 / g or more) and high electric conductivity is preferable. For example, activated carbon or a metal porous body can be used as the substrate 1a.

 触媒1bは、正極側における上記の式(2)の反応や式(5)の反応を助け、これにより放電電圧を向上させると共に充電電圧を低下させる機能を有する粉末状の物質である。 The catalyst 1 b is a powdery substance having a function of assisting the reaction of the formula (2) or the reaction of the formula (5) on the positive electrode side to thereby improve the discharge voltage and reduce the charge voltage.

 担体1dは、触媒1bを基材1aに担持する機能を有しており、バインダ1cは、基材1a、触媒1bおよび担体1dを互いに結着させる機能を有する。なお、触媒1b、バインダ1c、担体1dとして用いられる物質の詳細については、後述する各実施例においてそれぞれ説明する。 The support 1d has a function of supporting the catalyst 1b on the base 1a, and the binder 1c has a function of binding the base 1a, the catalyst 1b and the support 1d to each other. The details of the substances used as the catalyst 1b, the binder 1c, and the carrier 1d will be described in the respective examples described later.

 なお、正極部材1の大きさは、前述のセパレータ2よりも小さく、かつ負極部材3よりも大きくすることが好ましい。すなわち、セパレータ2が最も大きく、正極部材1、負極部材3の順に小さくなるように、これらの大きさを設定することができる。 The size of the positive electrode member 1 is preferably smaller than that of the separator 2 described above and larger than that of the negative electrode member 3. That is, these sizes can be set so that the separator 2 is the largest and becomes smaller in the order of the positive electrode member 1 and the negative electrode member 3.

 セパレータ2には、LiPF6を電解質とする電解液が含浸されている。この電解液には、1モルのLiPF6を非水溶媒であるプロピレンカーボネートに溶かしたものを使用した。正極部材1の表面と負極部材3の表面に電解液をそれぞれ数滴程度ずつ滴下した後、これらの表面を内側にして正極部材1と負極部材3の間にセパレータ2を挟み込むことで、電解液をセパレータ2に含浸させた。 The separator 2 is impregnated with an electrolytic solution using LiPF 6 as an electrolyte. As this electrolyte, one in which 1 mol of LiPF 6 was dissolved in propylene carbonate which is a non-aqueous solvent was used. After several drops of an electrolytic solution are dropped on the surface of the positive electrode member 1 and the surface of the negative electrode member 3 respectively, the separator 2 is sandwiched between the positive electrode member 1 and the negative electrode member 3 with these surfaces inside. The separator 2 was impregnated with

 集電体6は、厚さ1mmのステンレス鋼製メッシュである。なお、前述のように正極部材1において基材1aを金属多孔質体とした場合は、これを集電体6と兼用することも可能である。 The current collector 6 is a stainless steel mesh having a thickness of 1 mm. In addition, when the base material 1a is made into a metal porous body in the positive electrode member 1 as mentioned above, it is also possible to use this as the current collector 6.

 押さえ板5はステンレス鋼製であり、締め付けバネ7から受ける締め付け力に応じて、負極部材3およびOリング4をセパレータ2の方向に加勢する。これにより、負極部材3、セパレータ2および正極部材1が互いに密着される構造とした。 The pressure plate 5 is made of stainless steel, and urges the negative electrode member 3 and the O-ring 4 in the direction of the separator 2 in accordance with the tightening force received from the tightening spring 7. Thus, the negative electrode member 3, the separator 2 and the positive electrode member 1 are in close contact with each other.

 本実施形態では、酸素封入弁8を開け、濃度99.9%の酸素ガスを500ml/分の流量で10~15分程度流すことで、集電体6の外側から電池セルの内部に流入させた。その後、酸素封入弁8を閉じることで、電池セルの内部に酸素ガスを封入した。 In this embodiment, the oxygen filling valve 8 is opened, and oxygen gas having a concentration of 99.9% is flowed at a flow rate of 500 ml / min for about 10 to 15 minutes to flow into the battery cell from the outside of the current collector 6. The Thereafter, by closing the oxygen filling valve 8, oxygen gas was filled in the battery cell.

 なお、以上説明したような金属空気二次電池の組み立ては、グローブボックス内で行った。 In addition, the assembly of the metal air secondary battery as described above was performed in a glove box.

 次に、触媒1b、バインダ1cおよび担体1dの詳細について説明する。本実施形態では、触媒1bとして二酸化マンガン(MnO2)を、担体1dとしてカーボンを、バインダ1cとしてポリフッ化ビニリデン(PVDF)をそれぞれ使用した。また、担体1dとしては、カーボンを用いた。その具体例を、実施例1~7、比較例1として、表1を基に以下に説明する。表1は、本発明の実施例1~7および比較例1に用いた材料と、平均充電電圧の一覧を示している。 Next, details of the catalyst 1b, the binder 1c, and the carrier 1d will be described. In this embodiment, manganese dioxide (MnO 2 ) is used as the catalyst 1b, carbon is used as the carrier 1d, and polyvinylidene fluoride (PVDF) is used as the binder 1c. In addition, carbon was used as the carrier 1d. Specific examples thereof will be described below based on Table 1 as Examples 1 to 7 and Comparative Example 1. Table 1 shows a list of materials used in Examples 1 to 7 of the present invention and Comparative Example 1 and an average charging voltage.

Figure JPOXMLDOC01-appb-T000001
Figure JPOXMLDOC01-appb-T000001

(実施例1)
 実施例1では、担体1dとして、総細孔容積が15.8mL/g(ここでgは担体の重量を示す。以下同様)、2nm以下のミクロ細孔容積が0.499mL/gのものを用いて正極部材1を構成した。
Example 1
In Example 1, as the carrier 1d, one having a total pore volume of 15.8 mL / g (wherein g represents the weight of the carrier, and the same applies hereinafter) and a micropore volume of 2 nm or less of 0.499 mL / g The positive electrode member 1 was configured using.

(実施例2~7)
 実施例2~7では、それぞれ表1に示す担体1dを用いて同様に正極部材1を構成した。
(Examples 2 to 7)
In Examples 2 to 7, the positive electrode member 1 was similarly configured using the carrier 1d shown in Table 1.

(比較例1)
 比較例1では、実施例7に示した担体1dと同じ材料で正極部材1を構成した。
(Comparative example 1)
In Comparative Example 1, the positive electrode member 1 was formed of the same material as the carrier 1 d shown in Example 7.

 次に、本実施形態による金属空気二次電池を使用した充放電評価の実験結果について説明する。本実施形態では、上記実施例1~7および比較例1による各金属空気二次電池を使用して、次のような充放電評価の実験を行った。 Next, experimental results of charge / discharge evaluation using the metal-air secondary battery according to the present embodiment will be described. In the present embodiment, using the metal air secondary batteries according to the above-described Examples 1 to 7 and Comparative Example 1, experiments of charge / discharge evaluation as follows were conducted.

 ここでは、充放電条件として、前述のように電極面積を0.5cm2としたときに、放電時は0.1mA/cm2の定電流放電を行い、充電時は0.02mA/cm2の定電流充電を行った。この時、充電時の平均電圧をそれぞれ測定し、表1に平均充電電圧として示した。 Here, as charge and discharge condition, when a 0.5 cm 2 of electrode area, as described above, when discharging a constant current discharge of 0.1 mA / cm 2, during charging of 0.02 mA / cm 2 Constant current charging was performed. At this time, the average voltage at the time of charge was measured, and is shown in Table 1 as an average charge voltage.

 なお、実験では、実施例1~7および比較例1の各金属空気二次電池を端子付きデシケータ内にそれぞれ設置し、デシケータの内部にアルゴンガスを封入した後、デシケータの外側端子を充放電評価装置に取り付けて測定を行った。 In the experiment, each metal air secondary battery of each of Examples 1 to 7 and Comparative Example 1 was placed in a terminal-equipped desiccator, and after argon gas was sealed in the inside of the desiccator, charge / discharge evaluation of the outer terminal of the desiccator It attached to the device and measured.

 本実験により得られた平均充電電圧を表1に示す。この表のとおり、平均充電電圧は、2nm以下の細孔容積と、生成物体積占有比率が10%を超えると上昇し、4Vになることが分かった。 The average charging voltage obtained by this experiment is shown in Table 1. As shown in the table, it was found that the average charge voltage increased to 4 V when the pore volume of 2 nm or less and the product volume occupancy ratio exceeded 10%.

 また、平均充電電圧は2nm以下の細孔容積/総細孔容積の比率が少なくとも15%以上であれば充電電圧が低いことがわかった。 In addition, it was found that the charge voltage is low when the ratio of pore volume / total pore volume at an average charge voltage of 2 nm or less is at least 15% or more.

 この結果は次のように考えられる。 The result is considered as follows.

 2nm以下の細孔が多いほど、絶縁物であるLi22が析出する大きさが小さいため、充電時に分解がしやすいと考えられる。しかし今回の結果は、実施例で示すように、我々の研究によれば、2nm以下の細孔容積に占める生成物体積の比が、ある一定以上になると充電過電圧が上昇することを初めて見出した。このような知見は、特開2006-335596号公報に示すような、2nm以下の細孔が総細孔容積の90%以上であるような材料であっても、金属空気二次電池として充電過電圧を下げるためには、生成物の量、つまり、放電容量を規制しなければならない。 As the number of pores having a size of 2 nm or less increases, the size at which Li 2 O 2, which is an insulator, is deposited is smaller, so it is considered that decomposition is likely to occur during charging. However, as shown in the examples, according to our study, we have found for the first time that the charge overpotential rises when the ratio of the product volume to the pore volume of 2 nm or less becomes a certain level or more. . Such a finding is considered to be a charge over voltage as a metal-air secondary battery, even in a material whose pores of 2 nm or less are 90% or more of the total pore volume as shown in JP-A-2006-335596. In order to reduce the amount of product, the amount of product, ie, the discharge capacity, must be regulated.

 以上説明したような本実験結果により、担体1dの細孔容積と、放電容量で定義される生成物体積の比を規定することで、充電過電圧が低い金属空気二次電池を提供することができる。 By defining the ratio of the pore volume of the carrier 1d and the product volume defined by the discharge capacity according to the experimental results as described above, it is possible to provide a metal air secondary battery with a low charge overpotential. .

 以上説明した実施の形態によると、金属空気二次電池は、リチウムイオンを吸蔵および放出する負極部材3と、酸素をイオン化する正極部材1と、負極部材3と正極部材1の間に配置されたセパレータ2に含浸された電解質とを備え、前記正極部材の細孔容積Aと、前記金属空気二次電池の最大放電容量x(Ah)から算出される生成物体積Bにおいて、B/A比を一定値以下にするようにxを制御して用いることを特徴としたので、金属空気二次電池における充電過電圧の低減を達成することができる。 According to the embodiment described above, the metal-air secondary battery is disposed between the negative electrode member 3 for absorbing and releasing lithium ions, the positive electrode member 1 for ionizing oxygen, the negative electrode member 3 and the positive electrode member 1. In the product volume B calculated from the pore volume A of the positive electrode member and the maximum discharge capacity x (Ah) of the metal-air secondary battery, the B / A ratio is provided. Since x is controlled and used so as to be equal to or less than a predetermined value, it is possible to achieve the reduction of the charge over voltage in the metal-air secondary battery.

 特に、実施例1~7に示すように、細孔は2nm以下の細孔を有し、その細孔容積と最大放電容量から算出される生成物体積の比が0.1以下であると充電電圧を低減できる。ここで、2nm以下の細孔は、BET法で測定したもので定義される。 In particular, as shown in Examples 1 to 7, the pores have pores of 2 nm or less, and charging is performed when the ratio of the product volume calculated from the pore volume to the maximum discharge capacity is 0.1 or less. The voltage can be reduced. Here, the pore of 2 nm or less is defined by the BET method.

 また、実施例1~7に示すように、2nm以下の細孔容積と、総細孔容積の比が少なくとも15%以上あることで、充電電圧を低減できる。 Further, as shown in Examples 1 to 7, when the ratio of the pore volume of 2 nm or less to the total pore volume is at least 15% or more, the charge voltage can be reduced.

 さらに実施例1~7に示したように、担体1dとして炭素を用いているが、これに限定されるものではなく、導電性材料、例えば、アルミ、ニッケル、SUSなどであってもよい。これらの導電性材料は、それ自身が細孔を有してもよいし、粉末を固めて正極部材を形成することで細孔を形成してもかまわない。 Furthermore, as shown in Examples 1 to 7, although carbon is used as the carrier 1d, the present invention is not limited to this, and a conductive material such as aluminum, nickel, SUS or the like may be used. These conductive materials may themselves have pores, or may be formed by solidifying powder to form a positive electrode member.

 なお、以上説明した実施の形態では、実施例1~7、および比較例1において触媒1bとしてMnO2を用いた例を示したが、本発明の骨子は担体1dに関するものであるため、触媒にはPtなどの貴金属触媒や、酸化物などの一般に用いられるものでもよい。 In the embodiment described above, although the examples using MnO 2 as the catalyst 1b in the examples 1 to 7 and the comparative example 1 are shown, since the main point of the present invention relates to the carrier 1d, May be a commonly used noble metal catalyst such as Pt or an oxide.

 また、以上説明した実施の形態では、LiPF6を電解質とし、プロピレンカーボネートを溶媒とした電解液をセパレータ2に含浸させて用いた例を説明したが、一般的なリチウムイオン電池等で利用される他の非水系電解液を用いてもよい。すなわち、プロピレンカーボネート以外の溶媒として、たとえばエチレンカーボネート、ブチレンカーボネート、ビニレンカーボネート、γ-ブチロラクトン、ジメチルカーボネート、ジエチルカーボネート、メチルエチルカーボネート、1,2-ジメトキシエタン、2-メチルテトラヒドロフラン、ジメチルスルフォキシド、1,3-ジオキソラン、ホルムアミド、ジメチルホルムアミド、プロピオン酸メチル、プロピオン酸エチル、リン酸トリエステル、トリメトキシメタン、ジオキソラン、ジエチルエーテル、スルホラン、3-メチル-2-オキサゾリジノン、テトラヒドロフラン、1,2-ジエトキシエタン、クロルエチレンカーボネート、クロルプロピレンカーボネート等を用いることができる。望ましくは、これらのうち高沸点の環状化合物を溶媒として用いることが好ましい。 In the embodiment described above, an example was described in which the separator 2 was impregnated with an electrolytic solution using LiPF 6 as the electrolyte and propylene carbonate as the solvent, but it is used in general lithium ion batteries and the like. Other non-aqueous electrolytes may be used. That is, as solvents other than propylene carbonate, for example, ethylene carbonate, butylene carbonate, vinylene carbonate, γ-butyrolactone, dimethyl carbonate, diethyl carbonate, methyl ethyl carbonate, 1,2-dimethoxyethane, 2-methyltetrahydrofuran, dimethyl sulfoxide, 1,3-dioxolane, formamide, dimethylformamide, methyl propionate, ethyl propionate, phosphoric acid triester, trimethoxymethane, dioxolane, diethyl ether, sulfolane, 3-methyl-2-oxazolidinone, tetrahydrofuran, 1,2-dioxane Ethoxyethane, chloroethylene carbonate, chloropropylene carbonate and the like can be used. Desirably, among these, it is preferable to use a high boiling cyclic compound as a solvent.

 さらに、エチレンオキシド、アクリロニトリル、フッ化ビニリデン、メタクリル酸メチル、ヘキサフルオロプロピレンなどの高分子に保持させた固体電解質や、イオン液体などを、非水系電解液の代わりに使用してもよい。 Furthermore, a solid electrolyte supported by a polymer such as ethylene oxide, acrylonitrile, vinylidene fluoride, methyl methacrylate, hexafluoropropylene or the like, an ionic liquid or the like may be used instead of the non-aqueous electrolytic solution.

 また、LiPF6以外の電解質として、一般的なリチウムイオン二次電池等で利用される他の電解質を用いてもよい。たとえば、LiBF4、LiClO4、LiCF3SO3、LiCF3CO2、LiAsF6、LiSbF6、LiTFSIなどを電解質として用いることができる。あるいは、リチウムトリフルオロメタンスルホンイミドで代表されるリチウムのイミド塩などのようなリチウム塩を電解質として用いることもできる。 Further, as an electrolyte other than LiPF 6, it may be used other electrolytes utilized in ordinary lithium ion secondary battery or the like. For example, can be used as LiBF 4, LiClO 4, LiCF 3 SO 3, LiCF 3 CO 2, LiAsF 6, LiSbF 6, LiTFSI such an electrolyte. Alternatively, a lithium salt such as an imide salt of lithium represented by lithium trifluoromethanesulfonimide can also be used as the electrolyte.

 また、エチレンオキシド、アクリロニトリル、フッ化ビニリデン、メタクリル酸メチル、ヘキサフルオロプロピレンの高分子に、非水電解液を含浸させたゲル電解質を使用してもよい。 Alternatively, a polymer of ethylene oxide, acrylonitrile, vinylidene fluoride, methyl methacrylate, or hexafluoropropylene may be used as a gel electrolyte impregnated with a non-aqueous electrolyte.

 上記実施の形態では、負極部材3として金属リチウムを用いることにより、負極部材3がリチウムイオンを吸蔵および放出する例を説明したが、他の金属によるイオンを負極部材3が吸蔵および放出するようにしてもよい。たとえば、Na、Ca、Mg、Zn、Al、Fe等の金属を負極部材3として用いることで、これらのイオンを負極部材3が吸蔵および放出することができる。 In the above embodiment, an example is described in which the negative electrode member 3 occludes and releases lithium ions by using metal lithium as the negative electrode member 3, but the negative electrode member 3 occludes and releases ions of other metals May be For example, by using a metal such as Na, Ca, Mg, Zn, Al, or Fe as the negative electrode member 3, the negative electrode member 3 can occlude and release these ions.

 上記実施の形態では、バインダ1cとしてPVDFを用いた例を説明したが、一般的なリチウムイオン二次電池等で利用される他のバインダ(結着材)を用いてもよい。たとえば、ポリテトラフルオロエチレン(PTFE)などのフッ素系樹脂や、スチレンブタジエンゴム(SBR)などをバインダ1cとして用いることができる。 Although the example which used PVDF as the binder 1c was demonstrated in the said embodiment, you may use the other binder (binder) used by a general lithium ion secondary battery etc. For example, a fluorine-based resin such as polytetrafluoroethylene (PTFE), styrene butadiene rubber (SBR) or the like can be used as the binder 1c.

 上記実施の形態では、セパレータ2にポリエチレンを用いた例を説明したが、一般的なリチウムイオン二次電池等で利用される他の材料を用いてもよい。たとえば、ポリプロピレンなどの多孔質セパレータや、金属イオン導電性を有するガラスセラミックスなどを用いてセパレータ2を構成することができる。 Although the example which used polyethylene for the separator 2 was demonstrated in the said embodiment, you may use the other material utilized with a general lithium ion secondary battery etc. For example, the separator 2 can be configured using a porous separator such as polypropylene or a glass ceramic having metal ion conductivity.

 上記実施の形態では継手構造の電池セルを使用した例を説明したが、電池セルの形態はこれに限定されない。たとえば、ラミネート型、円筒型などの電池セルも使用可能である。すなわち、金属空気二次電池の反応が確認できるものであれば、本発明は電池セルの形態に依存しない。 Although the said embodiment demonstrated the example which used the battery cell of coupling structure, the form of a battery cell is not limited to this. For example, battery cells such as laminate type and cylindrical type can also be used. That is, as long as the reaction of the metal-air secondary battery can be confirmed, the present invention does not depend on the form of the battery cell.

1 正極部材
1a 基材
1b 触媒
1c バインダ
1d 担体
2 セパレータ
3 負極部材
4 Oリング
5 押さえ板
6 集電体
7 締め付けバネ
8 酸素封入弁
REFERENCE SIGNS LIST 1 positive electrode member 1 a base 1 b catalyst 1 c binder 1 d carrier 2 separator 2 negative electrode member 4 O ring 5 pressing plate 6 current collector 7 tightening spring 8 oxygen filled valve

Claims (5)

 金属イオンを吸蔵・放出する負極部材と、酸素をイオン化する正極部材と、前記負極部材と前記正極部材との間に設置された電解質が含浸されているセパレータと、を有する金属空気二次電池において、
 前記正極部材は、2nm以下の細孔を有し、
 前記細孔の容積Aと、前記二次電池の放電容量から算出される生成物体積Bとの比(B/A)が0.1以下であることを特徴とする金属空気二次電池。
A metal air secondary battery having a negative electrode member for absorbing and releasing metal ions, a positive electrode member for ionizing oxygen, and a separator impregnated with an electrolyte disposed between the negative electrode member and the positive electrode member ,
The positive electrode member has pores of 2 nm or less,
The metal air secondary battery, wherein the ratio (B / A) of the pore volume A to the product volume B calculated from the discharge capacity of the secondary battery is 0.1 or less.
 請求項1において、前記正極部材は、導電性材料であることを特徴とする金属空気二次電池。 The metal air secondary battery according to claim 1, wherein the positive electrode member is a conductive material.  請求項1において、前記正極部材の細孔は、BET法によって計測された2nm以下の細孔を有することを特徴とする金属空気二次電池。 The metal air secondary battery according to claim 1, wherein the pores of the positive electrode member have pores of 2 nm or less measured by a BET method.  請求項1において、前記正極部材の細孔において、2nm以下の細孔容積と、総細孔容積との比が15%以上であることを特徴とする金属空気二次電池。 The metal air secondary battery according to claim 1, wherein a ratio of a pore volume of 2 nm or less to a total pore volume in the pores of the positive electrode member is 15% or more.  請求項1において、前記負極部材は、Li、Na、Ca、Mg、Zn、Al、Feのいずれかの金属によるイオンを吸蔵および放出することを特徴とする金属空気二次電池。 The metal-air secondary battery according to claim 1, wherein the negative electrode member occludes and releases ions of any one of Li, Na, Ca, Mg, Zn, Al and Fe.
PCT/JP2013/061705 2012-05-30 2013-04-22 Metal-air secondary battery Ceased WO2013179807A1 (en)

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