WO2015092959A1 - リチウム硫黄二次電池 - Google Patents
リチウム硫黄二次電池 Download PDFInfo
- Publication number
- WO2015092959A1 WO2015092959A1 PCT/JP2014/005237 JP2014005237W WO2015092959A1 WO 2015092959 A1 WO2015092959 A1 WO 2015092959A1 JP 2014005237 W JP2014005237 W JP 2014005237W WO 2015092959 A1 WO2015092959 A1 WO 2015092959A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- positive electrode
- negative electrode
- sulfur
- lithium
- separator
- Prior art date
Links
Images
Classifications
-
- 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
-
- 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
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/58—Selection of substances as active materials, active masses, active liquids of inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFy; of polyanionic structures, e.g. phosphates, silicates or borates
- H01M4/583—Carbonaceous material, e.g. graphite-intercalation compounds or CFx
- H01M4/587—Carbonaceous material, e.g. graphite-intercalation compounds or CFx for inserting or intercalating light metals
-
- 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
-
- 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
- H01M10/0525—Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
-
- 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
- H01M10/056—Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes
- H01M10/0564—Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes the electrolyte being constituted of organic materials only
- H01M10/0566—Liquid materials
- H01M10/0567—Liquid materials characterised by the additives
-
- 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
- H01M10/058—Construction or manufacture
-
- 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
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/362—Composites
- H01M4/366—Composites as layered products
-
- 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
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/38—Selection of substances as active materials, active masses, active liquids of elements or alloys
-
- 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
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/58—Selection of substances as active materials, active masses, active liquids of inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFy; of polyanionic structures, e.g. phosphates, silicates or borates
- H01M4/581—Chalcogenides or intercalation compounds thereof
- H01M4/5815—Sulfides
-
- 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
- H01M4/64—Carriers or collectors
- H01M4/66—Selection of materials
- H01M4/663—Selection of materials containing carbon or carbonaceous materials as conductive part, e.g. graphite, carbon fibres
-
- 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
- H01M4/64—Carriers or collectors
- H01M4/70—Carriers or collectors characterised by shape or form
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/409—Separators, membranes or diaphragms characterised by the material
- H01M50/44—Fibrous material
-
- 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
- H01M10/056—Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes
- H01M10/0564—Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes the electrolyte being constituted of organic materials only
- H01M10/0566—Liquid materials
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/409—Separators, membranes or diaphragms characterised by the material
- H01M50/411—Organic material
- H01M50/414—Synthetic resins, e.g. thermoplastics or thermosetting resins
- H01M50/417—Polyolefins
-
- 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
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
-
- 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
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
- Y02T10/60—Other road transportation technologies with climate change mitigation effect
- Y02T10/70—Energy storage systems for electromobility, e.g. batteries
Definitions
- the present invention relates to a lithium-sulfur secondary battery.
- lithium secondary batteries Since lithium secondary batteries have a high energy density, they are used not only for mobile devices such as mobile phones and personal computers, but also for hybrid vehicles, electric vehicles, power storage and storage systems, and the like. As one of such lithium secondary batteries, a lithium-sulfur secondary battery that is charged and discharged by a reaction between lithium and sulfur has recently attracted attention.
- a lithium-sulfur secondary battery includes a positive electrode having a positive electrode active material containing sulfur, a negative electrode having a negative electrode active material containing lithium, and a separator that is disposed between the positive electrode and the negative electrode and holds an electrolytic solution. For example, it is known from Patent Document 1.
- a plurality of carbon nanotubes are oriented on the current collector surface of the positive electrode in a direction perpendicular to the surface, and each surface of the carbon nanotubes is covered with sulfur. This is known, for example, from Patent Document 2.
- the polysulfide diffused to the negative electrode side does not contribute to the charge / discharge reaction, and the amount of sulfur in the positive electrode decreases, resulting in a decrease in charge / discharge capacity. Further, when polysulfide reacts with lithium of the negative electrode, the charging reaction is not accelerated (so-called redox shuttle phenomenon occurs), and the charge / discharge efficiency is also lowered.
- an object of the present invention is to provide a lithium-sulfur secondary battery that can suppress the diffusion of polysulfide eluted in the electrolyte into the negative electrode and suppress the decrease in charge / discharge capacity.
- the present invention includes a positive electrode having a positive electrode active material containing sulfur, a negative electrode having a negative electrode active material containing lithium, and a separator disposed between the positive electrode and the negative electrode to hold an electrolyte.
- This lithium-sulfur secondary battery is characterized in that a polymer nonwoven fabric having a sulfone group is disposed between at least one of the separator and the positive electrode and between the separator and the negative electrode.
- the separator and the polymer nonwoven fabric having a sulfone group may be in contact with each other or may be separated by a predetermined distance.
- the polymer nonwoven fabric is made of polypropylene or polyethylene.
- the separator allows the passage of polysulfide
- the polysulfide generated at the positive electrode is eluted into the electrolyte
- the polysulfide diffuses to the negative electrode side through the separator, and the charge / discharge capacity is reduced due to the decrease in the amount of sulfur in the positive electrode. cause. Therefore, the present inventors have intensively studied and have come to know that a polymer nonwoven fabric having a sulfone group suppresses passage of polysulfide while allowing passage of lithium ions.
- the polymer non-woven fabric having a sulfone group is disposed on at least one of the positive electrode side and the negative electrode side of the separator, it is possible to prevent the polysulfide eluted in the electrolyte from diffusing into the negative electrode, thereby reducing the charge / discharge capacity. Can be suppressed.
- a positive electrode includes a current collector and a plurality of carbon nanotubes oriented in a direction perpendicular to the surface of the current collector, and the surface of each carbon nanotube is covered with sulfur. It is preferable to apply to a case. In this case, the amount of sulfur is greater than that applied to the surface of the current collector, and the polysulfide is more easily eluted in the electrolyte, but if the present invention is applied, the polysulfide diffuses to the negative electrode side. It can be effectively suppressed.
- FIG. 2 is a schematic cross-sectional view showing an enlargement of the positive electrode shown in FIG. 1.
- the graph which shows the experimental result (cycle characteristic of a discharge capacity maintenance factor) for confirming the effect of this invention.
- B is a lithium-sulfur secondary battery
- the lithium-sulfur secondary battery B includes a positive electrode P having a positive electrode active material containing sulfur, a negative electrode N having a negative electrode active material containing lithium, and these positive electrodes P, And a separator S which is disposed between the negative electrodes N and holds the electrolytic solution L.
- the positive electrode P includes a positive electrode current collector P1 and a positive electrode active material layer P2 formed on the surface of the positive electrode current collector P1.
- the positive electrode current collector P1 includes, for example, a base 1, a base film (also referred to as “barrier film”) 2 formed on the surface of the base 1 with a film thickness of 5 to 50 nm, and 0.5 on the base film 2. And a catalyst layer 3 having a thickness of ⁇ 5 nm.
- a metal foil or a metal mesh made of Ni, Cu, or Pt can be used as the substrate 1, for example, a metal foil or a metal mesh made of Ni, Cu, or Pt can be used.
- the base film 2 is for improving the adhesion between the substrate 1 and a carbon nanotube 4 described later.
- the catalyst layer 3 is made of at least one metal selected from, for example, Ni, Fe, or Co.
- the positive electrode active material layer P2 includes a surface of the positive electrode current collector P1, a large number of carbon nanotubes 4 grown by being oriented in a direction orthogonal to the surface, and sulfur 5 covering the entire surface of each of the carbon nanotubes 4. Composed. There is a gap between the carbon nanotubes 4 covered with sulfur 5, and an electrolyte solution L (described later) is allowed to flow into this gap.
- each of the carbon nanotubes 4 is advantageously of a high aspect ratio having a length in the range of 100 to 1000 ⁇ m and a diameter in the range of 5 to 50 nm, for example.
- the thickness of the sulfur 5 covering the entire surface of each carbon nanotube 4 is preferably in the range of 1 to 3 nm, for example.
- the positive electrode P can be formed by the following method. That is, the Al film as the base film 2 and the Ni film as the catalyst layer 3 are sequentially formed on the surface of the Ni foil as the substrate 1 to obtain the positive electrode current collector P1.
- a method for forming the base film 2 and the catalyst layer 3 for example, a known electron beam evaporation method, a sputtering method, or a dipping using a solution of a compound containing a catalyst metal can be used. To do.
- the obtained positive electrode current collector P1 was placed in a processing chamber of a known CVD apparatus, and a mixed gas containing a raw material gas and a dilution gas was supplied into the processing chamber under an operating pressure of 100 Pa to atmospheric pressure, and a temperature of 600 to 800 ° C.
- a mixed gas containing a raw material gas and a dilution gas was supplied into the processing chamber under an operating pressure of 100 Pa to atmospheric pressure, and a temperature of 600 to 800 ° C.
- the carbon nanotubes 4 are grown on the surface of the current collector P1 so as to be oriented perpendicular to the surface.
- a CVD method for growing the carbon nanotubes 4 a thermal CVD method, a plasma CVD method, or a hot filament CVD method can be used.
- source gas hydrocarbons, such as methane, ethylene, and acetylene, alcohol, such as methanol and ethanol, can be used, for example, and nitrogen, argon, or hydrogen can be used as dilution gas.
- the flow rates of the source gas and the dilution gas can be appropriately set according to the volume of the processing chamber. For example, the flow rate of the source gas can be set within a range of 10 to 500 sccm, and the flow rate of the dilution gas can be set within a range of 100 to 5000 sccm. It can be set with.
- the weight of the sulfur to be arranged can be set according to the density of the carbon nanotubes 4.
- the weight of sulfur is preferably set to 0.7 to 3 times the weight of the carbon nanotubes 4.
- the positive electrode P thus formed has a weight (impregnation amount) of sulfur 5 per unit area of the carbon nanotube 4 of 2.0 mg / cm 2 or more.
- the negative electrode N for example, Li and Al or In alloy, or Si, SiO, Sn, SnO 2 or hard carbon doped with lithium ions can be used in addition to Li alone.
- the separator S is composed of a porous film made of a resin such as polyethylene or polypropylene, or a non-woven fabric, and can conduct lithium ions (Li + ) between the positive electrode P and the negative electrode N through the electrolytic solution L. Yes.
- polysulfide is generated while sulfur and lithium are reacted in multiple stages.
- Polysulfide especially Li 2 S 4 or Li 2 S 6
- the separator S allows passage of polysulfide.
- the polysulfide eluted in the electrolyte L passes through the separator S and diffuses to the negative electrode side, causing a decrease in capacity due to a decrease in the amount of sulfur in the positive electrode. For this reason, it is important how to suppress the diffusion of polysulfide to the negative electrode side.
- the present inventor has conducted extensive research and has come to know that a polymer nonwoven fabric having a sulfone group suppresses passage of polysulfide while allowing passage of lithium ions.
- the polymer nonwoven fabric F which has a sulfone group was arrange
- the polymer nonwoven fabric F those made of polypropylene or polyethylene can be used. If such a structure is adopted, since polysulfide eluted in the electrolyte L does not easily pass through the polymer nonwoven fabric F, diffusion of polysulfide to the negative electrode side can be suppressed, and a decrease in charge / discharge capacity can be suppressed.
- the electrolytic solution L includes an electrolyte and a solvent that dissolves the electrolyte.
- the electrolyte known lithium bis (trifluoromethanesulfonyl) imide (hereinafter referred to as “LiTFSI”), LiPF 6 , LiBF 4, or the like can be used.
- the solvent known solvents can be used, for example, selected from ethers such as tetrahydrofuran, glyme, diglyme, triglyme, tetraglyme, diethoxyethane (DEE) and dimethoxyethane (DME). At least one kind can be used.
- dioxolane DOL
- the mixing ratio of diethoxyethane and dioxolane can be set to 9: 1.
- lithium nitrate may be added to the electrolytic solution L in order to form a coating on the negative electrode surface that inhibits the passage of polysulfide while allowing the passage of lithium ions.
- the positive electrode P was prepared as follows. That is, the substrate 1 is a Ni foil having a diameter of 14 mm ⁇ and a thickness of 0.020 mm, an Al film as a base film 2 is formed on the Ni foil 1 with a thickness of 15 nm by an electron beam evaporation method, and a catalyst is formed on the Al film 2.
- the Fe film as the layer 3 was formed by electron beam evaporation with a film thickness of 5 nm to obtain a positive electrode current collector P1.
- the obtained positive electrode current collector P1 was placed in a processing chamber of a thermal CVD apparatus, acetylene 200 sccm and nitrogen 1000 sccm were supplied into the processing chamber, operating pressure: 1 atm, temperature: 750 ° C., growth time: 10 minutes
- the carbon nanotubes 4 were grown to a length of 800 ⁇ m by vertically aligning on the surface of the positive electrode current collector P1.
- Granular sulfur was placed on the carbon nanotubes 4 and placed in a tubular furnace, and heated at 120 ° C. for 5 minutes in an Ar atmosphere to cover the carbon nanotubes 4 with sulfur 5 to produce a positive electrode P. .
- the weight (impregnation amount) of sulfur 5 per unit area of the carbon nanotube 4 was 4 mg / cm 2 .
- the negative electrode N was made of metallic lithium having a diameter of 15 mm ⁇ and a thickness of 0.6 mm, and the separator S was made of a porous film made of polypropylene.
- the positive electrode P and the negative electrode N are opposed to each other through the separator S, a polypropylene non-woven fabric F having a sulfone group is disposed between the separator S and the negative electrode N, and the electrolytic solution L is held in the separator S so that the lithium sulfur secondary A battery coin cell was prepared.
- the electrolytic solution L was prepared by dissolving LiTFSI as an electrolyte in a mixed solution of diethoxyethane (DEE) and dioxolane (DOL) (mixing ratio 9: 1) to adjust the concentration to 1 mol / l.
- the one to which lithium nitrate was added was used.
- the coin cell thus produced was regarded as an invention. Moreover, it replaced with the polypropylene nonwoven fabric F which has a sulfone group, and the coin cell produced similarly to the said invention product was made into the comparative product 1 except the point which has arrange
- FIG. FIG. 3 shows the discharge capacity retention rate (the discharge capacity at the second cycle is 100%) when the discharge current density is measured at 0.5 mA / cm 2 for these invention products and comparative products 1 and 2, respectively.
- the invention product can suppress a decrease in charge / discharge capacity more than the comparative products 1 and 2. This is considered to be because the diffusion of polysulfide to the negative electrode side was suppressed by the polypropylene nonwoven fabric F having a sulfone group.
- the comparison product 1 has a larger decrease in charge / discharge capacity than the comparison product 2. This is considered to be due to the fact that the lithium ion conductivity was lowered by disposing a polypropylene non-woven fabric having no sulfone group.
- the embodiment of the present invention has been described above, but the present invention is not limited to the above.
- the shape of the lithium-sulfur secondary battery is not particularly limited, and may be a button type, a sheet type, a laminated type, a cylindrical type, or the like other than the coin cell.
- the nonwoven fabric F was arrange
- a nonwoven fabric can be disposed between both the separator S and the positive electrode P and between the separator S and the negative electrode N.
- B Lithium sulfur secondary battery
- P positive electrode
- N negative electrode
- L electrolyte
- P1 current collector
- 1 substrate
- 4 carbon nanotube
- 5 sulfur.
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Inorganic Chemistry (AREA)
- Condensed Matter Physics & Semiconductors (AREA)
- General Physics & Mathematics (AREA)
- Physics & Mathematics (AREA)
- Composite Materials (AREA)
- Secondary Cells (AREA)
- Cell Separators (AREA)
- Battery Electrode And Active Subsutance (AREA)
- Cell Electrode Carriers And Collectors (AREA)
Abstract
Description
Claims (2)
- 硫黄を含む正極活物質を有する正極と、リチウムを含む負極活物質を有する負極と、正極と負極との間に配置されて電解液を保持するセパレータとを備えるリチウム硫黄二次電池において、
セパレータと正極との間、及びセパレータと負極との間の少なくとも一方に、スルホン基を有する高分子不織布を配置したことを特徴とするリチウム硫黄二次電池。 - 前記正極は、集電体と、集電体の表面に、当該表面に直交する方向に配向させた複数本のカーボンナノチューブとを備え、隣接するカーボンナノチューブ相互間に所定の間隙が存するように、カーボンナノチューブの各々の表面を硫黄で覆ってなることを特徴とする請求項1記載のリチウム硫黄二次電池。
Priority Applications (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2015553345A JPWO2015092959A1 (ja) | 2013-12-18 | 2014-10-15 | リチウム硫黄二次電池 |
DE112014005918.8T DE112014005918T5 (de) | 2013-12-18 | 2014-10-15 | Lithium-Schwefel-Akkumulator |
KR1020167018813A KR20160100333A (ko) | 2013-12-18 | 2014-10-15 | 리튬 유황 이차전지 |
US15/101,526 US20170005312A1 (en) | 2013-12-18 | 2014-10-15 | Lithium-Sulfur Secondary Battery |
CN201480067929.4A CN105830273A (zh) | 2013-12-18 | 2014-10-15 | 锂硫二次电池 |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2013261070 | 2013-12-18 | ||
JP2013-261070 | 2013-12-18 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2015092959A1 true WO2015092959A1 (ja) | 2015-06-25 |
Family
ID=53402346
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/JP2014/005237 WO2015092959A1 (ja) | 2013-12-18 | 2014-10-15 | リチウム硫黄二次電池 |
Country Status (7)
Country | Link |
---|---|
US (1) | US20170005312A1 (ja) |
JP (1) | JPWO2015092959A1 (ja) |
KR (1) | KR20160100333A (ja) |
CN (1) | CN105830273A (ja) |
DE (1) | DE112014005918T5 (ja) |
TW (1) | TW201530871A (ja) |
WO (1) | WO2015092959A1 (ja) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2016119165A (ja) * | 2014-12-18 | 2016-06-30 | 株式会社アルバック | アルカリ金属−硫黄電池用正極及びこれを備えた二次電池の製造方法 |
KR20170001375A (ko) * | 2015-06-26 | 2017-01-04 | 주식회사 엘지화학 | 리튬 황 전지 및 이의 제조방법 |
JP2019522316A (ja) * | 2016-09-09 | 2019-08-08 | エルジー・ケム・リミテッド | リチウム−硫黄電池 |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109103418B (zh) * | 2018-08-23 | 2021-04-13 | 宁德新能源科技有限公司 | 电极及包含所述电极的电池 |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2000268799A (ja) * | 1999-03-15 | 2000-09-29 | Mitsubishi Chemicals Corp | リチウムイオン二次電池 |
JP2002025527A (ja) * | 2000-07-03 | 2002-01-25 | Japan Storage Battery Co Ltd | 非水電解液二次電池 |
JP2002532852A (ja) * | 1998-12-17 | 2002-10-02 | モルテック コーポレイション | 電気化学セル用セパレーターのための保護コーティング |
WO2012070184A1 (ja) * | 2010-11-26 | 2012-05-31 | 株式会社アルバック | リチウム硫黄二次電池用の正極及びその形成方法 |
WO2013087348A2 (de) * | 2011-12-16 | 2013-06-20 | Robert Bosch Gmbh | Lithium-schwefel-zellen-separator mit polysulfidsperrschicht |
JP2013539193A (ja) * | 2010-10-07 | 2013-10-17 | バッテル メモリアル インスティチュート | 充電式リチウム−硫黄電池電極用のグラフェン−硫黄ナノ複合体 |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5213722A (en) * | 1987-11-17 | 1993-05-25 | Matsushita Electric Industrial Co., Ltd. | Method of making a separator material for a storage battery |
JP3532168B2 (ja) * | 2001-06-20 | 2004-05-31 | トーヨーキッチンアンドリビング株式会社 | スライドパネル式収納家具 |
JP2008041606A (ja) * | 2006-08-10 | 2008-02-21 | Matsushita Electric Ind Co Ltd | 非水電解質電池用セパレータ及び非水電解質電池 |
JP2012070184A (ja) | 2010-09-22 | 2012-04-05 | Fujitsu Ten Ltd | 放送受信装置 |
FR2977722B1 (fr) * | 2011-07-05 | 2014-03-14 | Commissariat Energie Atomique | Separateur d'electrodes pour accumulateur au lithium/soufre |
JP2013114920A (ja) | 2011-11-29 | 2013-06-10 | Toyota Central R&D Labs Inc | リチウム硫黄電池 |
US9093710B2 (en) * | 2012-01-18 | 2015-07-28 | E I Du Pont De Nemours And Company | Compositions, layerings, electrodes and methods for making |
WO2013126864A1 (en) * | 2012-02-23 | 2013-08-29 | E. I. Du Pont De Nemours And Company | Compositions, layerings, electrodes and methods for making |
-
2014
- 2014-10-15 KR KR1020167018813A patent/KR20160100333A/ko not_active Application Discontinuation
- 2014-10-15 DE DE112014005918.8T patent/DE112014005918T5/de not_active Withdrawn
- 2014-10-15 US US15/101,526 patent/US20170005312A1/en not_active Abandoned
- 2014-10-15 CN CN201480067929.4A patent/CN105830273A/zh active Pending
- 2014-10-15 WO PCT/JP2014/005237 patent/WO2015092959A1/ja active Application Filing
- 2014-10-15 JP JP2015553345A patent/JPWO2015092959A1/ja active Pending
- 2014-10-29 TW TW103137429A patent/TW201530871A/zh unknown
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002532852A (ja) * | 1998-12-17 | 2002-10-02 | モルテック コーポレイション | 電気化学セル用セパレーターのための保護コーティング |
JP2000268799A (ja) * | 1999-03-15 | 2000-09-29 | Mitsubishi Chemicals Corp | リチウムイオン二次電池 |
JP2002025527A (ja) * | 2000-07-03 | 2002-01-25 | Japan Storage Battery Co Ltd | 非水電解液二次電池 |
JP2013539193A (ja) * | 2010-10-07 | 2013-10-17 | バッテル メモリアル インスティチュート | 充電式リチウム−硫黄電池電極用のグラフェン−硫黄ナノ複合体 |
WO2012070184A1 (ja) * | 2010-11-26 | 2012-05-31 | 株式会社アルバック | リチウム硫黄二次電池用の正極及びその形成方法 |
WO2013087348A2 (de) * | 2011-12-16 | 2013-06-20 | Robert Bosch Gmbh | Lithium-schwefel-zellen-separator mit polysulfidsperrschicht |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2016119165A (ja) * | 2014-12-18 | 2016-06-30 | 株式会社アルバック | アルカリ金属−硫黄電池用正極及びこれを備えた二次電池の製造方法 |
KR20170001375A (ko) * | 2015-06-26 | 2017-01-04 | 주식회사 엘지화학 | 리튬 황 전지 및 이의 제조방법 |
KR101994877B1 (ko) * | 2015-06-26 | 2019-07-01 | 주식회사 엘지화학 | 리튬 황 전지 및 이의 제조방법 |
JP2019522316A (ja) * | 2016-09-09 | 2019-08-08 | エルジー・ケム・リミテッド | リチウム−硫黄電池 |
Also Published As
Publication number | Publication date |
---|---|
DE112014005918T5 (de) | 2016-09-08 |
CN105830273A (zh) | 2016-08-03 |
US20170005312A1 (en) | 2017-01-05 |
KR20160100333A (ko) | 2016-08-23 |
TW201530871A (zh) | 2015-08-01 |
JPWO2015092959A1 (ja) | 2017-03-16 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
KR101502538B1 (ko) | 리튬 유황 2차 전지용의 양극 및 그 형성 방법 | |
WO2015083314A1 (ja) | リチウム硫黄二次電池 | |
WO2015092959A1 (ja) | リチウム硫黄二次電池 | |
JP2014203593A (ja) | リチウム硫黄二次電池用の正極及びその形成方法 | |
KR101849754B1 (ko) | 리튬 유황 이차전지용 양극 및 그 형성방법 | |
JP6422070B2 (ja) | リチウム硫黄二次電池用正極の形成方法 | |
JP2017004605A (ja) | リチウム硫黄二次電池及びセパレータの製造方法 | |
JP6210869B2 (ja) | リチウム硫黄二次電池用の正極及びその形成方法 | |
JP2015115270A (ja) | リチウム硫黄二次電池 | |
JP6298625B2 (ja) | リチウム硫黄二次電池用の正極の形成方法及びリチウム硫黄二次電池用正極 | |
US9997770B2 (en) | Lithium-sulfur secondary battery | |
JP2015115209A (ja) | リチウム硫黄二次電池 | |
US20220115638A1 (en) | Metallic lithium based battery electrodes, formation thereof, and uses thereof | |
CN115642370A (zh) | 锂硫电池用夹层材料及其制备方法和应用 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
121 | Ep: the epo has been informed by wipo that ep was designated in this application |
Ref document number: 14871213 Country of ref document: EP Kind code of ref document: A1 |
|
ENP | Entry into the national phase |
Ref document number: 2015553345 Country of ref document: JP Kind code of ref document: A |
|
WWE | Wipo information: entry into national phase |
Ref document number: 15101526 Country of ref document: US |
|
WWE | Wipo information: entry into national phase |
Ref document number: 112014005918 Country of ref document: DE |
|
ENP | Entry into the national phase |
Ref document number: 20167018813 Country of ref document: KR Kind code of ref document: A |
|
122 | Ep: pct application non-entry in european phase |
Ref document number: 14871213 Country of ref document: EP Kind code of ref document: A1 |