WO2025215390A1 - Closed-type lithium-oxygen battery - Google Patents
Closed-type lithium-oxygen batteryInfo
- Publication number
- WO2025215390A1 WO2025215390A1 PCT/IB2024/000150 IB2024000150W WO2025215390A1 WO 2025215390 A1 WO2025215390 A1 WO 2025215390A1 IB 2024000150 W IB2024000150 W IB 2024000150W WO 2025215390 A1 WO2025215390 A1 WO 2025215390A1
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- WIPO (PCT)
- Prior art keywords
- active material
- electrode active
- closed
- material layer
- gel
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Classifications
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/05—Accumulators with non-aqueous electrolyte
- H01M10/052—Li-accumulators
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
- H01M4/131—Electrodes based on mixed oxides or hydroxides, or on mixtures of oxides or hydroxides, e.g. LiCoOx
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/90—Selection of catalytic material
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
Definitions
- the present invention relates to a closed-type lithium-oxygen battery.
- Lithium-oxygen batteries (lithium-oxygen secondary batteries) are known as a type of non-aqueous electrolyte secondary battery. These lithium-oxygen batteries have the highest theoretical energy density of all secondary batteries, including next-generation batteries, and are expected to offer battery performance with an energy density significantly exceeding that of current lithium-ion secondary batteries. However, sufficient capacity characteristics have yet to be achieved, and further improvements are currently required.
- Lithium-oxygen batteries are broadly divided into two types: those that use gaseous molecular oxygen ( O2 ) as the oxygen source, consume O2 during discharge, and generate O2 during charge (lithium-air batteries), and those that do not consume or generate O2 (narrowly defined lithium-oxygen batteries). Because the latter do not exchange O2 with the atmosphere, they can be constructed as sealed cells and can be called “closed-type lithium-oxygen batteries.”
- Japanese Patent Laid-Open Publication No. 2015-159098 discloses the above-mentioned closed-type lithium-oxygen battery.
- This document attempts to achieve a high capacity of the electrode active material by mechanochemically pulverizing a raw material composition containing lithium oxide ( Li2O ) as an electrode active material and a transition metal atom-containing oxide ( Co3O4 , etc. ) as a catalyst, while preventing atmospheric moisture, carbon dioxide, and the like from entering the cell as a closed-type battery.
- Li2O lithium oxide
- Co3O4 , etc. transition metal atom-containing oxide
- the present invention therefore aims to provide a means for improving the charge/discharge efficiency of closed-type lithium-oxygen batteries.
- FIG. 1 is a cross-sectional view schematically illustrating a stacked (flat) closed-type lithium oxygen battery according to one embodiment of the present invention.
- One embodiment of the present invention is a battery for a closed-type lithium-oxygen battery, comprising: an electrode in which an electrode active material layer containing a lithium oxide, a catalyst, and a gel-forming polymer is disposed on the surface of a current collector; and an electrolyte layer in which an electrolytic solution is impregnated in a separator disposed adjacent to the electrode, wherein the porosity of the electrode active material layer is x [%], the ratio of the volume of the gel-forming polymer to the volume of the electrode active material layer is y [%], and the liquid absorption rate of the gel-forming polymer with respect to the electrolytic solution is z [%], the relationship of the following formula (1) is satisfied: 0 ⁇ yz/x ⁇ 8.7 Formula (1) In the course of searching for a means for improving the charge-discharge efficiency of a closed-type lithium-oxygen battery, the inventors discovered that incorporating a gel-forming polymer in addition to lithium oxide (Li 2 O) and a catalyst into the electrode active material layer
- FIG. 1 is a cross-sectional view schematically illustrating a stacked (flat) closed-type lithium-oxygen battery (hereinafter simply referred to as a "stacked-type lithium-oxygen battery”) according to one embodiment of the present invention.
- the term "closed-type lithium-oxygen battery” refers to a lithium-oxygen battery in which charge and discharge reactions proceed with the cell sealed (i.e., no exchange of molecular oxygen ( O2 ) with the atmosphere occurs during the charge and discharge reactions).
- O2 molecular oxygen
- This "closed-type lithium-oxygen battery” is disclosed in the above-mentioned Japanese Patent Application Laid-Open No. 2015-159098 as well as in a document such as (Wang, J.
- the present embodiment will be described taking as an example a case where the electrode according to the present embodiment is a positive electrode, the electrode can also be used as a negative electrode of a closed-type lithium-oxygen battery.
- the stacked lithium-oxygen battery 10a of this embodiment has a structure in which a substantially rectangular power-generating element 21, where the actual charge/discharge reaction takes place, is sealed inside a laminate film 29.
- the power-generating element 21 is configured by stacking a positive electrode, in which a positive electrode active material layer 13 is disposed on both sides of a positive electrode current collector 11', an electrolyte layer 17 made of a separator containing an electrolytic solution, and a negative electrode, in which a negative electrode active material layer 15 is disposed on both sides of a negative electrode current collector 12.
- the current collector has a function of mediating the transfer of electrons from the positive electrode active material layer and the negative electrode active material layer described later.
- the material constituting the current collector There are no particular limitations on the material constituting the current collector. For example, metals and conductive resins can be used as the material constituting the current collector.
- the electrode active material layer is disposed on the surface of the current collector and contains lithium oxide as an electrode active material, a catalyst, and a gel-forming polymer.
- the electrode active material layer is preferably a positive electrode active material layer from the viewpoint of more significant contribution to improving charge/discharge efficiency.
- the electrode active material (lithium oxide) functions as a positive electrode active material.
- Lithium oxide is a compound in which lithium and oxygen are covalently bonded, and there are several compounds depending on the atomic ratio.
- the lithium oxide preferably contains one or more selected from the group consisting of Li 2 O, LiO, Li 2 O 2 , and LiO 2.
- the lithium oxide contains Li 2 O, Li 2 O 2 , or LiO 2.
- the lithium oxide contains Li 2 O from the viewpoints of having a higher theoretical capacity and being chemically stable (less likely to decompose, and less reactivity with moisture and carbon dioxide in the air) compared to other lithium oxides.
- the electrode active material when the electrode is a positive electrode, conventionally known materials can be used as the negative electrode active material constituting the negative electrode.
- suitable negative electrode active materials include , for example, carbon materials such as graphite, soft carbon, hard carbon, lithium-transition metal composite oxides (for example, Li4Ti5O12 ), metal materials (tin , silicon), silicon-containing alloy-based negative electrode materials (for example , Si60Sn10Ti30 ), lithium alloy-based negative electrode materials (for example, lithium-tin alloy, lithium-silicon alloy, lithium-aluminum alloy, lithium-aluminum-manganese alloy, etc.).
- silicon-containing alloy-based negative electrode materials, carbon materials, lithium-transition metal composite oxides, and lithium alloy-based negative electrode materials are preferably used as the negative electrode active material.
- a catalyst is a substance that has the function of promoting the above-mentioned bonding/dissociation reaction between lithium oxide and oxygen by reducing the activation energy of these reactions. Any conventionally known compound can be used as a catalyst as long as it can exhibit this function.
- the catalyst is preferably a compound containing a transition metal (transition metal-containing compound).
- This transition metal-containing compound is preferably in the form of, for example, an oxide (including composite oxide), sulfide, halide, nitride, carbide, or the like containing the transition metal.
- the catalyst contains a transition metal-containing oxide.
- the transition metal is preferably at least one transition metal belonging to Groups 6 to 11 of the periodic table, more preferably one or more selected from the group consisting of cobalt, manganese, iron, nickel, molybdenum, iridium, and rhodium, particularly preferably one or more selected from the group consisting of cobalt, manganese, and iron, and most preferably cobalt.
- transition metal-containing compounds include transition metal-containing oxides such as cobalt oxide, manganese oxide, iron oxide, nickel oxide, molybdenum oxide, iridium oxide, and rhodium oxide.
- transition metal-containing oxides such as cobalt oxide, manganese oxide, iron oxide, nickel oxide, molybdenum oxide, iridium oxide, and rhodium oxide.
- cobalt oxide, manganese oxide, and iron oxide are preferred, and cobalt oxide (e.g., Co 3 O 4 ) is particularly preferred.
- the catalyst content in the electrode active material layer is not particularly limited, and although it depends on the type of lithium oxide and catalyst, it is preferably 50 to 500 mass%, more preferably 100 to 450 mass%, even more preferably 200 to 400 mass%, and especially preferably 250 to 350 mass%, relative to the total amount of lithium oxide (100 mass%) when the battery is fully discharged.
- the gel-forming polymer is an ion-conductive polymer, and can form a structure together with the electrode active material to play a role in ion conduction.
- the gel-forming polymer preferably contains at least one selected from the group consisting of polyethylene oxide (PEO), polypropylene oxide (PPO), polyethylene glycol (PEG), polyacrylonitrile (PAN), polyvinylidene fluoride (PVdF), polyvinylidene fluoride-hexafluoropropylene (PVdF-HEP), polymethyl methacrylate (PMMA), polyethylene glycol dimethacrylate, polyethylene glycol diacrylate, polypropylene glycol dimethacrylate, polypropylene glycol diacrylate, polymethyl methacrylate, and copolymers thereof.
- PEO polyethylene oxide
- PPO polypropylene oxide
- PEG polyethylene glycol
- PAN polyacrylonitrile
- PVdF polyvinylidene fluoride
- the gel-forming polymer is preferably selected from polyethylene oxide (PEO), polypropylene oxide (PPO), polyethylene glycol (PEG), polyacrylonitrile (PAN), polyvinylidene fluoride (PVdF), polyvinylidene fluoride-hexafluoropropylene copolymer (PVdF-HEP), and polymethyl methacrylate (PMMA).
- PEO polyethylene oxide
- PPO polypropylene oxide
- PEG polyethylene glycol
- PAN polyacrylonitrile
- PVdF polyvinylidene fluoride
- PVdF-HEP polyvinylidene fluoride-hexafluoropropylene copolymer
- PMMA polymethyl methacrylate
- the gel-forming polymer includes one containing a structural unit derived from vinylidene fluoride in the main chain (e.g., polyvinylidene fluoride (PVdF), polyvinylidene fluoride-hexafluoropropylene copolymer (PVdF-HEP), etc.).
- the gel-forming polymer includes polyvinylidene fluoride-hexafluoropropylene copolymer (PVdF-HEP).
- PVdF-HFP has high swelling properties in electrolytes, which can improve the ionic conductivity of lithium ions and the like in the electrode active material layer.
- PVdF-HFP is highly flexible, it can penetrate into the gaps between other components (electrode active materials, catalysts, conductive additives, etc.) contained in the electrode active material layer, improving their dispersibility. As a result, it is believed that electron conduction paths are well formed, enabling excellent charge/discharge efficiency.
- PVdF-HFP is not particularly limited as long as it is a copolymer of vinylidene fluoride and hexafluoropropylene.
- the lower limit of the proportion of hexafluoropropylene-derived structural units contained in PVdF-HFP, relative to the total structural units of PVdF-HFP, is preferably 4 mol% or more, more preferably 6 mol% or more, and even more preferably 6.5 mol% or more.
- the lower limit of the proportion of hexafluoropropylene-derived structural units contained in PVdF-HFP is preferably 20 mol% or less, more preferably 10 mol% or less, and even more preferably 8 mol% or less.
- the content of the gel-forming polymer in the electrode active material layer is not particularly limited, and although it depends on the type of lithium oxide and gel-forming polymer, it is preferably 10 to 100% by mass, more preferably 12 to 70% by mass, and even more preferably 15 to 60% by mass, relative to the total amount of the lithium oxide (100% by mass) when the battery is fully discharged.
- the electrode active material layer may further contain a binder other than the gel-forming polymer.
- binders include polyimide, styrene-butadiene rubber, carboxymethyl cellulose, polypropylene, polytetrafluoroethylene, polyacrylonitrile, and polyamide.
- the lower the content of these binders the better.
- the content of the gel-forming polymer relative to the total amount (100% by mass) of the binder is preferably 50% by mass or more, more preferably 80% by mass or more, even more preferably 90% by mass or more, particularly preferably 95% by mass or more, and most preferably 100% by mass.
- the electrode active material layer may further include a conductive additive.
- the conductive additive has a function of forming an electron conduction path (conductive passage) in the electrode active material layer. When such an electron conduction path is formed in the positive electrode active material layer, the internal resistance of the battery may be reduced and the rate characteristics may be improved.
- Conductive additives include particulate carbon materials such as acetylene black, carbon black, channel black, thermal black, and Ketjen Black (registered trademark), as well as fibrous carbon materials such as carbon nanotubes (single-walled carbon nanotubes and multi-walled carbon nanotubes), carbon nanofibers, vapor-grown carbon fibers, electrospun carbon fibers, polyacrylonitrile-based carbon fibers, and pitch-based carbon fibers.
- One type of conductive additive may be used alone, or two or more types may be used in combination.
- the content of the conductive additive in the electrode active material layer is preferably 15% by mass or less, more preferably 12% by mass or less, and even more preferably 10% by mass or less, relative to 100% by mass of the total solids content of the electrode active material layer.
- aggregation of the conductive additives is suppressed, resulting in favorable formation of electron conduction paths, thereby further improving charge/discharge efficiency.
- the conductive additive content is preferably greater than 0% by mass, and is preferably 1% by mass or more, more preferably 2% by mass or more, and even more preferably 3% by mass or more. At such a lower limit, sufficient conductive additive is present to form electron conduction paths, thereby further improving charge/discharge efficiency.
- each component lithium oxide, catalyst, gel-forming polymer, and optional conductive additive
- these components be present so that the lithium oxide and catalyst involved in the battery reaction are in contact with each other.
- the lithium oxide and catalyst are in the form of composite particles combined with a gel-forming polymer.
- "in the form of composite particles" of the lithium oxide and catalyst means that when a charge/discharge reaction is carried out in a closed-type lithium-oxygen battery, the particles do not collapse and maintain their particle shape even if the lithium oxide expands and contracts during charge/discharge. This configuration allows the charge/discharge reaction to proceed more smoothly when lithium oxide is used as an electrode material, which can effectively contribute to further improving the capacity characteristics of the battery.
- the battery according to this embodiment is characterized in that, when the porosity of the electrode active material layer is x [%], the volume ratio of the gel-forming polymer to the volume of the electrode active material layer is y [%], and the liquid absorption rate of the gel-forming polymer with respect to the electrolyte solution contained in the electrolyte layer is z [%], the battery satisfies formula (1): 0 ⁇ yz/x ⁇ 8.7.
- the inventors have found that there are appropriate ranges from the viewpoint of the charge/discharge efficiency of the battery among the porosity of the electrode active material layer (x), the volume ratio of the gel-forming polymer to the volume of the electrode active material layer (y), and the liquid absorption rate of the gel-forming polymer with respect to the electrolyte solution contained in the electrolyte layer (z), and have quantified this finding using the above relational formula.
- the flexibility of the gel-forming polymer suppresses the movement of the electrode active material and catalyst within the active material layer, effectively preventing their detachment.
- These mechanisms are thought to maintain the initial contact between the electrode active material and the catalyst even after repeated charge/discharge cycles, maintaining the initial capacity (i.e., improving charge/discharge efficiency).
- the above mechanism is merely speculative, and the accuracy of this mechanism does not affect the technical scope of the present invention.
- the value of yz/x preferably satisfies formula (2): 1.4 ⁇ yz/x ⁇ 8.7, more preferably formula (3): 3.2 ⁇ yz/x ⁇ 5.7, and even more preferably formula (4): 3.8 ⁇ yz/x ⁇ 4.8.
- formula (2) 1.4 ⁇ yz/x ⁇ 8.7
- formula (3) 3.2 ⁇ yz/x ⁇ 5.7
- formula (4) 3.8 ⁇ yz/x ⁇ 4.8.
- the gel-forming polymer exhibits better compliance with the contraction of the lithium oxide, thereby further improving charge-discharge efficiency.
- the values of x, y, and z are calculated using the method described in the Examples below.
- improved charge-discharge efficiency means that when a battery according to the present embodiment is constructed, the initial charge-discharge efficiency is improved compared to when a battery (comparative battery) having the same configuration except for not satisfying the specifications of the battery according to the present embodiment is constructed.
- the initial charge/discharge efficiency of the battery according to this embodiment is preferably 105 or more, more preferably 119 or more, even more preferably 125 or more, and particularly preferably 127 or more, when the initial charge/discharge efficiency of the comparative battery is taken as 100.
- the initial charge/discharge efficiency is measured using the method described in the Examples section below.
- the above x can be controlled by adjusting the particle size of the electrode active material, the amount of gel-forming polymer added, the thickness of the electrode active material layer, the pressing conditions during electrode fabrication, etc.
- the porosity (x) of the electrode active material layer preferably satisfies 25 ⁇ x ⁇ 70, more preferably 25 ⁇ x ⁇ 50, even more preferably 28 ⁇ x ⁇ 37, and particularly preferably 30 ⁇ x ⁇ 37.
- the above y can be controlled by adjusting the content of the gel-forming polymer in the electrode active material layer.
- the volume ratio (y) of the gel-forming polymer to the volume of the electrode active material layer preferably satisfies 7.0 ⁇ y ⁇ 15.0, more preferably 9.0 ⁇ y ⁇ 13.0, and even more preferably 10.5 ⁇ y ⁇ 12.5.
- the above z can be controlled by changing the type of gel-forming polymer and the composition of the electrolyte solution.
- the liquid absorption rate (z) of the gel-forming polymer preferably satisfies 10 ⁇ z ⁇ 100, and more preferably 12 ⁇ x ⁇ 50.
- the thickness of the electrode active material layer is typically about 1 to 1000 ⁇ m, preferably 20 to 800 ⁇ m, more preferably 30 to 500 ⁇ m, and even more preferably 40 to 200 ⁇ m.
- the thicker the electrode active material layer the more electrode active material can be retained to achieve sufficient capacity (energy density).
- the thinner the electrode active material layer the more improved the discharge rate characteristics can be.
- the electrolyte layer contains an electrolytic solution (liquid electrolyte) and preferably has a configuration in which a separator is impregnated with the electrolytic solution.
- the electrolyte functions as a carrier of lithium ions.
- the electrolyte has a form in which a lithium salt is dissolved in a non-aqueous solvent.
- the electrolyte is obtained by further adding a fluorine-containing carbonate to the non-aqueous solvent in which the lithium salt is dissolved.
- Preferred non-aqueous solvents are those that readily dissolve lithium salts, such as chain carbonates such as dimethyl carbonate (DMC), diethyl carbonate (DEC), dipropyl carbonate (DPC), methyl propyl carbonate (MPC), ethyl propyl carbonate (EPC), and methyl ethyl carbonate (MEC); fluorine-containing chain carbonates in which some of the hydrogen atoms of these chain carbonates have been replaced with fluorine atoms; ethylene carbonate (EC), propylene carbonate (PC), and butyl carbonate.
- chain carbonates such as dimethyl carbonate (DMC), diethyl carbonate (DEC), dipropyl carbonate (DPC), methyl propyl carbonate (MPC), ethyl propyl carbonate (EPC), and methyl ethyl carbonate (MEC)
- fluorine-containing chain carbonates in which some of the hydrogen atoms of these chain carbonates have been replaced with fluorine atom
- fluorine-containing cyclic carbonates in which some of the hydrogen atoms of these cyclic carbonates have been replaced with fluorine atoms; methyl propionate (MP), methyl acetate (MA), methyl formate (MF), 4-methyldioxolane (4MeDOL), dioxolane (DOL), 2-methyltetrahydrofuran (2MeTHF), tetrahydrofuran (THF), dimethoxyethane (DME), dimethyl sulfoxide (DMSO), and gamma-butyrolactone (GBL).
- MP methyl propionate
- MA methyl acetate
- MF methyl formate
- 4MeDOL 4-methyldioxolane
- DOL dioxolane
- 2MeTHF 2-methyltetrahydrofuran
- THF tetrahydrofuran
- DME dimethoxyethane
- DMSO dimethyl sulfoxide
- GBL gamma
- the non-aqueous solvent contains a chain carbonate, and it is even more preferable that it contains at least one selected from the group consisting of diethyl carbonate (DEC), ethyl methyl carbonate (EMC), and dimethyl carbonate (DMC).
- DEC diethyl carbonate
- EMC ethyl methyl carbonate
- DMC dimethyl carbonate
- lithium salts include Li( FSO2 ) 2N (lithium bis(fluorosulfonyl)imide; LiFSI ), Li ( C2F5SO2 ) 2N , LiPF6 , LiBF4 , LiClO4 , LiAsF6 , and LiCF3SO3 .
- the concentration of the lithium salt in the non-aqueous solvent is preferably 0.1 to 3.0 mol/L, and more preferably 0.8 to 2.2 mol/L.
- the electrolyte solution further contains a fluorine-containing carbonate, such as a fluorine-containing cyclic carbonate or a fluorine-containing chain carbonate.
- a fluorine-containing carbonate such as a fluorine-containing cyclic carbonate or a fluorine-containing chain carbonate.
- preferred fluorine-containing carbonates include fluorine-containing cyclic carbonates such as fluoroethylene carbonate (FEC), difluoroethylene carbonate, and 4-fluoropropylene carbonate; and fluorine-containing chain carbonates such as ethyl trifluoromethyl carbonate, 2,2,2-trifluoroethyl methyl carbonate, and bis(2,2,2-trifluoroethyl) carbonate.
- the content of the fluorine-containing carbonate is not particularly limited.
- the electrolyte solution contains 0.5 to 10 mass% of fluorine-containing carbonate, particularly fluoroethylene carbonate, based on the total amount of the finally obtained electrolyte solution. This makes it possible to achieve the above-mentioned effects more significantly.
- the electrolyte solution contains two or more types of fluorine-containing carbonates, it is preferable that the total amount thereof be within the above range.
- the electrolyte may further contain additives other than the components mentioned above.
- additives include vinylene carbonate, methyl vinylene carbonate, dimethyl vinylene carbonate, phenyl vinylene carbonate, diphenyl vinylene carbonate, ethyl vinylene carbonate, diethyl vinylene carbonate, vinyl ethylene carbonate, 1,2-divinyl ethylene carbonate, 1-methyl-1-vinyl ethylene carbonate, 1-methyl-2-vinyl ethylene carbonate, 1-ethyl-1-vinyl ethylene carbonate, and 1-ethyl-2-vinyl ethylene carbonate.
- additives examples include ethylene carbonate, vinyl vinylene carbonate, allyl ethylene carbonate, vinyloxymethyl ethylene carbonate, allyloxymethyl ethylene carbonate, acryloxymethyl ethylene carbonate, methacryloxymethyl ethylene carbonate, ethynyl ethylene carbonate, propargyl ethylene carbonate, ethynyloxymethyl ethylene carbonate, propargyloxyethylene carbonate, methylene ethylene carbonate, and 1,1-dimethyl-2-methylene ethylene carbonate.
- additives may be used alone or in combination of two or more. Furthermore, when an additive is used in the electrolyte, the amount used can be adjusted as appropriate.
- the separator constituting the electrolyte layer has the function of retaining the electrolyte to ensure lithium ion conductivity between the positive electrode and the negative electrode, and also functions as a partition wall between the positive electrode and the negative electrode.
- separator's form examples include a porous sheet separator made of polymer or fiber that absorbs and retains the electrolyte, and a nonwoven fabric separator.
- porous sheet separator made of a polymer or fiber for example, a microporous material (microporous membrane) can be used.
- a microporous material microporous membrane
- specific forms of the porous sheet made of polymer or fiber include microporous (microporous membrane) separators made of polyolefins such as polyethylene (PE) and polypropylene (PP); laminates of multiple layers of these (for example, a laminate with a three-layer structure of PP/PE/PP); hydrocarbon resins such as polyimide, aramid, and polyvinylidene fluoride-hexafluoropropylene (PVDF-HFP); and glass fibers.
- PE polyethylene
- PP polypropylene
- PVDF-HFP polyvinylidene fluoride-hexafluoropropylene
- Nonwoven fabric separators may be made from conventional materials such as cotton, rayon, acetate, nylon, polyester; polyolefins such as PP and PE; polyimide, and aramid, either alone or in combination.
- the thickness of the separator should be the same as that of the electrolyte layer, preferably 5 to 200 ⁇ m, and particularly preferably 10 to 100 ⁇ m.
- a separator with a heat-resistant insulating layer laminated on a porous substrate can be used.
- the heat-resistant insulating layer is a ceramic layer containing inorganic particles and a binder.
- the presence of a heat-resistant insulating layer alleviates the internal stress of the separator that increases with temperature rise, thereby suppressing thermal shrinkage. As a result, short circuits between battery electrodes can be prevented, resulting in a battery configuration that is less susceptible to performance degradation due to temperature rise.
- the presence of a heat-resistant insulating layer improves the mechanical strength of the separator with heat-resistant insulating layer, making it less likely to rupture. Furthermore, the heat-shrinkage suppression effect and high mechanical strength make the separator less likely to curl during the battery manufacturing process.
- the material constituting the current collector plates (25, 27) is not particularly limited, and known highly conductive materials conventionally used as current collector plates for lithium-ion secondary batteries can be used. Metal materials such as aluminum, copper, titanium, nickel, stainless steel (SUS), and alloys thereof are preferred as constituent materials of the current collector plates. From the viewpoints of light weight, corrosion resistance, and high conductivity, aluminum and copper are more preferred, and aluminum is particularly preferred.
- the positive electrode current collector plate 25 and the negative electrode current collector plate 27 may be made of the same material or different materials.
- the closed-type lithium-oxygen battery according to this embodiment has excellent charge/discharge efficiency. Therefore, the closed-type lithium-oxygen battery according to this embodiment is suitable for use as a power source for driving EVs and HEVs.
- the battery according to claim 1 having the characteristics of claim 2; the battery according to claim 1 or 2 having the characteristics of claim 3; the battery according to any one of claims 1 to 3 having the characteristics of claim 4; the battery according to any one of claims 1 to 4 having the characteristics of claim 5; the battery according to any one of claims 1 to 5 having the characteristics of claim 6; the battery according to claim 6 having the characteristics of claim 7; the battery according to any one of claims 1 to 7 having the characteristics of claim 8; the battery according to any one of claims 1 to 8 having the characteristics of claim 9; the battery according to any one of claims 1 to 9 having the characteristics of claim 10; and the battery according to any one of claims 1 to 10 having the characteristics of claim 11.
- the porosity (x) of the positive electrode active material layer was measured as follows: (1) The mass per unit area of the positive electrode active material layer was measured, and the mass of each material per unit area of the positive electrode active material layer was calculated from the compounding ratio of the materials. (2) The thickness [A] of the positive electrode active material layer was measured using a micrometer. (3) Using the mass of each material determined in (1) and the density of each material, the thickness [B] of the positive electrode active material layer when the porosity is 0% was calculated.
- the pore volume of the positive electrode active material layer was calculated from the difference (A-B) between the measured thickness of the positive electrode active material layer and the calculated thickness of the positive electrode active material layer, and the pore volume per 1 m3 of the positive electrode active material layer was determined. The percentage of the obtained value was defined as the porosity x [%].
- Example 1 (Preparation of positive electrode material) Lithium oxide (Li 2 O, manufactured by Kojundo Chemical Laboratory Co., Ltd.) as the positive electrode active material (lithium oxide) and cobalt oxide (Co 3 O 4 , manufactured by Kojundo Chemical Laboratory Co., Ltd.) as the catalyst were placed in a separate 70 mL planetary ball mill pot and each was ground using a planetary ball mill (grinding conditions: 40 g of 3 mm diameter zirconia balls and 15 g of 15 mm diameter zirconia balls at a rotation speed of 400 rpm for 1 hour).
- NMP N-methyl-2-pyrrolidone
- the resulting NMP solution of PVdF-HFP was mixed with the ball mill mixture of lithium oxide and cobalt oxide and the conductive additive acetylene black (AB) (Li-400, manufactured by Denka Co., Ltd., average primary particle size: 48 nm, aspect ratio: 1), and further mixed using the mixer/kneader (kneading conditions: 2000 rpm for 5 minutes).
- the resulting mixture was transferred to a metal tray and placed on a hot plate heated to 120°C to volatilize the NMP.
- the remaining powder was then collected and mixed by hand in an agate mortar for 5 minutes to prepare the positive electrode material of Example 1.
- the mixture ratio (mass ratio) of lithium oxide:cobalt oxide:acetylene black:PVdF-HFP was 20:60:10:10.
- NMP was added to the positive electrode material prepared above to adjust the solid content to 25% by mass, and the viscosity was adjusted to prepare a positive electrode slurry.
- the positive electrode slurry was uniformly applied to aluminum foil placed on a smooth plate using a doctor blade so that the final thickness of the positive electrode active material layer was 200 ⁇ m.
- the resulting laminate was then dried for 30 minutes on a hot plate heated to 80°C, and then pressed using a roll press.
- the laminate was then transferred to a vacuum dryer and dried under vacuum at 130°C for 8 hours to prepare a positive electrode of this example in which a positive electrode active material layer was formed on the surface of the aluminum foil.
- the porosity (x) of the positive electrode active material layer was 28%.
- EC ethylene carbonate
- DEC diethyl carbonate
- LiPF 6 lithium hexafluorophosphate
- Examples 2 to 4 The closed-type lithium-oxygen batteries (coin cells) of these Examples were produced using the same method as in Example 1 described above, except that the conditions for the pressing treatment were changed so that the porosity (x [%]) of the positive electrode active material layer and the volume ratio (y [%]) of the gel-forming polymer to the volume of the positive electrode active material layer were the values shown in Table 1 below.
- Example 5 The closed-type lithium-oxygen battery (coin cell) of this example was produced using the same method as in Example 1 described above, except that the amounts of the positive electrode active material (lithium oxide) and the catalyst (cobalt oxide) used were changed to the values shown in Table 1 below, and the conditions of the pressing treatment were changed so that the porosity (x [%]) of the positive electrode active material layer and the volume ratio (y [%]) of the gel-forming polymer to the volume of the positive electrode active material layer were the values shown in Table 1 below.
- the amounts of the positive electrode active material (lithium oxide) and the catalyst (cobalt oxide) used were changed to the values shown in Table 1 below, and the conditions of the pressing treatment were changed so that the porosity (x [%]) of the positive electrode active material layer and the volume ratio (y [%]) of the gel-forming polymer to the volume of the positive electrode active material layer were the values shown in Table 1 below.
- a closed-type lithium-oxygen battery (coin cell) of this comparative example was produced using the same method as in Example 1 described above, except that the amounts of the positive electrode active material (lithium oxide), catalyst (cobalt oxide), and gel-forming polymer (PVdF-HFP) used were changed to the values shown in Table 1 below, and the conditions of the pressing process were changed so that the porosity (x [%]) of the positive electrode active material layer and the volume ratio (y [%]) of the gel-forming polymer to the volume of the positive electrode active material layer were the values shown in Table 1 below.
- the positive electrode active material lithium oxide
- catalyst cobalt oxide
- PVdF-HFP gel-forming polymer
- Charge/discharge tester TOSCAT-3000, model TYS-30TU10 (manufactured by Toyo Systems Co., Ltd.)
- Charge/discharge conditions [Charging process] 0.02 C (current density 18 mA / g), 1.8 V ⁇ 4.6 V (CCCV; 0.01 C cutoff)
- Charge process 0.02C (current density 18mA/g), 4.6V ⁇ 1.8V (CC)
- Rest time between charging and discharging processes 30 minutes.
- 10a stacked lithium-oxygen battery; 11′ positive electrode current collector 12 negative electrode current collector 13 positive electrode active material layer, 15 negative electrode active material layer, 17 electrolyte layer, 19 cell layer, 21 power generating element, 25 Positive electrode current collector (positive electrode tab), 27 negative electrode current collector plate (negative electrode tab), 29 Laminating film.
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Abstract
Description
本発明は、クローズドタイプリチウム酸素電池に関する。 The present invention relates to a closed-type lithium-oxygen battery.
近年、環境・エネルギー問題の解決へ向けて、種々の電気自動車の普及が期待されている。これら電気自動車の普及の鍵を握るモータ駆動用電源などの車載電源として、二次電池の開発が鋭意行われている。二次電池としては、高エネルギー密度、高出力が期待できるリチウムイオン二次電池等の非水電解質二次電池に注目が集まっている。 In recent years, the widespread adoption of various electric vehicles is expected to help solve environmental and energy problems. Secondary batteries are being actively developed as on-board power sources for driving motors and other applications, which hold the key to the widespread adoption of these electric vehicles. Attention is being focused on non-aqueous electrolyte secondary batteries, such as lithium-ion secondary batteries, which are expected to offer high energy density and high output.
非水電解質二次電池の1種として、リチウム酸素電池(リチウム酸素二次電池)が知られている。このリチウム酸素電池は、次世代電池を含むすべての二次電池の中で最も理論エネルギー密度が高く、現行のリチウムイオン二次電池を大きく超える高いエネルギー密度を備えた電池性能が期待されている。しかしながら、いまだ十分な容量特性を実現するには至っておらず、さらなる改良が求められているのが現状である。 Lithium-oxygen batteries (lithium-oxygen secondary batteries) are known as a type of non-aqueous electrolyte secondary battery. These lithium-oxygen batteries have the highest theoretical energy density of all secondary batteries, including next-generation batteries, and are expected to offer battery performance with an energy density significantly exceeding that of current lithium-ion secondary batteries. However, sufficient capacity characteristics have yet to be achieved, and further improvements are currently required.
リチウム酸素電池は、酸素源として気体の分子状酸素(O2)を用い、放電時にはO2を消費し、充電時にはO2を生成する形式(リチウム空気電池)と、このようなO2の消費や生成を伴わない形式(狭義のリチウム酸素電池)とに大別される。後者は大気とのO2のやり取りを伴わないことから、密閉セルとして電池を構成することができ、「クローズドタイプリチウム酸素電池」と言うことができる。 Lithium-oxygen batteries are broadly divided into two types: those that use gaseous molecular oxygen ( O2 ) as the oxygen source, consume O2 during discharge, and generate O2 during charge (lithium-air batteries), and those that do not consume or generate O2 (narrowly defined lithium-oxygen batteries). Because the latter do not exchange O2 with the atmosphere, they can be constructed as sealed cells and can be called "closed-type lithium-oxygen batteries."
従来、特開2015−159098号公報には、上述したクローズドタイプリチウム酸素電池が開示されている。この文献では、クローズドタイプとして大気中の水分や二酸化炭素等のセル内への混入を防止しつつ、電極活物質である酸化リチウム(Li2O)と触媒である遷移金属原子含有酸化物(Co3O4など)とを含む原料組成物をメカノケミカル処理により微粉化させることで、電極活物質の高容量化を実現しようと試みている。 Japanese Patent Laid-Open Publication No. 2015-159098 discloses the above-mentioned closed-type lithium-oxygen battery. This document attempts to achieve a high capacity of the electrode active material by mechanochemically pulverizing a raw material composition containing lithium oxide ( Li2O ) as an electrode active material and a transition metal atom-containing oxide ( Co3O4 , etc. ) as a catalyst, while preventing atmospheric moisture, carbon dioxide, and the like from entering the cell as a closed-type battery.
本発明者らの検討によれば、特開2015−159098号に開示されている技術を用いてクローズドタイプリチウム酸素電池を作製した場合には、十分な充放電効率(充電容量に対する放電容量の比)を実現することができない場合があることが判明した。 The inventors' investigations have revealed that when closed-type lithium-oxygen batteries are fabricated using the technology disclosed in JP 2015-159098 A, it may not be possible to achieve sufficient charge/discharge efficiency (the ratio of discharge capacity to charge capacity).
そこで本発明は、クローズドタイプリチウム酸素電池の充放電効率を向上させうる手段を提供することを目的とする。 The present invention therefore aims to provide a means for improving the charge/discharge efficiency of closed-type lithium-oxygen batteries.
本発明の一形態は、リチウム酸化物、触媒およびゲル形成性ポリマーを含む電極活物質層が集電体の表面に配置された電極と、前記電極に隣接して配置されたセパレータに電解液が含浸されてなる電解質層とを有するクローズドタイプリチウム酸素電池に関する。当該電池は、前記電極活物質層の空孔率をx[%]とし、前記電極活物質層の体積に占める前記ゲル形成性ポリマーの体積の割合をy[%]とし、前記電解液に対する前記ゲル形成性ポリマーの吸液率をz[%]としたとき、下記式(1)の関係を満たす点に特徴がある:
0<yz/x≦8.7 ・・・式(1)
One aspect of the present invention relates to a closed-type lithium-oxygen battery having an electrode in which an electrode active material layer containing lithium oxide, a catalyst, and a gel-forming polymer is disposed on the surface of a current collector, and an electrolyte layer in which an electrolytic solution is impregnated in a separator disposed adjacent to the electrode. The battery is characterized in that, when the porosity of the electrode active material layer is x [%], the volume ratio of the gel-forming polymer to the volume of the electrode active material layer is y [%], and the liquid absorption rate of the gel-forming polymer with respect to the electrolytic solution is z [%], the relationship of the following formula (1) is satisfied:
0<yz/x≦8.7 Formula (1)
本発明の一形態は、リチウム酸化物、触媒およびゲル形成性ポリマーを含む電極活物質層が集電体の表面に配置された電極と、前記電極に隣接して配置されたセパレータに電解液が含浸されてなる電解質層とを有し、前記電極活物質層の空孔率をx[%]とし、前記電極活物質層の体積に占める前記ゲル形成性ポリマーの体積の割合をy[%]とし、前記電解液に対する前記ゲル形成性ポリマーの吸液率をz[%]としたとき、下記式(1)の関係を満たす、クローズドタイプリチウム酸素電池用電池である:
0<yz/x≦8.7 ・・・式(1)
本発明者らは、クローズドタイプリチウム酸素電池の充放電効率を向上させうる手段を探索する中で、電極活物質層に酸化リチウム(Li2O)および触媒に加えてゲル形成性ポリマーを含ませるとともに、上記パラメータ(x、y、z)を所定の関係に制御することが充放電効率の向上に有用であることを見出した。
One embodiment of the present invention is a battery for a closed-type lithium-oxygen battery, comprising: an electrode in which an electrode active material layer containing a lithium oxide, a catalyst, and a gel-forming polymer is disposed on the surface of a current collector; and an electrolyte layer in which an electrolytic solution is impregnated in a separator disposed adjacent to the electrode, wherein the porosity of the electrode active material layer is x [%], the ratio of the volume of the gel-forming polymer to the volume of the electrode active material layer is y [%], and the liquid absorption rate of the gel-forming polymer with respect to the electrolytic solution is z [%], the relationship of the following formula (1) is satisfied:
0<yz/x≦8.7 Formula (1)
In the course of searching for a means for improving the charge-discharge efficiency of a closed-type lithium-oxygen battery, the inventors discovered that incorporating a gel-forming polymer in addition to lithium oxide (Li 2 O) and a catalyst into the electrode active material layer and controlling the above parameters (x, y, z) to have a predetermined relationship is effective in improving the charge-discharge efficiency.
以下、図面を参照しながら、上述した本発明の実施形態を説明するが、本発明の技術的範囲は特許請求の範囲の記載に基づいて定められるべきであり、以下の形態のみに制限されない。なお、図面の寸法比率は、説明の都合上誇張されており、実際の比率とは異なる場合がある。本明細書において、範囲を示す「X~Y」は「X以上Y以下」を意味する。また、特記しない限り、操作および物性等の測定は室温(20~25℃)、相対湿度40~50%RHの条件で行う。 The following describes the above-mentioned embodiments of the present invention with reference to the drawings. However, the technical scope of the present invention should be determined based on the claims and is not limited to the following embodiments. Note that the dimensional proportions in the drawings have been exaggerated for the sake of explanation and may differ from the actual proportions. In this specification, the range "X-Y" means "X or greater and Y or less." Furthermore, unless otherwise specified, operations and measurements of physical properties are performed at room temperature (20-25°C) and a relative humidity of 40-50% RH.
図1は、本発明の一実施形態である積層型(扁平型)のクローズドタイプリチウム酸素電池(以下、単に「積層型リチウム酸素電池」とも称する)を模式的に表した断面図である。なお、本明細書において、「クローズドタイプリチウム酸素電池」とは、セルが密閉された状態で充放電反応が進行する(よって、充放電反応の進行時に大気との分子状酸素(O2)のやり取りを伴わない)リチウム酸素電池を意味する。この「クローズドタイプリチウム酸素電池」については、上述した特開2015−159098号のほか、文献(Wang, J. et al., Reversible Conversion between Lithium Superoxide and Lithium Peroxide: A Closed ”Lithium−Oxygen” Battery. Inorganics 2023, 11, 69.)などにも開示がある。また、本実施形態では、本形態に係る電極が正極である場合を例に挙げて説明するが、当該電極はクローズドタイプリチウム酸素電池の負極にも使用可能である。 1 is a cross-sectional view schematically illustrating a stacked (flat) closed-type lithium-oxygen battery (hereinafter simply referred to as a "stacked-type lithium-oxygen battery") according to one embodiment of the present invention. In this specification, the term "closed-type lithium-oxygen battery" refers to a lithium-oxygen battery in which charge and discharge reactions proceed with the cell sealed (i.e., no exchange of molecular oxygen ( O2 ) with the atmosphere occurs during the charge and discharge reactions). This "closed-type lithium-oxygen battery" is disclosed in the above-mentioned Japanese Patent Application Laid-Open No. 2015-159098 as well as in a document such as (Wang, J. et al., Reversible Conversion between Lithium Superoxide and Lithium Peroxide: A Closed "Lithium-Oxygen" Battery. Inorganics 2023, 11, 69.) Furthermore, although the present embodiment will be described taking as an example a case where the electrode according to the present embodiment is a positive electrode, the electrode can also be used as a negative electrode of a closed-type lithium-oxygen battery.
図1に示すように、本実施形態の積層型リチウム酸素電池10aは、実際に充放電反応が進行する略矩形の発電要素21が、ラミネートフィルム29の内部に封止された構造を有する。ここで、発電要素21は、正極集電体11’の両面に正極活物質層13が配置された正極と、電解液を含有するセパレータからなる電解質層17と、負極集電体12の両面に負極活物質層15が配置された負極とを積層した構成を有している。具体的には、1つの正極活物質層13とこれに隣接する負極活物質層15とが、電解質層17を介して対向するようにして、正極、電解質層および負極がこの順に積層されている。これにより、正極、電解質層および負極は、1つの単電池層19を構成する。したがって、図1に示す積層型リチウム酸素電池10aは、単電池層19が複数積層されることで、電気的に並列接続されてなる構成を有するともいえる。 As shown in FIG. 1, the stacked lithium-oxygen battery 10a of this embodiment has a structure in which a substantially rectangular power-generating element 21, where the actual charge/discharge reaction takes place, is sealed inside a laminate film 29. The power-generating element 21 is configured by stacking a positive electrode, in which a positive electrode active material layer 13 is disposed on both sides of a positive electrode current collector 11', an electrolyte layer 17 made of a separator containing an electrolytic solution, and a negative electrode, in which a negative electrode active material layer 15 is disposed on both sides of a negative electrode current collector 12. Specifically, the positive electrode, electrolyte layer, and negative electrode are stacked in this order, with one positive electrode active material layer 13 and the adjacent negative electrode active material layer 15 facing each other with the electrolyte layer 17 interposed between them. The positive electrode, electrolyte layer, and negative electrode thus constitute a single cell layer 19. Therefore, the stacked lithium-oxygen battery 10a shown in FIG. 1 can be said to have a configuration in which a plurality of cell layers 19 are stacked and electrically connected in parallel.
正極集電体11’および負極集電体12には、各電極(正極および負極)と導通される正極集電板25および負極集電板27がそれぞれ取り付けられ、ラミネートフィルム29の端部に挟まれるようにしてラミネートフィルム29の外部に導出される構造を有している。正極集電板25および負極集電板27は、それぞれ必要に応じて正極端子リードおよび負極端子リード(図示せず)を介して、各電極の正極集電体11’および負極集電体12に超音波溶接や抵抗溶接等により取り付けられていてもよい。 A positive electrode current collector 25 and a negative electrode current collector 27, which are electrically connected to the respective electrodes (positive and negative electrodes), are attached to the positive electrode current collector 11' and the negative electrode current collector 12, respectively, and are configured to be sandwiched between the edges of the laminate film 29 and extend outside the laminate film 29. If necessary, the positive electrode current collector 25 and the negative electrode current collector 27 may be attached to the positive electrode current collector 11' and the negative electrode current collector 12 of each electrode by ultrasonic welding, resistance welding, or the like, via positive electrode terminal leads and negative electrode terminal leads (not shown).
以下、本実施形態に係る積層型リチウム酸素電池の主要な構成部材について説明する。 The main components of the stacked lithium-oxygen battery according to this embodiment are described below.
[集電体]
集電体は、後述する正極活物質層や負極活物質層からの電子の移動を媒介する機能を有する。集電体を構成する材料に特に制限はない。集電体の構成材料としては、例えば、金属や、導電性を有する樹脂が採用されうる。
[Current collector]
The current collector has a function of mediating the transfer of electrons from the positive electrode active material layer and the negative electrode active material layer described later. There are no particular limitations on the material constituting the current collector. For example, metals and conductive resins can be used as the material constituting the current collector.
[電極活物質層]
電極活物質層は、上記集電体の表面に配置され、電極活物質としてのリチウム酸化物、触媒、およびゲル形成性ポリマーを含む。特に、充放電効率の向上効果への寄与がより顕著である観点から、電極活物質層は正極活物質層であることが好ましい。この場合、電極活物質(リチウム酸化物)は正極活物質として機能する。
[Electrode active material layer]
The electrode active material layer is disposed on the surface of the current collector and contains lithium oxide as an electrode active material, a catalyst, and a gel-forming polymer. In particular, the electrode active material layer is preferably a positive electrode active material layer from the viewpoint of more significant contribution to improving charge/discharge efficiency. In this case, the electrode active material (lithium oxide) functions as a positive electrode active material.
(リチウム酸化物)
リチウム酸化物は、リチウムが酸素と共有結合した化合物であり、これらの原子比によっていくつかの化合物が存在する。具体的に、リチウム酸化物は、Li2O、LiO、Li2O2およびLiO2からなる群から選択される1種または2種以上を含むことが好ましい。なかでも、リチウム酸化物は、Li2O、Li2O2またはLiO2を含むことがより好ましい。特に、他のリチウム酸化物と比較して理論容量が高く、化学的に安定である(分解しにくく、空気中の水分や二酸化炭素との反応性も低い)という観点から、Li2Oを含むことが特に好ましい。
(lithium oxide)
Lithium oxide is a compound in which lithium and oxygen are covalently bonded, and there are several compounds depending on the atomic ratio. Specifically, the lithium oxide preferably contains one or more selected from the group consisting of Li 2 O, LiO, Li 2 O 2 , and LiO 2. Among them, it is more preferable that the lithium oxide contains Li 2 O, Li 2 O 2 , or LiO 2. In particular, it is particularly preferable that the lithium oxide contains Li 2 O from the viewpoints of having a higher theoretical capacity and being chemically stable (less likely to decompose, and less reactivity with moisture and carbon dioxide in the air) compared to other lithium oxides.
なお、上記電極が正極である場合、負極を構成する負極活物質としては、従来公知の材料が採用されうる。このような負極活物質としては、例えば、グラファイト(黒鉛)、ソフトカーボン、ハードカーボン等の炭素材料、リチウム−遷移金属複合酸化物(例えば、Li4Ti5O12)、金属材料(スズ、シリコン)、ケイ素含有合金系負極材料(例えば、Si60Sn10Ti30)、リチウム合金系負極材料(例えばリチウム−スズ合金、リチウム−シリコン合金、リチウム−アルミニウム合金、リチウム−アルミニウム−マンガン合金等)などが挙げられる。好ましくは、容量、出力特性の観点から、ケイ素含有合金系負極材料、炭素材料、リチウム−遷移金属複合酸化物、リチウム合金系負極材料が、負極活物質として好ましく用いられる。 In addition, when the electrode is a positive electrode, conventionally known materials can be used as the negative electrode active material constituting the negative electrode.Such negative electrode active materials include , for example, carbon materials such as graphite, soft carbon, hard carbon, lithium-transition metal composite oxides (for example, Li4Ti5O12 ), metal materials (tin , silicon), silicon-containing alloy-based negative electrode materials (for example , Si60Sn10Ti30 ), lithium alloy-based negative electrode materials (for example, lithium-tin alloy, lithium-silicon alloy, lithium-aluminum alloy, lithium-aluminum-manganese alloy, etc.).Preferably, from the viewpoint of capacity and output characteristics, silicon-containing alloy-based negative electrode materials, carbon materials, lithium-transition metal composite oxides, and lithium alloy-based negative electrode materials are preferably used as the negative electrode active material.
(触媒)
触媒は、上述したリチウム酸化物と酸素との間の結合・解離反応の活性化エネルギーを低下させることによってこれらの反応を促進する機能を有する物質である。このような機能を発現できるのであれば、従来公知の任意の化合物が触媒として使用可能である。一例として、触媒は、遷移金属を含有する化合物(遷移金属含有化合物)であることが好ましい。この遷移金属含有化合物は、例えば、遷移金属を含有する酸化物(複合酸化物を含む)、硫化物、ハロゲン化物、窒化物、炭化物等の形態であることが好ましい。なかでも、触媒活性に優れるという観点から、触媒は遷移金属含有酸化物を含むものであることが好ましい。触媒が遷移金属含有化合物を含む場合に、当該化合物に含まれる遷移金属の種類について特に制限はなく、遷移金属に分類されるいずれの金属の原子であってもよく、1種または2種以上が用いられうる。なかでも、遷移金属は、触媒活性の観点から、周期表の第6~11族に属する遷移金属の少なくとも1種であることが好ましく、コバルト、マンガン、鉄、ニッケル、モリブデン、イリジウムおよびロジウムからなる群から選択される1種または2種以上であることがより好ましく、コバルト、マンガンおよび鉄からなる群から選択される1種または2種以上であることが特に好ましく、コバルトであることが最も好ましい。遷移金属含有化合物の一例としては、遷移金属含有酸化物である酸化コバルト、酸化マンガン、酸化鉄、酸化ニッケル、酸化モリブデン、酸化イリジウムおよび酸化ロジウムが挙げられる。なかでも、酸化コバルト、酸化マンガンおよび酸化鉄が好ましく、酸化コバルト(例えば、Co3O4)が特に好ましい。
(catalyst)
A catalyst is a substance that has the function of promoting the above-mentioned bonding/dissociation reaction between lithium oxide and oxygen by reducing the activation energy of these reactions. Any conventionally known compound can be used as a catalyst as long as it can exhibit this function. As an example, the catalyst is preferably a compound containing a transition metal (transition metal-containing compound). This transition metal-containing compound is preferably in the form of, for example, an oxide (including composite oxide), sulfide, halide, nitride, carbide, or the like containing the transition metal. Among these, from the viewpoint of excellent catalytic activity, it is preferable that the catalyst contains a transition metal-containing oxide. When the catalyst contains a transition metal-containing compound, there are no particular restrictions on the type of transition metal contained in the compound, and it may be an atom of any metal classified as a transition metal, and one or more types may be used. Among these, from the viewpoint of catalytic activity, the transition metal is preferably at least one transition metal belonging to Groups 6 to 11 of the periodic table, more preferably one or more selected from the group consisting of cobalt, manganese, iron, nickel, molybdenum, iridium, and rhodium, particularly preferably one or more selected from the group consisting of cobalt, manganese, and iron, and most preferably cobalt. Examples of transition metal-containing compounds include transition metal-containing oxides such as cobalt oxide, manganese oxide, iron oxide, nickel oxide, molybdenum oxide, iridium oxide, and rhodium oxide. Among these, cobalt oxide, manganese oxide, and iron oxide are preferred, and cobalt oxide (e.g., Co 3 O 4 ) is particularly preferred.
電極活物質層における触媒の含有量は特に制限されず、リチウム酸化物および触媒の種類にもよるが、電池の完全放電時において、上述したリチウム酸化物の全量100質量%に対して、好ましくは50~500質量%であり、より好ましくは100~450質量%であり、さらに好ましくは200~400質量%であり、特に好ましくは250~350質量%である。 The catalyst content in the electrode active material layer is not particularly limited, and although it depends on the type of lithium oxide and catalyst, it is preferably 50 to 500 mass%, more preferably 100 to 450 mass%, even more preferably 200 to 400 mass%, and especially preferably 250 to 350 mass%, relative to the total amount of lithium oxide (100 mass%) when the battery is fully discharged.
(ゲル形成性ポリマー)
ゲル形成性ポリマーは、イオン伝導性ポリマーであり、電極活物質とともに構造体を形成して、イオン伝導の役割を担うことができる。ゲル形成性ポリマーは、充放電効率および出力特性の観点から、ポリエチレンオキシド(PEO)、ポリプロピレンオキシド(PPO)、ポリエチレングリコール(PEG)、ポリアクリロニトリル(PAN)、ポリフッ化ビニリデン(PVdF)、ポリフッ化ビニリデン−ヘキサフルオロプロピレン(PVdF−HEP)、ポリメチルメタクリレート(PMMA)、ポリエチレングリコールジメタクリレート、ポリエチレングリコールジアクリレート、ポリプロピレングリコールジメタクリレート、ポリプロピレングリコールジアクリレート、ポリメチルメタクリレート、およびこれらの共重合体からなる群から選択される少なくとも1種を含むことが好ましい。また、ゲル形成性ポリマーは、充放電効率および出力特性をより高めるとの観点から、好ましくはポリエチレンオキシド(PEO)、ポリプロピレンオキシド(PPO)、ポリエチレングリコール(PEG)、ポリアクリロニトリル(PAN)、ポリフッ化ビニリデン(PVdF)、ポリフッ化ビニリデン−ヘキサフルオロプロピレン共重合体(PVdF−HEP)およびポリメチルメタクリレート(PMMA)から選択される。また、より好ましい実施形態において、ゲル形成性ポリマーは、主鎖にビニリデンフルオライドに由来する構成単位を含有するもの(例えば、ポリフッ化ビニリデン(PVdF)、ポリフッ化ビニリデン−ヘキサフルオロプロピレン共重合体(PVdF−HEP)など)を含む。特に好ましい実施形態において、ゲル形成性ポリマーはポリフッ化ビニリデン−ヘキサフルオロプロピレン共重合体(PVdF−HEP)を含む。PVdF−HFPは電解液への膨潤性が高いため、電極活物質層におけるリチウムイオン等のイオン伝導性が向上しうる。また、PVdF−HFPは柔軟性が高いため、電極活物質層に含まれる他の部材(電極活物質、触媒、導電助剤等)の隙間に入り込み、これらの分散性を向上させることもできる。その結果、電子伝導パスが良好に形成され、優れた充放電効率を発揮することができると考えられる。
(Gel-forming polymer)
The gel-forming polymer is an ion-conductive polymer, and can form a structure together with the electrode active material to play a role in ion conduction. From the viewpoint of charge/discharge efficiency and output characteristics, the gel-forming polymer preferably contains at least one selected from the group consisting of polyethylene oxide (PEO), polypropylene oxide (PPO), polyethylene glycol (PEG), polyacrylonitrile (PAN), polyvinylidene fluoride (PVdF), polyvinylidene fluoride-hexafluoropropylene (PVdF-HEP), polymethyl methacrylate (PMMA), polyethylene glycol dimethacrylate, polyethylene glycol diacrylate, polypropylene glycol dimethacrylate, polypropylene glycol diacrylate, polymethyl methacrylate, and copolymers thereof. Furthermore, from the viewpoint of further improving charge/discharge efficiency and output characteristics, the gel-forming polymer is preferably selected from polyethylene oxide (PEO), polypropylene oxide (PPO), polyethylene glycol (PEG), polyacrylonitrile (PAN), polyvinylidene fluoride (PVdF), polyvinylidene fluoride-hexafluoropropylene copolymer (PVdF-HEP), and polymethyl methacrylate (PMMA). Furthermore, in a more preferred embodiment, the gel-forming polymer includes one containing a structural unit derived from vinylidene fluoride in the main chain (e.g., polyvinylidene fluoride (PVdF), polyvinylidene fluoride-hexafluoropropylene copolymer (PVdF-HEP), etc.). In a particularly preferred embodiment, the gel-forming polymer includes polyvinylidene fluoride-hexafluoropropylene copolymer (PVdF-HEP). PVdF-HFP has high swelling properties in electrolytes, which can improve the ionic conductivity of lithium ions and the like in the electrode active material layer. Furthermore, because PVdF-HFP is highly flexible, it can penetrate into the gaps between other components (electrode active materials, catalysts, conductive additives, etc.) contained in the electrode active material layer, improving their dispersibility. As a result, it is believed that electron conduction paths are well formed, enabling excellent charge/discharge efficiency.
PVdF−HFPはフッ化ビニリデンおよびヘキサフルオロプロピレンの共重合体であれば特に制限されない。PVdF−HFPに含まれるヘキサフルオロプロピレン由来の構成単位の割合の下限は、PVdF−HFPの全構成単位に対して、4モル%以上であることが好ましく、6モル%以上であることがより好ましく、6.5モル%以上であることがさらに好ましい。また、PVdF−HFPに含まれるヘキサフルオロプロピレン由来の構成単位の割合の下限は、20モル%以下であることが好ましく、10モル%以下であることがより好ましく、8モル%以下であることがさらに好ましい。ヘキサフルオロプロピレン由来の構成単位の割合が上記範囲であることにより、電解液への膨潤性、柔軟性がより向上しうる。その結果、電極活物質層におけるイオン伝導性や電子伝導性が向上し、優れた充放電効率を発揮することができる。 PVdF-HFP is not particularly limited as long as it is a copolymer of vinylidene fluoride and hexafluoropropylene. The lower limit of the proportion of hexafluoropropylene-derived structural units contained in PVdF-HFP, relative to the total structural units of PVdF-HFP, is preferably 4 mol% or more, more preferably 6 mol% or more, and even more preferably 6.5 mol% or more. Furthermore, the lower limit of the proportion of hexafluoropropylene-derived structural units contained in PVdF-HFP is preferably 20 mol% or less, more preferably 10 mol% or less, and even more preferably 8 mol% or less. When the proportion of hexafluoropropylene-derived structural units is within the above range, swelling in the electrolyte and flexibility can be further improved. As a result, the ionic conductivity and electronic conductivity of the electrode active material layer are improved, enabling excellent charge/discharge efficiency to be achieved.
電極活物質層におけるゲル形成性ポリマーの含有量は特に制限されず、リチウム酸化物およびゲル形成性ポリマーの種類にもよるが、電池の完全放電時において、上述したリチウム酸化物の全量100質量%に対して、好ましくは10~100質量%であり、より好ましくは12~70質量%であり、さらに好ましくは15~60質量%である。 The content of the gel-forming polymer in the electrode active material layer is not particularly limited, and although it depends on the type of lithium oxide and gel-forming polymer, it is preferably 10 to 100% by mass, more preferably 12 to 70% by mass, and even more preferably 15 to 60% by mass, relative to the total amount of the lithium oxide (100% by mass) when the battery is fully discharged.
(ゲル形成性ポリマー以外のバインダ)
なお、電極活物質層は、上述したゲル形成性ポリマー以外のバインダをさらに含んでもよい。このようなバインダとしては、例えば、ポリイミド、スチレン−ブタジエンゴム、カルボキシメチルセルロース、ポリプロピレン、ポリテトラフルオロエチレン、ポリアクリロニトリル、ポリアミドなどが挙げられる、ただし、これらのバインダの含有量は少ないほど好ましい。具体的に、バインダの全量100質量%に占めるゲル形成性ポリマーの含有量は、好ましくは50質量%以上であり、より好ましくは80質量%以上であり、さらに好ましくは90質量%以上であり、特に好ましくは95質量%以上であり、最も好ましくは100質量%である。
(Binders other than gel-forming polymers)
The electrode active material layer may further contain a binder other than the gel-forming polymer. Examples of such binders include polyimide, styrene-butadiene rubber, carboxymethyl cellulose, polypropylene, polytetrafluoroethylene, polyacrylonitrile, and polyamide. However, the lower the content of these binders, the better. Specifically, the content of the gel-forming polymer relative to the total amount (100% by mass) of the binder is preferably 50% by mass or more, more preferably 80% by mass or more, even more preferably 90% by mass or more, particularly preferably 95% by mass or more, and most preferably 100% by mass.
(導電助剤)
電極活物質層は、導電助剤をさらに含むことができる。導電助剤は、導電助剤は、電極活物質層中で電子伝導パス(導電通路)を形成する機能を有する。このような電子伝導パスが正極活物質層中に形成されると、電池の内部抵抗が低減し、レート特性が向上しうる。
(Conductive additive)
The electrode active material layer may further include a conductive additive. The conductive additive has a function of forming an electron conduction path (conductive passage) in the electrode active material layer. When such an electron conduction path is formed in the positive electrode active material layer, the internal resistance of the battery may be reduced and the rate characteristics may be improved.
導電助剤としては、アセチレンブラック、カーボンブラック、チャンネルブラック、サーマルブラック、ケッチェンブラック(登録商標)等の粒子状炭素材料、およびカーボンナノチューブ(単層カーボンナノチューブおよび複層カーボンナノチューブ)、カーボンナノファイバー、気相成長炭素繊維、電界紡糸法炭素繊維、ポリアクリロニトリル系炭素繊維、ピッチ系炭素繊維等の繊維状炭素材料が挙げられる。導電助剤は、1種のみが単独で使用されてもよいし、2種以上が併用されてもよい。 Conductive additives include particulate carbon materials such as acetylene black, carbon black, channel black, thermal black, and Ketjen Black (registered trademark), as well as fibrous carbon materials such as carbon nanotubes (single-walled carbon nanotubes and multi-walled carbon nanotubes), carbon nanofibers, vapor-grown carbon fibers, electrospun carbon fibers, polyacrylonitrile-based carbon fibers, and pitch-based carbon fibers. One type of conductive additive may be used alone, or two or more types may be used in combination.
電極活物質層に含まれる導電助剤の含有量は、電極活物質層の全固形分100質量%に対して、15質量%以下であることが好ましく、12質量%以下であることがより好ましく、10質量%以下であることがさらに好ましい。かような上限値であると、導電助剤同士の凝集が抑制されることにより電子伝導パスが良好に形成されるため、充放電効率をより向上させることができる。なお、導電助剤の含有量の下限値は特に制限されないが、0質量%を超え、1質量%以上であることが好ましく、2質量%以上であることが好ましく、3質量%以上であることがさらに好ましい。かような下限値であると、電子伝導パスを形成するための十分な導電助剤が存在することから、充放電効率をより向上することができる。 The content of the conductive additive in the electrode active material layer is preferably 15% by mass or less, more preferably 12% by mass or less, and even more preferably 10% by mass or less, relative to 100% by mass of the total solids content of the electrode active material layer. At such an upper limit, aggregation of the conductive additives is suppressed, resulting in favorable formation of electron conduction paths, thereby further improving charge/discharge efficiency. There is no particular lower limit for the conductive additive content, but it is preferably greater than 0% by mass, and is preferably 1% by mass or more, more preferably 2% by mass or more, and even more preferably 3% by mass or more. At such a lower limit, sufficient conductive additive is present to form electron conduction paths, thereby further improving charge/discharge efficiency.
電極活物質層における各構成成分(リチウム酸化物、触媒、ゲル形成性ポリマーおよび任意の導電助剤)の存在形態について特に制限はないが、電池反応に関与するリチウム酸化物と触媒とが互いに接触するようにこれらの構成成分が存在していることが好ましい。特に、リチウム酸化物と触媒とが、ゲル形成性ポリマーによって複合化された複合粒子の形態であることがより好ましい。ここで、リチウム酸化物と触媒とが「複合粒子の形態である」とは、クローズドタイプリチウム酸素電池に対して充放電反応を実施した際に、充放電時にリチウム酸化物が膨張収縮したとしても粒子が崩壊せずに粒子の形状を保っている状態を意味する。このような構成とすることによって、リチウム酸化物を電極材料として用いた場合に充放電反応がよりスムーズに進行し、電池の容量特性のより一層の向上に有効に寄与しうる。 While there are no particular restrictions on the form in which each component (lithium oxide, catalyst, gel-forming polymer, and optional conductive additive) in the electrode active material layer exists, it is preferable that these components be present so that the lithium oxide and catalyst involved in the battery reaction are in contact with each other. In particular, it is more preferable that the lithium oxide and catalyst are in the form of composite particles combined with a gel-forming polymer. Here, "in the form of composite particles" of the lithium oxide and catalyst means that when a charge/discharge reaction is carried out in a closed-type lithium-oxygen battery, the particles do not collapse and maintain their particle shape even if the lithium oxide expands and contracts during charge/discharge. This configuration allows the charge/discharge reaction to proceed more smoothly when lithium oxide is used as an electrode material, which can effectively contribute to further improving the capacity characteristics of the battery.
[電極活物質層の空孔率、ゲル形成性ポリマーの体積の割合、およびゲル形成性ポリマーの吸液率の関係]
上述したように、本形態に係る電池は、電極活物質層の空孔率をx[%]とし、電極活物質層の体積に占めるゲル形成性ポリマーの体積の割合をy[%]とし、電解質層に含まれる電解液に対するゲル形成性ポリマーの吸液率をz[%]としたときに、式(1):0<yz/x≦8.7を満たすことを特徴とする。本発明者らは、電極活物質層の空孔率(x)、電極活物質層の体積に占めるゲル形成性ポリマーの体積の割合(y)、および電解質層に含まれる電解液に対するゲル形成性ポリマーの吸液率(z)の間に、電池の充放電効率の観点からの適正範囲が存在することを見出し、その知見を上記関係式で数値化した。
[Relationship between the porosity of the electrode active material layer, the volume ratio of the gel-forming polymer, and the liquid absorption rate of the gel-forming polymer]
As described above, the battery according to this embodiment is characterized in that, when the porosity of the electrode active material layer is x [%], the volume ratio of the gel-forming polymer to the volume of the electrode active material layer is y [%], and the liquid absorption rate of the gel-forming polymer with respect to the electrolyte solution contained in the electrolyte layer is z [%], the battery satisfies formula (1): 0 < yz/x ≦ 8.7. The inventors have found that there are appropriate ranges from the viewpoint of the charge/discharge efficiency of the battery among the porosity of the electrode active material layer (x), the volume ratio of the gel-forming polymer to the volume of the electrode active material layer (y), and the liquid absorption rate of the gel-forming polymer with respect to the electrolyte solution contained in the electrolyte layer (z), and have quantified this finding using the above relational formula.
上記yz/xの値が8.7を超えると(つまり、ゲル形成性ポリマーの体積割合が多すぎたり吸液率が大きすぎたりすると)、十分な充放電効率を達成することができない。これは、電極活物質であるリチウム酸化物が収縮したときにゲル形成性ポリマーが電極活物質と触媒との間に入り込んでこれらの接点(反応場)が減少し、その後の電池反応が進行しにくくなることによるものと考えられる。これに対し、上記yz/xの値が8.7以下であれば、リチウム酸化物の収縮にゲル形成性ポリマーが適切に追従することができ、充放電反応の全体にわたって、電極活物質と触媒との接触も十分に維持される。また、ゲル形成性ポリマーが柔軟性を有していることで、電極活物質および触媒の活物質層内での動きが抑制され、これらの材料の脱落も効果的に防止される。そして、これらのメカニズムに起因して、繰り返しの充放電の後であっても電極活物質と触媒との初期の接触状態を維持することができ、初期の容量を維持できる(つまり、充放電効率が向上する)ものと考えられる。ただし、上記のメカニズムはあくまでも推測に基づくものであり、当該メカニズムの正誤が本発明の技術的範囲に影響することはない。 If the yz/x value exceeds 8.7 (i.e., if the volume fraction of the gel-forming polymer is too high or the liquid absorption rate is too high), sufficient charge/discharge efficiency cannot be achieved. This is thought to be because, when the lithium oxide (electrode active material) shrinks, the gel-forming polymer penetrates between the electrode active material and the catalyst, reducing the contact point (reaction field) between them and hindering the subsequent battery reaction. In contrast, if the yz/x value is 8.7 or less, the gel-forming polymer can appropriately follow the contraction of the lithium oxide, maintaining sufficient contact between the electrode active material and the catalyst throughout the charge/discharge reaction. Furthermore, the flexibility of the gel-forming polymer suppresses the movement of the electrode active material and catalyst within the active material layer, effectively preventing their detachment. These mechanisms are thought to maintain the initial contact between the electrode active material and the catalyst even after repeated charge/discharge cycles, maintaining the initial capacity (i.e., improving charge/discharge efficiency). However, the above mechanism is merely speculative, and the accuracy of this mechanism does not affect the technical scope of the present invention.
充放電効率をより一層向上させるという観点から、上記yz/xの値は、式(2):1.4≦yz/x≦8.7を満たすことが好ましく、式(3):3.2≦yz/x≦5.7を満たすことがより好ましく、式(4):3.8≦yz/x≦4.8を満たすことがさらに好ましい。上記yz/xの値がこれらの範囲内であれば、リチウム酸化物の収縮に対してゲル形成性ポリマーがより優れた追従性を発揮し、充放電効率をより一層向上させることができる。なお、上記x、yおよびzの値は、後述する実施例に記載の方法により算出するものとする。また、本明細書において、「充放電効率の向上」とは、本形態に係る電池を構成した場合に、本形態に係る電池の規定を満たさないこと以外は同じ構成を有する電池(比較電池)を構成した場合と比較して、初回充放電効率が向上することを意味する。この際の初回充放電効率の向上の程度について特に制限はないが、本形態に係る電池の初回充放電効率は、比較電池の初回充放電効率を100としたときに、好ましくは105以上であり、より好ましくは119以上であり、さらに好ましくは125以上であり、特に好ましくは127以上である。なお、初回充放電効率の測定は、後述する実施例の欄に記載の方法を用いて実施される。 From the perspective of further improving charge-discharge efficiency, the value of yz/x preferably satisfies formula (2): 1.4≦yz/x≦8.7, more preferably formula (3): 3.2≦yz/x≦5.7, and even more preferably formula (4): 3.8≦yz/x≦4.8. When the value of yz/x is within these ranges, the gel-forming polymer exhibits better compliance with the contraction of the lithium oxide, thereby further improving charge-discharge efficiency. The values of x, y, and z are calculated using the method described in the Examples below. In this specification, "improved charge-discharge efficiency" means that when a battery according to the present embodiment is constructed, the initial charge-discharge efficiency is improved compared to when a battery (comparative battery) having the same configuration except for not satisfying the specifications of the battery according to the present embodiment is constructed. There are no particular restrictions on the degree of improvement in the initial charge/discharge efficiency, but the initial charge/discharge efficiency of the battery according to this embodiment is preferably 105 or more, more preferably 119 or more, even more preferably 125 or more, and particularly preferably 127 or more, when the initial charge/discharge efficiency of the comparative battery is taken as 100. The initial charge/discharge efficiency is measured using the method described in the Examples section below.
上記xは、電極活物質の粒子径、ゲル形成性ポリマーの仕込み量、電極活物質層の厚み、電極作製時のプレス条件等を調整することにより制御することができる。充放電効率をより向上させるという観点から、電極活物質層の空孔率(x)は、好ましくは25≦x≦70を満たし、より好ましくは25≦x≦50を満たし、さらに好ましくは28≦x≦37を満たし、特に好ましくは30≦x≦37を満たす。 The above x can be controlled by adjusting the particle size of the electrode active material, the amount of gel-forming polymer added, the thickness of the electrode active material layer, the pressing conditions during electrode fabrication, etc. From the perspective of further improving charge/discharge efficiency, the porosity (x) of the electrode active material layer preferably satisfies 25≦x≦70, more preferably 25≦x≦50, even more preferably 28≦x≦37, and particularly preferably 30≦x≦37.
また、上記yは、電極活物質層中のゲル形成性ポリマーの含有量等を調整することにより制御することができる。充放電効率をより向上させるという観点から、電極活物質層の体積に占めるゲル形成性ポリマーの体積の割合(y)は、好ましくは7.0≦y≦15.0を満たし、より好ましくは9.0≦y≦13.0を満たし、さらに好ましくは10.5≦y≦12.5を満たす。 Furthermore, the above y can be controlled by adjusting the content of the gel-forming polymer in the electrode active material layer. From the perspective of further improving charge/discharge efficiency, the volume ratio (y) of the gel-forming polymer to the volume of the electrode active material layer preferably satisfies 7.0≦y≦15.0, more preferably 9.0≦y≦13.0, and even more preferably 10.5≦y≦12.5.
さらに、上記zは、ゲル形成性ポリマーの種類や電解液の組成を変化させることによって制御することができる。充放電効率をより向上させるという観点から、ゲル形成性ポリマーの吸液率(z)は、好ましくは10≦z≦100を満たし、より好ましくは12≦x≦50を満たす。 Furthermore, the above z can be controlled by changing the type of gel-forming polymer and the composition of the electrolyte solution. From the perspective of further improving charge/discharge efficiency, the liquid absorption rate (z) of the gel-forming polymer preferably satisfies 10≦z≦100, and more preferably 12≦x≦50.
電極活物質層の厚みは特に制限されず、電池についての従来公知の知見が適宜参照されうる。一例を挙げると、電極活物質層の厚みは、通常1~1000μm程度、好ましくは20~800μmであり、より好ましくは30~500μmであり、さらに好ましくは40~200μmである。電極活物質層の厚みが大きいほど、十分な容量(エネルギー密度)を発揮するための電極活物質を保持することが可能となる。一方、電極活物質層の厚みが小さいほど、放電レート特性が向上しうる。 There are no particular restrictions on the thickness of the electrode active material layer, and conventionally known knowledge about batteries can be referenced as appropriate. For example, the thickness of the electrode active material layer is typically about 1 to 1000 μm, preferably 20 to 800 μm, more preferably 30 to 500 μm, and even more preferably 40 to 200 μm. The thicker the electrode active material layer, the more electrode active material can be retained to achieve sufficient capacity (energy density). On the other hand, the thinner the electrode active material layer, the more improved the discharge rate characteristics can be.
[電解質層]
電解質層は、電解液(液体電解質)を含む。電解質層は、セパレータに電解液が含浸されてなる構成を有することが好ましい。
[Electrolyte layer]
The electrolyte layer contains an electrolytic solution (liquid electrolyte) and preferably has a configuration in which a separator is impregnated with the electrolytic solution.
(電解液)
電解液は、リチウムイオンのキャリヤーとしての機能を有する。電解液は、非水溶媒にリチウム塩が溶解した形態を有する。好ましくは、電解液は、非水溶媒にリチウム塩を溶解させたものに含フッ素カーボネートがさらに添加されたものである。
(electrolyte)
The electrolyte functions as a carrier of lithium ions. The electrolyte has a form in which a lithium salt is dissolved in a non-aqueous solvent. Preferably, the electrolyte is obtained by further adding a fluorine-containing carbonate to the non-aqueous solvent in which the lithium salt is dissolved.
非水溶媒としては、リチウム塩を溶解しやすいものが好ましく、例えば、ジメチルカーボネート(DMC)、ジエチルカーボネート(DEC)、ジプロピルカーボネート(DPC)、メチルプロピルカーボネート(MPC)、エチルプロピルカーボネート(EPC)、メチルエチルカーボネート(MEC)などの鎖状カーボネート;これらの鎖状カーボネートの水素原子の一部がフッ素原子で置換された含フッ素鎖状カーボネート;エチレンカーボネート(EC)、プロピレンカーボネート(PC)、ブチレンカーボネート(BC)などの環状カーボネート;これらの環状カーボネートの水素原子の一部がフッ素原子で置換された含フッ素環状カーボネート;プロピオン酸メチル(MP)、酢酸メチル(MA)、ギ酸メチル(MF)、4−メチルジオキソラン(4MeDOL)、ジオキソラン(DOL)、2−メチルテトラヒドロフラン(2MeTHF)、テトラヒドロフラン(THF)、ジメトキシエタン(DME)、ジメチルスルホキシド(DMSO)、およびγ−ブチロラクトン(GBL)などが挙げられる。 Preferred non-aqueous solvents are those that readily dissolve lithium salts, such as chain carbonates such as dimethyl carbonate (DMC), diethyl carbonate (DEC), dipropyl carbonate (DPC), methyl propyl carbonate (MPC), ethyl propyl carbonate (EPC), and methyl ethyl carbonate (MEC); fluorine-containing chain carbonates in which some of the hydrogen atoms of these chain carbonates have been replaced with fluorine atoms; ethylene carbonate (EC), propylene carbonate (PC), and butyl carbonate. fluorine-containing cyclic carbonates in which some of the hydrogen atoms of these cyclic carbonates have been replaced with fluorine atoms; methyl propionate (MP), methyl acetate (MA), methyl formate (MF), 4-methyldioxolane (4MeDOL), dioxolane (DOL), 2-methyltetrahydrofuran (2MeTHF), tetrahydrofuran (THF), dimethoxyethane (DME), dimethyl sulfoxide (DMSO), and gamma-butyrolactone (GBL).
なかでも、非水溶媒は、急速充電特性および出力特性をより向上できるとの観点から、鎖状カーボネートを含むことが好ましく、ジエチルカーボネート(DEC)、エチルメチルカーボネート(EMC)およびジメチルカーボネート(DMC)からなる群から選択される少なくとも1種を含むことがより好ましい。 In particular, from the viewpoint of further improving rapid charging characteristics and output characteristics, it is preferable that the non-aqueous solvent contains a chain carbonate, and it is even more preferable that it contains at least one selected from the group consisting of diethyl carbonate (DEC), ethyl methyl carbonate (EMC), and dimethyl carbonate (DMC).
リチウム塩としては、Li(FSO2)2N(リチウムビス(フルオロスルホニル)イミド;LiFSI)、Li(C2F5SO2)2N、LiPF6、LiBF4、LiClO4、LiAsF6、LiCF3SO3等が挙げられる。 Examples of lithium salts include Li( FSO2 ) 2N (lithium bis(fluorosulfonyl)imide; LiFSI ), Li ( C2F5SO2 ) 2N , LiPF6 , LiBF4 , LiClO4 , LiAsF6 , and LiCF3SO3 .
上記非水溶媒中のリチウム塩の濃度は、0.1~3.0mol/Lであることが好ましく、0.8~2.2mol/Lであることがより好ましい。 The concentration of the lithium salt in the non-aqueous solvent is preferably 0.1 to 3.0 mol/L, and more preferably 0.8 to 2.2 mol/L.
また、電解液は、含フッ素環状カーボネート、含フッ素鎖状カーボネートなどの含フッ素カーボネートをさらに含むことが好ましい。このようにすることで電池を高電圧で動作させた場合であっても優れた耐久性を有しうる。また、これらの含フッ素カーボネートは正極活物質の表面に保護膜を形成し、正極活物質の耐電圧性を高めることができる。 It is also preferable that the electrolyte solution further contains a fluorine-containing carbonate, such as a fluorine-containing cyclic carbonate or a fluorine-containing chain carbonate. This allows the battery to have excellent durability even when operated at high voltage. Furthermore, these fluorine-containing carbonates form a protective film on the surface of the positive electrode active material, thereby improving the voltage resistance of the positive electrode active material.
この際、含フッ素カーボネートとしては、フルオロエチレンカーボネート(FEC)、ジフルオロエチレンカーボネート、4−フルオロプロピレンカーボネートなどの含フッ素環状カーボネート;エチルトリフルオロメチルカーボネート、2,2,2−トリフルオロエチルメチルカーボネート、ビス(2,2,2−トリフルオロエチル)カーボネートなどの含フッ素鎖状カーボネートが好ましく用いられうる。含フッ素カーボネートの含有量は特に制限されない。好ましい実施形態において、電解液は、含フッ素カーボネート、特にはフルオロエチレンカーボネートを最終的に得られる電解液の全量に対して0.5~10質量%含む。これにより上記効果がより顕著に得られうる。なお、電解液が2種類以上の含フッ素カーボネートを含む場合はその合計量が上記範囲であることが好ましい。 In this case, preferred fluorine-containing carbonates include fluorine-containing cyclic carbonates such as fluoroethylene carbonate (FEC), difluoroethylene carbonate, and 4-fluoropropylene carbonate; and fluorine-containing chain carbonates such as ethyl trifluoromethyl carbonate, 2,2,2-trifluoroethyl methyl carbonate, and bis(2,2,2-trifluoroethyl) carbonate. The content of the fluorine-containing carbonate is not particularly limited. In a preferred embodiment, the electrolyte solution contains 0.5 to 10 mass% of fluorine-containing carbonate, particularly fluoroethylene carbonate, based on the total amount of the finally obtained electrolyte solution. This makes it possible to achieve the above-mentioned effects more significantly. When the electrolyte solution contains two or more types of fluorine-containing carbonates, it is preferable that the total amount thereof be within the above range.
電解液は、上述した成分以外の添加剤をさらに含有してもよい。かような化合物の具体例としては、例えば、ビニレンカーボネート、メチルビニレンカーボネート、ジメチルビニレンカーボネート、フェニルビニレンカーボネート、ジフェニルビニレンカーボネート、エチルビニレンカーボネート、ジエチルビニレンカーボネート、ビニルエチレンカーボネート、1,2−ジビニルエチレンカーボネート、1−メチル−1−ビニルエチレンカーボネート、1−メチル−2−ビニルエチレンカーボネート、1−エチル−1−ビニルエチレンカーボネート、1−エチル−2−ビニルエチレンカーボネート、ビニルビニレンカーボネート、アリルエチレンカーボネート、ビニルオキシメチルエチレンカーボネート、アリルオキシメチルエチレンカーボネート、アクリルオキシメチルエチレンカーボネート、メタクリルオキシメチルエチレンカーボネート、エチニルエチレンカーボネート、プロパルギルエチレンカーボネート、エチニルオキシメチルエチレンカーボネート、プロパルギルオキシエチレンカーボネート、メチレンエチレンカーボネート、1,1−ジメチル−2−メチレンエチレンカーボネートなどが挙げられる。これらの添加剤は、1種のみが単独で用いられてもよいし、2種以上が併用されてもよい。また、添加剤を電解液に使用する場合の使用量は、適宜調整することができる。 The electrolyte may further contain additives other than the components mentioned above. Specific examples of such compounds include vinylene carbonate, methyl vinylene carbonate, dimethyl vinylene carbonate, phenyl vinylene carbonate, diphenyl vinylene carbonate, ethyl vinylene carbonate, diethyl vinylene carbonate, vinyl ethylene carbonate, 1,2-divinyl ethylene carbonate, 1-methyl-1-vinyl ethylene carbonate, 1-methyl-2-vinyl ethylene carbonate, 1-ethyl-1-vinyl ethylene carbonate, and 1-ethyl-2-vinyl ethylene carbonate. Examples of the additives include ethylene carbonate, vinyl vinylene carbonate, allyl ethylene carbonate, vinyloxymethyl ethylene carbonate, allyloxymethyl ethylene carbonate, acryloxymethyl ethylene carbonate, methacryloxymethyl ethylene carbonate, ethynyl ethylene carbonate, propargyl ethylene carbonate, ethynyloxymethyl ethylene carbonate, propargyloxyethylene carbonate, methylene ethylene carbonate, and 1,1-dimethyl-2-methylene ethylene carbonate. These additives may be used alone or in combination of two or more. Furthermore, when an additive is used in the electrolyte, the amount used can be adjusted as appropriate.
(セパレータ)
電解質層を構成するセパレータは、電解質を保持して正極と負極との間のリチウムイオン伝導性を確保する機能、および正極と負極との間の隔壁としての機能を有する。
(separator)
The separator constituting the electrolyte layer has the function of retaining the electrolyte to ensure lithium ion conductivity between the positive electrode and the negative electrode, and also functions as a partition wall between the positive electrode and the negative electrode.
セパレータの形態としては、例えば、上記電解液を吸収保持するポリマーや繊維からなる多孔性シートのセパレータや不織布セパレータ等を挙げることができる。 Examples of the separator's form include a porous sheet separator made of polymer or fiber that absorbs and retains the electrolyte, and a nonwoven fabric separator.
ポリマーないし繊維からなる多孔性シートのセパレータとしては、例えば、微多孔質(微多孔膜)を用いることができる。該ポリマーないし繊維からなる多孔性シートの具体的な形態としては、例えば、ポリエチレン(PE)、ポリプロピレン(PP)などのポリオレフィン;これらを複数積層した積層体(例えば、PP/PE/PPの3層構造をした積層体など)、ポリイミド、アラミド、ポリフッ化ビニリデン−ヘキサフルオロプロピレン(PVDF−HFP)等の炭化水素系樹脂、ガラス繊維などからなる微多孔質(微多孔膜)セパレータが挙げられる。 As a porous sheet separator made of a polymer or fiber, for example, a microporous material (microporous membrane) can be used. Specific forms of the porous sheet made of polymer or fiber include microporous (microporous membrane) separators made of polyolefins such as polyethylene (PE) and polypropylene (PP); laminates of multiple layers of these (for example, a laminate with a three-layer structure of PP/PE/PP); hydrocarbon resins such as polyimide, aramid, and polyvinylidene fluoride-hexafluoropropylene (PVDF-HFP); and glass fibers.
不織布セパレータとしては、綿、レーヨン、アセテート、ナイロン、ポリエステル;PP、PEなどのポリオレフィン;ポリイミド、アラミドなど従来公知のものを、単独または混合して用いる。 Nonwoven fabric separators may be made from conventional materials such as cotton, rayon, acetate, nylon, polyester; polyolefins such as PP and PE; polyimide, and aramid, either alone or in combination.
セパレータの厚みは、電解質層と同じであればよく、好ましくは5~200μmであり、特に好ましくは10~100μmである。 The thickness of the separator should be the same as that of the electrolyte layer, preferably 5 to 200 μm, and particularly preferably 10 to 100 μm.
また、セパレータとして、多孔質基体に耐熱絶縁層が積層されたセパレータ(耐熱絶縁層付セパレータ)を用いることができる。耐熱絶縁層は、無機粒子およびバインダを含むセラミック層である。耐熱絶縁層付セパレータは融点または熱軟化点が150℃以上、好ましくは200℃以上である耐熱性の高いものを用いる。耐熱絶縁層を有することによって、温度上昇の際に増大するセパレータの内部応力が緩和されるため熱収縮抑制効果が得られうる。その結果、電池の電極間ショートの誘発を防ぐことができるため、温度上昇による性能低下が起こりにくい電池構成になる。また、耐熱絶縁層を有することによって、耐熱絶縁層付セパレータの機械的強度が向上し、セパレータの破膜が起こりにくい。さらに、熱収縮抑制効果および機械的強度の高さから、電池の製造工程でセパレータがカールしにくくなる。 Furthermore, a separator with a heat-resistant insulating layer laminated on a porous substrate (separator with heat-resistant insulating layer) can be used. The heat-resistant insulating layer is a ceramic layer containing inorganic particles and a binder. A highly heat-resistant separator with a melting point or thermal softening point of 150°C or higher, preferably 200°C or higher, is used. The presence of a heat-resistant insulating layer alleviates the internal stress of the separator that increases with temperature rise, thereby suppressing thermal shrinkage. As a result, short circuits between battery electrodes can be prevented, resulting in a battery configuration that is less susceptible to performance degradation due to temperature rise. Furthermore, the presence of a heat-resistant insulating layer improves the mechanical strength of the separator with heat-resistant insulating layer, making it less likely to rupture. Furthermore, the heat-shrinkage suppression effect and high mechanical strength make the separator less likely to curl during the battery manufacturing process.
[正極集電板および負極集電板]
集電板(25、27)を構成する材料は、特に制限されず、リチウムイオン二次電池用の集電板として従来用いられている公知の高導電性材料が用いられうる。集電板の構成材料としては、例えば、アルミニウム、銅、チタン、ニッケル、ステンレス鋼(SUS)、これらの合金等の金属材料が好ましい。軽量、耐食性、高導電性の観点から、より好ましくはアルミニウム、銅であり、特に好ましくはアルミニウムである。なお、正極集電板25と負極集電板27とでは、同一の材料が用いられてもよいし、異なる材料が用いられてもよい。
[Positive electrode current collector plate and negative electrode current collector plate]
The material constituting the current collector plates (25, 27) is not particularly limited, and known highly conductive materials conventionally used as current collector plates for lithium-ion secondary batteries can be used. Metal materials such as aluminum, copper, titanium, nickel, stainless steel (SUS), and alloys thereof are preferred as constituent materials of the current collector plates. From the viewpoints of light weight, corrosion resistance, and high conductivity, aluminum and copper are more preferred, and aluminum is particularly preferred. The positive electrode current collector plate 25 and the negative electrode current collector plate 27 may be made of the same material or different materials.
本形態に係るクローズドタイプリチウム酸素電池は、上述したように充放電効率に優れるものである。したがって、本形態に係るクローズドタイプリチウム酸素電池は、EV、HEVの駆動用電源として好適に使用される。 As described above, the closed-type lithium-oxygen battery according to this embodiment has excellent charge/discharge efficiency. Therefore, the closed-type lithium-oxygen battery according to this embodiment is suitable for use as a power source for driving EVs and HEVs.
以上、本発明の一形態に係るクローズドタイプリチウム酸素電池を説明したが、本発明は上述した実施形態において説明した構成のみに限定されることはなく、特許請求の範囲の記載に基づいて適宜変更することが可能である。 The above describes a closed-type lithium-oxygen battery according to one embodiment of the present invention, but the present invention is not limited to the configuration described in the above embodiment and can be modified as appropriate based on the claims.
なお、以下の実施形態も本発明の範囲に含まれる:請求項2の特徴を有する請求項1に記載の電池;請求項3の特徴を有する請求項1または2に記載の電池;請求項4の特徴を有する請求項1~3のいずれかに記載の電池;請求項5の特徴を有する請求項1~4のいずれかに記載の電池;請求項6の特徴を有する請求項1~5のいずれかに記載の電池;請求項7の特徴を有する請求項6に記載の電池;請求項8の特徴を有する請求項1~7のいずれかに記載の電池;請求項9の特徴を有する請求項1~8のいずれかに記載の電池;請求項10の特徴を有する請求項1~9のいずれかに記載の電池;請求項11の特徴を有する請求項1~10のいずれかに記載の電池。 The following embodiments are also within the scope of the present invention: the battery according to claim 1 having the characteristics of claim 2; the battery according to claim 1 or 2 having the characteristics of claim 3; the battery according to any one of claims 1 to 3 having the characteristics of claim 4; the battery according to any one of claims 1 to 4 having the characteristics of claim 5; the battery according to any one of claims 1 to 5 having the characteristics of claim 6; the battery according to claim 6 having the characteristics of claim 7; the battery according to any one of claims 1 to 7 having the characteristics of claim 8; the battery according to any one of claims 1 to 8 having the characteristics of claim 9; the battery according to any one of claims 1 to 9 having the characteristics of claim 10; and the battery according to any one of claims 1 to 10 having the characteristics of claim 11.
以下、実施例により本発明をさらに詳細に説明する。ただし、本発明の技術的範囲が以下の実施例のみに制限されるわけではない。 The present invention will be explained in more detail below using examples. However, the technical scope of the present invention is not limited to the following examples.
《クローズドタイプリチウム酸素電池の作製》
[測定方法]
以下の実施例および比較例において、x、yおよびzの値については、それぞれ以下の測定方法を用いて測定した。
<<Creating a closed-type lithium-oxygen battery>>
[Measurement method]
In the following examples and comparative examples, the values of x, y and z were measured using the following measurement methods.
(正極活物質層の空孔率(x)の測定)
正極活物質層の空孔率(x)については、以下のようにして測定した:
(1)正極活物質層の単位面積当たりの質量を測定した。そして、材料の配合比から、正極活物質層の単位面積当たりの各材料の質量を求めた。
(2)マイクロメーターを用いて、正極活物質層の厚み[A]を測定した。
(3)(1)で求めた各材料の質量と、各材料の密度とを用いて、空孔率0%である場合の正極活物質層の厚み[B]を算出した。
(4)測定した正極活物質層の厚みと算出した正極活物質層の厚みとの差(A−B)から正極活物質層の空孔体積を算出し、正極活物質層1m3当たりの空孔体積を求め、得られた値の百分率を空孔率x[%]とした。
(Measurement of Porosity (x) of Positive Electrode Active Material Layer)
The porosity (x) of the positive electrode active material layer was measured as follows:
(1) The mass per unit area of the positive electrode active material layer was measured, and the mass of each material per unit area of the positive electrode active material layer was calculated from the compounding ratio of the materials.
(2) The thickness [A] of the positive electrode active material layer was measured using a micrometer.
(3) Using the mass of each material determined in (1) and the density of each material, the thickness [B] of the positive electrode active material layer when the porosity is 0% was calculated.
(4) The pore volume of the positive electrode active material layer was calculated from the difference (A-B) between the measured thickness of the positive electrode active material layer and the calculated thickness of the positive electrode active material layer, and the pore volume per 1 m3 of the positive electrode active material layer was determined. The percentage of the obtained value was defined as the porosity x [%].
(正極活物質層の体積に占めるゲル形成性ポリマーの体積の割合(y)の測定)
正極活物質層の体積に占めるゲル形成性ポリマーの体積の割合(y)については、得られた正極活物質層において、以下の式に基づき、正極活物質層の体積に占めるゲル形成性ポリマーの体積の割合y[%]を算出した:
ゲル形成性ポリマーの体積=(ゲル形成性ポリマーの質量)/(ゲル形成性ポリマーの密度)
ゲル形成性ポリマーの体積の割合(y)=(ゲル形成性ポリマーの体積)/[正極活物質層の総体積×(1−x/100)]。
(Measurement of the volume ratio (y) of the gel-forming polymer to the volume of the positive electrode active material layer)
Regarding the volume ratio (y) of the gel-forming polymer to the volume of the positive electrode active material layer, the volume ratio y [%] of the gel-forming polymer to the volume of the positive electrode active material layer obtained was calculated based on the following formula:
Volume of gel-forming polymer = (mass of gel-forming polymer) / (density of gel-forming polymer)
The volume ratio of the gel-forming polymer (y)=(volume of the gel-forming polymer)/[total volume of the positive electrode active material layer×(1−x/100)].
(電解液に対するゲル形成性ポリマーの吸液率(z)の測定)
電解液に対するゲル形成性ポリマーの吸液率(z)については、電解液への浸漬前および浸漬後のゲル形成性ポリマーの重量を測定して、以下の式により算出した:
吸液率(%)=[(電解液浸漬後のゲル形成性ポリマーの重量−電解液浸漬前のゲル形成性ポリマーの重量)/電解液浸漬前のゲル形成性ポリマーの重量]×100
この際、電解液としては、電池の作製に用いた電解液と同じものを使用した。
(Measurement of the absorption rate (z) of the gel-forming polymer for the electrolyte)
The liquid absorption rate (z) of the gel-forming polymer with respect to the electrolyte was calculated by measuring the weight of the gel-forming polymer before and after immersion in the electrolyte, using the following formula:
Liquid absorption rate (%)=[(weight of gel-forming polymer after immersion in electrolyte solution−weight of gel-forming polymer before immersion in electrolyte solution)/weight of gel-forming polymer before immersion in electrolyte solution]×100
In this case, the same electrolyte as that used in the production of the battery was used.
[実施例1]
(正極材料の調製)
正極活物質(リチウム酸化物)として酸化リチウム(Li2O、株式会社高純度化学研究所製)と、触媒として酸化コバルト(Co3O4、株式会社高純度化学研究所製)と、を別の70mL遊星ボールミル用のポットに入れ、それぞれ遊星ボールミル粉砕(粉砕条件:3mmφのジルコニアボール40gおよび15mmφのジルコニアボール15個を用いて回転数400rpmにて1時間処理)を行った。
[Example 1]
(Preparation of positive electrode material)
Lithium oxide (Li 2 O, manufactured by Kojundo Chemical Laboratory Co., Ltd.) as the positive electrode active material (lithium oxide) and cobalt oxide (Co 3 O 4 , manufactured by Kojundo Chemical Laboratory Co., Ltd.) as the catalyst were placed in a separate 70 mL planetary ball mill pot and each was ground using a planetary ball mill (grinding conditions: 40 g of 3 mm diameter zirconia balls and 15 g of 15 mm diameter zirconia balls at a rotation speed of 400 rpm for 1 hour).
次いで、粉砕された酸化リチウム5g、酸化コバルト15gを70mL遊星ボールミル用のポットに入れ、遊星ボールミル混合(混合条件:3mmφのジルコニアボール40gおよび15mmφのジルコニアボール15個を用いて回転数400rpmにて1時間処理)を行った。 Next, 5 g of crushed lithium oxide and 15 g of cobalt oxide were placed in a 70 mL planetary ball mill pot and mixed using a planetary ball mill (mixing conditions: 40 g of 3 mm diameter zirconia balls and 15 15 mm diameter zirconia balls, rotating at 400 rpm for 1 hour).
一方、ゲル形成性ポリマーであるPVdF−HFP(Kyner Flex 2501、Arkema製、ヘキサフルオロプロピレン由来の構成単位数の割合:6.9モル%;吸液率(z)=13[%])および溶媒である適量のN−メチル−2−ピロリドン(NMP、富士フイルム和光純薬株式会社製)を、遊星撹拌型混合混練装置「あわとり練太郎」(ARE−310、株式会社シンキー製)を用いて混錬(混錬条件:2000rpmにて5分間)し、PVdF−HFPをNMPに溶解した。このようにして得られたPVdF−HFPのNMP溶液に、上記でボールミル混合した酸化リチウムと酸化コバルトとの混合物および導電助剤であるアセチレンブラック(AB)(Li−400、デンカ株式会社製、平均一次粒子径:48nm、アスペクト比:1)を入れ、上記混合混練装置を用いてさらに混錬(混錬条件:2000rpmにて5分間)を行った。得られた混合液を金属トレイに移し、120℃に加温したホットプレートに置いてNMPを揮発させた。そして、残留した粉末を回収し、メノウ乳鉢で5分間手混ぜを行って、実施例1の正極材料を調製した。なお、本実施例の正極材料において、酸化リチウム:酸化コバルト:アセチレンブラック:PVdF−HFPの混合割合(質量比)は20:60:10:10であった。 Meanwhile, the gel-forming polymer PVdF-HFP (Kyner Flex 2501, manufactured by Arkema; proportion of hexafluoropropylene-derived structural units: 6.9 mol%; liquid absorption rate (z) = 13%]) and an appropriate amount of N-methyl-2-pyrrolidone (NMP, manufactured by Fujifilm Wako Pure Chemical Industries, Ltd.) as a solvent were kneaded (kneading conditions: 2000 rpm for 5 minutes) using a planetary stirring mixer/kneader "Awatori Rentaro" (ARE-310, manufactured by Thinky Corporation) to dissolve the PVdF-HFP in NMP. The resulting NMP solution of PVdF-HFP was mixed with the ball mill mixture of lithium oxide and cobalt oxide and the conductive additive acetylene black (AB) (Li-400, manufactured by Denka Co., Ltd., average primary particle size: 48 nm, aspect ratio: 1), and further mixed using the mixer/kneader (kneading conditions: 2000 rpm for 5 minutes). The resulting mixture was transferred to a metal tray and placed on a hot plate heated to 120°C to volatilize the NMP. The remaining powder was then collected and mixed by hand in an agate mortar for 5 minutes to prepare the positive electrode material of Example 1. In this example, the mixture ratio (mass ratio) of lithium oxide:cobalt oxide:acetylene black:PVdF-HFP was 20:60:10:10.
(正極の作製)
上記で調製した正極材料にNMPを固形分濃度が25質量%となるように添加して粘度を調整し、正極スラリーを作製した。平滑盤上に設置したアルミニウム箔の上に、正極活物質層の最終厚みが200μmとなるように、ドクターブレードを用いて正極スラリーを均一に塗布した。その後、80℃に加温したホットプレート上で30分間乾燥し、その後、得られた積層体に対して、ロールプレス機を用いてプレス処理を施した。次いで、真空乾燥機に移動させて真空下で130℃、8時間乾燥することで、アルミニウム箔の表面に正極活物質層が形成されてなる本実施例の正極を作製した。なお、正極活物質層の空孔率(x)は28[%]であった。また、正極活物質層の体積に占めるゲル形成性ポリマー(PVdF−HFP)の体積の割合(y)は12.2であった。その結果、yz/xの値は、12.2×13/28=5.7と算出された。
(Preparation of Positive Electrode)
NMP was added to the positive electrode material prepared above to adjust the solid content to 25% by mass, and the viscosity was adjusted to prepare a positive electrode slurry. The positive electrode slurry was uniformly applied to aluminum foil placed on a smooth plate using a doctor blade so that the final thickness of the positive electrode active material layer was 200 μm. The resulting laminate was then dried for 30 minutes on a hot plate heated to 80°C, and then pressed using a roll press. The laminate was then transferred to a vacuum dryer and dried under vacuum at 130°C for 8 hours to prepare a positive electrode of this example in which a positive electrode active material layer was formed on the surface of the aluminum foil. The porosity (x) of the positive electrode active material layer was 28%. The volume ratio (y) of the gel-forming polymer (PVdF-HFP) to the volume of the positive electrode active material layer was 12.2. As a result, the value of yz/x was calculated to be 12.2 × 13/28 = 5.7.
(クローズドタイプリチウム酸素電池(コインセル)の作製)
上記で作製した正極と対極リチウムとを対向させ、この間にセパレータ(ポリオレフィン、厚み:20μm)を配置した。次いで、正極、セパレータ、および対極リチウムの積層体をコインセル(CR2032、材質:ステンレス鋼(SUS316))に入れ、下記電解液をシリンジにより注入し、密閉して本実施例のクローズドタイプリチウム酸素電池(コインセル)を作製した。なお、上記電解液としては、エチレンカーボネート(EC)とジエチルカーボネート(DEC)とをEC:DEC=3:7(体積比)の割合で混合した有機溶媒に、リチウム塩である六フッ化リン酸リチウム(LiPF6)を1mol/Lの濃度で溶解させたものを用いた。
(Fabrication of closed-type lithium-oxygen batteries (coin cells))
The positive electrode and lithium counter electrode prepared above were placed opposite each other, and a separator (polyolefin, thickness: 20 μm) was placed between them. Next, the laminate of the positive electrode, separator, and lithium counter electrode was placed in a coin cell (CR2032, material: stainless steel (SUS316)), and the following electrolyte solution was injected using a syringe and sealed to prepare a closed-type lithium-oxygen battery (coin cell) of this example. The electrolyte used was an organic solvent mixture of ethylene carbonate (EC) and diethyl carbonate (DEC) in a ratio of EC:DEC = 3:7 (volume ratio), in which lithium hexafluorophosphate (LiPF 6 ), a lithium salt, was dissolved at a concentration of 1 mol/L.
[実施例2~実施例4]
正極活物質層の空孔率(x[%])および正極活物質層の体積に占めるゲル形成性ポリマーの体積の割合(y[%])が下記の表1に示す値となるようにプレス処理の条件を変更したこと以外は、上述した実施例1と同じ方法を用いて、これらの実施例のクローズドタイプリチウム酸素電池(コインセル)を作製した。
[Examples 2 to 4]
The closed-type lithium-oxygen batteries (coin cells) of these Examples were produced using the same method as in Example 1 described above, except that the conditions for the pressing treatment were changed so that the porosity (x [%]) of the positive electrode active material layer and the volume ratio (y [%]) of the gel-forming polymer to the volume of the positive electrode active material layer were the values shown in Table 1 below.
[実施例5]
正極活物質(リチウム酸化物)および触媒(酸化コバルト)の使用量を下記の表1に示す値に変更し、かつ、正極活物質層の空孔率(x[%])および正極活物質層の体積に占めるゲル形成性ポリマーの体積の割合(y[%])が下記の表1に示す値となるようにプレス処理の条件を変更したこと以外は、上述した実施例1と同じ方法を用いて、本実施例のクローズドタイプリチウム酸素電池(コインセル)を作製した。
[Example 5]
The closed-type lithium-oxygen battery (coin cell) of this example was produced using the same method as in Example 1 described above, except that the amounts of the positive electrode active material (lithium oxide) and the catalyst (cobalt oxide) used were changed to the values shown in Table 1 below, and the conditions of the pressing treatment were changed so that the porosity (x [%]) of the positive electrode active material layer and the volume ratio (y [%]) of the gel-forming polymer to the volume of the positive electrode active material layer were the values shown in Table 1 below.
[実施例6]
ゲル形成性ポリマーとして、PVdF−HFP(Kyner Flex 2501)に代えてPVdF−HFP(Kyner Flex 2851、Arkema製、ヘキサフルオロプロピレン由来の構成単位数の割合:2.4モル%;吸液率(z)=45[%])を用い、かつ、正極活物質層の空孔率(x[%])および正極活物質層の体積に占めるゲル形成性ポリマーの体積の割合(y[%])が下記の表1に示す値となるようにプレス処理の条件を変更したこと以外は、上述した実施例1と同じ方法を用いて、本実施例のクローズドタイプリチウム酸素電池(コインセル)を作製した。
[Example 6]
A closed-type lithium-oxygen battery (coin cell) of this example was produced using the same method as in Example 1 described above, except that PVdF-HFP (Kyner Flex 2501) was replaced with PVdF-HFP (Kyner Flex 2851, manufactured by Arkema; proportion of the number of constitutional units derived from hexafluoropropylene: 2.4 mol %; liquid absorption rate (z)=45[%]) as the gel-forming polymer, and the conditions of the pressing treatment were changed so that the porosity (x[%]) of the positive electrode active material layer and the volume ratio (y[%]) of the gel-forming polymer to the volume of the positive electrode active material layer were the values shown in Table 1 below.
[実施例7]
ゲル形成性ポリマーとして、PVdF−HFP(Kyner Flex 2501)に代えてPVDF(クレハKFポリマーW#9700、クレハ製;吸液率(z)=95[%])を用い、かつ、正極活物質層の空孔率(x[%])および正極活物質層の体積に占めるゲル形成性ポリマーの体積の割合(y[%])が下記の表1に示す値となるようにプレス処理の条件を変更したこと以外は、上述した実施例5と同じ方法を用いて、本実施例のクローズドタイプリチウム酸素電池(コインセル)を作製した。
[Example 7]
A closed-type lithium-oxygen battery (coin cell) of this example was produced using the same method as in Example 5 described above, except that PVDF (Kureha KF Polymer W#9700, manufactured by Kureha; liquid absorption rate (z)=95[%]) was used as the gel-forming polymer instead of PVdF-HFP (Kyner Flex 2501), and the conditions for the press treatment were changed so that the porosity (x[%]) of the positive electrode active material layer and the volume ratio (y[%]) of the gel-forming polymer to the volume of the positive electrode active material layer were the values shown in Table 1 below.
[比較例1]
正極活物質(リチウム酸化物)、触媒(酸化コバルト)およびゲル形成性ポリマー(PVdF−HFP)の使用量を下記の表1に示す値に変更し、かつ、正極活物質層の空孔率(x[%])および正極活物質層の体積に占めるゲル形成性ポリマーの体積の割合(y[%])が下記の表1に示す値となるようにプレス処理の条件を変更したこと以外は、上述した実施例1と同じ方法を用いて、本比較例のクローズドタイプリチウム酸素電池(コインセル)を作製した。
[Comparative Example 1]
A closed-type lithium-oxygen battery (coin cell) of this comparative example was produced using the same method as in Example 1 described above, except that the amounts of the positive electrode active material (lithium oxide), catalyst (cobalt oxide), and gel-forming polymer (PVdF-HFP) used were changed to the values shown in Table 1 below, and the conditions of the pressing process were changed so that the porosity (x [%]) of the positive electrode active material layer and the volume ratio (y [%]) of the gel-forming polymer to the volume of the positive electrode active material layer were the values shown in Table 1 below.
[比較例2]
ゲル形成性ポリマーとして、PVdF−HFP(Kyner Flex 2501)に代えてPVDF(クレハKFポリマーW#7200、クレハ製;吸液率(z)=120[%])を用い、かつ、正極活物質層の空孔率(x[%])および正極活物質層の体積に占めるゲル形成性ポリマーの体積の割合(y[%])が下記の表1に示す値となるようにプレス処理の条件を変更したこと以外は、上述した実施例5と同じ方法を用いて、本比較例のクローズドタイプリチウム酸素電池(コインセル)を作製した。
[Comparative Example 2]
A closed-type lithium-oxygen battery (coin cell) of this comparative example was produced using the same method as in Example 5 described above, except that PVDF (Kureha KF Polymer W#7200, manufactured by Kureha; liquid absorption rate (z) = 120 [%]) was used as the gel-forming polymer instead of PVdF-HFP (Kyner Flex 2501), and the conditions for the press treatment were changed so that the porosity (x [%]) of the positive electrode active material layer and the volume ratio (y [%]) of the gel-forming polymer to the volume of the positive electrode active material layer were the values shown in Table 1 below.
《コインセルの評価(初回充放電効率の測定)》
上記で作製した実施例および比較例のクローズドタイプリチウム酸素電池(コインセル)について、300K(27℃)に設定された恒温槽内で以下の充放電試験(初回充放電)を行い、その際の充電容量および放電容量をそれぞれ測定した。そして、充電容量に対する放電容量の比を算出し、初回充放電効率とした。結果を下記の表1に示す。なお、表1に示す初回充放電効率の値は、比較例2の測定値を100とした場合の相対値である。
<Coin cell evaluation (measurement of initial charge/discharge efficiency)>
The closed-type lithium-oxygen batteries (coin cells) of the Examples and Comparative Examples prepared above were subjected to the following charge-discharge test (initial charge-discharge) in a thermostatic chamber set at 300 K (27°C), and the charge capacity and discharge capacity were measured. The ratio of the discharge capacity to the charge capacity was calculated to define the initial charge-discharge efficiency. The results are shown in Table 1 below. The initial charge-discharge efficiency values shown in Table 1 are relative values, with the measured value for Comparative Example 2 set to 100.
(充放電試験条件)
充放電試験機:
TOSCAT−3000、型式TYS−30TU10(東洋システム株式会社製)
充放電条件:
[充電過程]0.02C(電流密度18mA/g)、1.8V→4.6V(CCCV;0.01Cカットオフ)
[放電過程]0.02C(電流密度18mA/g)、4.6V→1.8V(CC)
充電過程と放電過程との間の休止時間:30分間。
(Charge/discharge test conditions)
Charge/discharge tester:
TOSCAT-3000, model TYS-30TU10 (manufactured by Toyo Systems Co., Ltd.)
Charge/discharge conditions:
[Charging process] 0.02 C (current density 18 mA / g), 1.8 V → 4.6 V (CCCV; 0.01 C cutoff)
[Discharge process] 0.02C (current density 18mA/g), 4.6V → 1.8V (CC)
Rest time between charging and discharging processes: 30 minutes.
表1に示す結果から、本発明によれば、電極活物質層に酸化リチウム(Li2O)および触媒に加えてゲル形成性ポリマーを含ませるとともに、上記パラメータ(x、y、z)を所定の関係に制御することで、クローズドタイプリチウム酸素電池の充放電効率を向上させうることがわかる。 The results shown in Table 1 show that, according to the present invention, the charge/discharge efficiency of a closed-type lithium-oxygen battery can be improved by incorporating a gel-forming polymer in addition to lithium oxide (Li 2 O) and a catalyst into the electrode active material layer and by controlling the above parameters (x, y, z) to have a predetermined relationship.
10a 積層型リチウム酸素電池、
11’ 正極集電体
12 負極集電体
13 正極活物質層、
15 負極活物質層、
17 電解質層、
19 単電池層、
21 発電要素、
25 正極集電板(正極タブ)、
27 負極集電板(負極タブ)、
29 ラミネートフィルム。
10a: stacked lithium-oxygen battery;
11′ positive electrode current collector 12 negative electrode current collector 13 positive electrode active material layer,
15 negative electrode active material layer,
17 electrolyte layer,
19 cell layer,
21 power generating element,
25 Positive electrode current collector (positive electrode tab),
27 negative electrode current collector plate (negative electrode tab),
29 Laminating film.
Claims (11)
前記電極活物質層の空孔率をx[%]とし、前記電極活物質層の体積に占める前記ゲル形成性ポリマーの体積の割合をy[%]とし、前記電解液に対する前記ゲル形成性ポリマーの吸液率をz[%]としたとき、下記式(1)の関係を満たす、クローズドタイプリチウム酸素電池:
0<yz/x≦8.7 ・・・式(1) The battery comprises an electrode in which an electrode active material layer containing lithium oxide, a catalyst, and a gel-forming polymer is disposed on the surface of a current collector, and an electrolyte layer in which a separator disposed adjacent to the electrode is impregnated with an electrolytic solution,
A closed-type lithium-oxygen battery, wherein the relationship of the following formula (1) is satisfied when the porosity of the electrode active material layer is x [%], the volume ratio of the gel-forming polymer to the volume of the electrode active material layer is y [%], and the liquid absorption rate of the gel-forming polymer with respect to the electrolyte is z [%]:
0<yz/x≦8.7 Formula (1)
1.4≦yz/x≦8.7 ・・・式(2) The closed-type lithium-oxygen battery according to claim 1, further satisfying the following formula (2):
1.4≦yz/x≦8.7...Formula (2)
3.2≦yz/x≦5.7 ・・・式(3) The closed-type lithium-oxygen battery according to claim 2, further satisfying the following formula (3):
3.2≦yz/x≦5.7...Formula (3)
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Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2012138290A (en) * | 2010-12-27 | 2012-07-19 | Toyota Motor Corp | Lithium secondary battery system and method for controlling the lithium secondary battery system |
| KR20140066517A (en) * | 2012-11-23 | 2014-06-02 | 에스케이이노베이션 주식회사 | Lithium air battery |
| JP2019046785A (en) * | 2017-08-31 | 2019-03-22 | パナソニックIpマネジメント株式会社 | Lithium air battery |
| JP2019057489A (en) * | 2017-09-13 | 2019-04-11 | パナソニックIpマネジメント株式会社 | Positive electrode for air cell and air cell |
| KR20200099822A (en) * | 2019-02-15 | 2020-08-25 | 주식회사 유뱃 | Electrochemical device and manufacturing method thereof |
-
2024
- 2024-04-08 WO PCT/IB2024/000150 patent/WO2025215390A1/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2012138290A (en) * | 2010-12-27 | 2012-07-19 | Toyota Motor Corp | Lithium secondary battery system and method for controlling the lithium secondary battery system |
| KR20140066517A (en) * | 2012-11-23 | 2014-06-02 | 에스케이이노베이션 주식회사 | Lithium air battery |
| JP2019046785A (en) * | 2017-08-31 | 2019-03-22 | パナソニックIpマネジメント株式会社 | Lithium air battery |
| JP2019057489A (en) * | 2017-09-13 | 2019-04-11 | パナソニックIpマネジメント株式会社 | Positive electrode for air cell and air cell |
| KR20200099822A (en) * | 2019-02-15 | 2020-08-25 | 주식회사 유뱃 | Electrochemical device and manufacturing method thereof |
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