EP3479424A1 - Komposit-kathodenschichtaufbau für festkörperbatterien auf lithiumbasis und ein verfahren zu seiner herstellung - Google Patents
Komposit-kathodenschichtaufbau für festkörperbatterien auf lithiumbasis und ein verfahren zu seiner herstellungInfo
- Publication number
- EP3479424A1 EP3479424A1 EP17734313.4A EP17734313A EP3479424A1 EP 3479424 A1 EP3479424 A1 EP 3479424A1 EP 17734313 A EP17734313 A EP 17734313A EP 3479424 A1 EP3479424 A1 EP 3479424A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- layer
- cathode layer
- conductive
- vol
- glass
- 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.)
- Withdrawn
Links
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
- H01M4/36—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
- 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
-
- 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
- H01M10/0561—Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes the electrolyte being constituted of inorganic materials only
- H01M10/0562—Solid materials
-
- 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
-
- 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
- H01M4/04—Processes of manufacture in general
- H01M4/0471—Processes of manufacture in general involving thermal treatment, e.g. firing, sintering, backing particulate active material, thermal decomposition, pyrolysis
-
- 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
- H01M4/139—Processes of 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
- H01M4/38—Selection of substances as active materials, active masses, active liquids of elements or alloys
- H01M4/381—Alkaline or alkaline earth metals elements
- H01M4/382—Lithium
-
- 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
- H01M50/46—Separators, membranes or diaphragms characterised by their combination with electrodes
-
- 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
-
- 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 invention relates to a composite cathode layer structure for
- Lithium-based solid-state batteries and a method for its production.
- the problem concerns the construction of a solid-state battery.
- Solid state batteries consist of an anode, a cathode and
- lithium-based solid-state battery In a high energy density, based on the use of metallic lithium as the anode material, and an increased security by dispensing with combustible organic components, which are used in the prior art as an electrolyte and as a binder can be. A consequence of this ion-conducting or cohesive connection of the individual components can be considerable mechanical stresses in the structure. They result from volume changes of the materials involved in loading and unloading processes.
- plastically reversibly deformable ion-conducting polymers e.g., lithium salt TFSi-modified PEO
- plastically reversibly deformable ion-conducting polymers e.g., lithium salt TFSi-modified PEO
- a significant disadvantage of polymeric solid electrolytes is their low stability to the growth of lithium dendrites (risk of short circuits), their combustibility in the event of damage to the battery and their low electrochemical stability in the case of certain combinations of electrode materials.
- a resulting completely inorganic composite cathode structure should be able to compensate under mechanical (temperature changes and differences in the coefficient of thermal expansion) and electrochemical aspects (charging and discharging processes) or avoid their occurrence by suitable choice of materials and design from the outset. It is therefore an object of the invention to provide lithium-based solid-state batteries in which the anodes are formed of metallic lithium or lithium, which are easy and safe to produce and achieve a long service life and increased safety.
- the present invention relates to a low-stress composite cathode layer construction for use in a
- Solid state battery a composite cathode layer structure take over the task of the supporting element of a repeating unit.
- the composite cathode layer construction consists of a multiphase sintered
- Substrate as a cathode layer which is provided on one side with an ion-conducting, electrically insulating further layer and on the other side with an electrically conductive but not ion-conducting further barrier layer.
- the further layer may be a barrier layer on which a solid electrolyte-forming layer can be formed or directly forms the solid electrolyte without additional layer alone.
- Anode material can be arranged as an anode.
- Anode material can be arranged as an anode.
- Solid state battery with increased electrical voltage or storage capacity form.
- Both existing on surfaces of the cathode layer layers form once an electrically conductive and once an ionic conductive Composite to each adjacent anode, wherein one of the two anodes together with the coated composite cathode forms a fully functional cell and the other anode is part of an adjacent cell.
- the cathode layer may be provided with an active material suitable for the temporary storage of lithium ions, one for lithium ions and one for lithium ions
- the barrier layer may be formed with a metal or carbon-containing glass or ceramic material and / or the further layer with a lithium ion-conducting glass or ceramic material or combinations thereof.
- the composite cathode layer construction consists of three essential ones
- Electrolytic material given as a lithium-ion conducting material, which forms a percolating structure in the cathode. This glass-based
- Electrolytic material also ensures the structural integrity of the cathode.
- Examples of potentially suitable low-melting and ion-conducting glasses can be found in the relevant specialist literature. 2 shows two diagrams of the temperature-dependent conductivity of various Li 2 O-based glasses (from Solid State Batteries: Materials Design and Optimization, ISBN 0-7923-9460-7, 1994), Kluwer Academic Press).
- an isotropic electronic conductivity is ensured via a further percolating electronically conductive barrier layer, which is integrated into the sintered glass structure.
- the composite cathode layer structure has a ternary structure which has electrical conductivity, ionic conductivity, and storage capacity for electrons and lithium ions.
- the ion-conducting further layer is connected to the cathode layer in an ion-conducting manner on one surface. It can serve a possibly required subsequent connection of an ion-conducting solid electrolyte and should have a smooth, defect-free surface. Ideally, it consists of a glass which is chemically identical or similar to the glass used for the cathode layer.
- the electronically conductive barrier layer is electrically conductively connected to the cathode layer at the oppositely disposed surface thereof. It may consist of either a metal layer (e.g., aluminum, copper or nickel). Prerequisite for this is a
- the composite cathode layer structure can also consist of a sintered electronically conductive binary glass-carbon composite, which is bonded and sintered cohesively and electrically conductive to the cathode layer. Their function is the spatial separation of the composite cathode layer structure from the adjacent anode according to the bipolar structure of a
- Coatings that perform the same function should be made so thin that the resulting mechanical stresses do not damage the composite cathode layer structure. Furthermore, the softening temperature of the glass phase of a current collector should be that of the glassy or ceramic used for the cathode layer
- Solid electrolyte materials to an excessive in the sintering or co-sintering of the composite cathode layer structure Softening or structural change selbiger to avoid.
- a composite cathode layer structure can be realized which is free of organic (non-flammable and toxic)
- Components is because inorganic non-metallic glasses can be used as auxiliary electrolytes and binder phases.
- thermo-mechanical stresses By using a low-melting, ion-conducting glass, the realization of a multilayer cathode layer with minimized thermo-mechanical stresses is possible.
- An electrically conductive glass-carbon barrier layer which is materially sintered with one side of the cathode layer, can realize an electrically conductive contact to an adjacent anode.
- An ionically conductive further layer which is materially sintered with the respective other side of the cathode layer, can produce an ionically conductive contact with another additional solid electrolyte layer, which in turn realizes contact with the next anode of an adjacent cell.
- the production of the three functional layers can be achieved simultaneously in a co-sintering process.
- FIG. 1 shows the basic sequence of the three essential layers 1 to 3 for a single repeat unit of a composite cathode layer structure using individual layers.
- a special feature of the structure described and a feature of the invention are the procedures for the preparation of the cathode layer 1 and the one side on oppositely arranged surfaces of the cathode layer 1 cohesively connected further layer 2 and the barrier layer 3.
- the aim of the procedures described is the composites of Layers 1, 2 and 3 to make possible low stress under thermomechanical aspects.
- Active ingredients Active material, ion-conductive glass or a sinterable at low temperatures ion-conductive
- Excipients such as organic binder and solvent and other additives mixed into a pourable slurry.
- Active material 50% by volume - 85% by volume (preferably 70-85% by volume)
- Carbon phase 5 vol.% - 15 vol.% (5 to 10 vol.%) Carbon phase 5 vol.% - 15 vol.% (5 to 10 vol.%).
- lithium-nickel-manganese-cobalt oxide (NMC) and lithium-cobalt oxide (LCO) and, in particular, glass can be used as the active material
- lithium-containing glasses containing as glass former B 2 0 3 , P 2 0 5 or S0 3 and other glass-forming oxides (eg Si0 2 , ZnO, Ge0 2 , Te0 2 ), which to a Low-melting character of glasses lead, use.
- glass former B 2 0 3 , P 2 0 5 or S0 3 and other glass-forming oxides eg Si0 2 , ZnO, Ge0 2 , Te0 2
- further potentially suitable glass compositions may contain further oxides (for example alkali metal and alkaline earth metal oxides) in order to obtain the glass structure in relevant properties such as ionic conductivity,
- Graphite can be used as the electrically conductive carbon phase.
- Binders polyvinyl butyral, polyvinyl alcohol, polypropylene carbonate, polymethyl methacrylate, polyvinylidene fluoride, alginates, celluloses, epoxy resins, UV-curing binders
- Solvents water, ethanol, acetone, toluene, methyl ethyl ketone, butanol, isopropanol, ethyl acetate, N-methyl-2-pyrrolidone; azeotropic mixtures (ethanol / methyl ethyl ketone / toluene; methyl isobutyl ketone / methanol;
- Plasticizer benzyl butyl phthalate, polyethylene glycol, dibutyl phthalate, diisononyl phthalate, polyalkylene glycol, dioctyl phthalate
- a prerequisite for the functionality of the composite cathode layer structure is an electrically conductive percolation of the carbon phase and an ion-conductive percolation of the ion-conductive phase in the sintered layer composite.
- the slip obtained is poured over a technologically established "Doctor Blade” process into a film having a thickness of between 50 ⁇ m and 500 ⁇ m (after drying)
- Pieces are cut out in suitable dimensions for the subsequent sintering process.
- the pieces are sandwiched between two SiC (eg Hexoloy) and carbon-based plates (setters), suitably additionally loaded with compressive forces and subjected to a sintering process.
- the basic procedure can in the simplest case to a
- the cathode layer may have a multi-layered structure graded with respect to the proportions of solid electrolyte and active material.
- a suitable graded structure may be designed as follows. Starting from the middle of a three- or multi-layered cathode layer, a gradient with varying ratios of
- the heat treatment required for sintering includes complete removal of the organic binder and the solvent and the actual subsequent sintering to form a dense composite structure consisting of lithium ion-conducting material, carbon phase and active material. Possibly.
- at least one change of atmosphere or furnace replacement may be required in order to avoid the burn-up of the setters (sintering aids) or adhesion of the sintered material to the same.
- the load of the setters should be chosen so that the lateral shrinkage of the film piece is completely converted into a pure height shrinkage and there is no cracking.
- the sintering process may be carried out in the manufacture of a composite cathode layer construction according to the invention in a microwave oven.
- Carbon or SiC-exist is for sintering means
- Microwave radiation having a frequency in the range of 2 GHz to 3 GHz, particularly of 2.4 GHz particularly suitable, since at least the set of SiC existing setter already at room temperature with the MW rays and directly reach the achievable directly in the SiC ceramic heat directly the film (s) to be sintered for the cathode layer, the further layer and / or the barrier layer. In this way, with suitable control of the microwave radiation, a very homogeneous
- Solid state battery can be viewed. Similarly, setters based on suitable carbon modifications should be allowed to heat directly using microwave radiation.
- a further layer 3 with electronic conductivity as a barrier layer and without ionic conductivity is required.
- a further layer 3 consisting of a glass-carbon composite can be used.
- this layer 3 for example, a film produced in a similar manner be as described for the cathode layer 1.
- a glass powder without conductivity for lithium ions and an electrically conductive carbon phase is necessary.
- the film additionally contains ceramic particles in order to adapt the thermal expansion coefficient of the resulting glass layer to that of the cathode layer 1. Depending on the proportion of ceramic particles, the proportion of glass phase decreases in the film formulation.
- another lithium-ion-conducting layer 2 is formed as a barrier layer or solid electrolyte on the other surface of the cathode layer 1 on the layer 3, which is not electrically conductive, necessary.
- a further layer 2 consisting of a lithium-ion conductive glass, which is also contained in the cathode layer 1, are used.
- a film are prepared in a similar manner as has been described for the cathode layer 1.
- only the lithium-ion conductive glass powder is necessary as a solid.
- the proportion of glass phase in the film is ideally 100% without consideration of the organic
- this film in addition to the glass additionally contains ceramic particles to the thermal
- the thicknesses of the cathode layer 1 provided on both sides with the further layer 2 and the barrier layer 3 should be oriented at the following ranges: 1 cathode layer 50 ⁇ - 200 ⁇
- the further layer 2 and / or the barrier layer 3 can / can also be applied in the form of a paste to a preferably still present as a green sheet substrate, which forms the cathode layer 1 after the heat treatment and the resulting sintering, and after a
- Drying then also be subjected to the heat treatment.
- the application of a paste may be accomplished by various known methods, e.g. printing, knife coating, spraying or pouring. It should be kept as constant as possible layer thickness.
- the layers 1, 2 and 3 in a common sintering step materially and functionally connected to each other according to Figure 1.
- the films of the layers 1, 2 and 3 are laminated together, then removed in a heat treatment, the organic components and then the remaining layers in a sintering step materially interconnected, ion-conducting on one side and electronically conductive on the other side.
- the cathode layer 1 On both sides of the cathode layer 1 each lead the small
- the necessary sintering temperature is based on the softening behavior of the glass phase used. Those skilled in the art are for sintering glass-containing films
- Example 2 for the preparation of a composite cathode layer structure with an ion-conducting glass layer and an electronically conductive metal layer
- the layers 1 and 2 are bonded to one another in a cohesive and functional manner in a common sintering step.
- the films of the cathode layers 1 and the further layer 2 are laminated and connected to one another in a sintering step in a material-bonded manner, on one side in an ion-conducting manner.
- the low softening temperatures of the glass phases contained in the films lead to the fact that only a comparatively low sintering temperature is required and a mechanically stress-relieved bond results.
- the necessary sintering temperature is based on the softening behavior of the glass phase used. Those skilled in the art are required for the sintering of glass-containing films viscosity ranges from the literature.
- the next step is on the opposite side of the
- Cathode layer 1 applied an electronically conductive metallic barrier layer 3.
- Possible methods are wet-chemical deposition, sputtering, vapor deposition and pressing on.
- Suitable metals are those which do not form alloys with lithium and are electrochemically stable. These are, for example, copper, nickel, titanium and stainless steel.
- Solid electrolyte used glass with 50 vol.%) Cast and dried.
- a slurry is poured with the composition of the cathode layer 1 and dried.
- a metallic foil possibly also a porous foil, such as pressed foam, mesh, or fleece
- Example 4 for producing a graded composite cathode layer structure, each with ionic and electronically conductive connection to the
- this composite cathode layer structure has a multilayer structure.
- three cathode foils each with different ratios of active material contained for the solid electrolyte in thicknesses of about 40 ⁇ poured.
- Film 1 80% by volume of active material 15% by volume of ion-conductive glass / ceramic and 5% by volume of carbon phase
- Film 2 65% by volume of active material 30% by volume of ion-conductive glass / ceramic and 5% by volume of carbon phase
- Film 3 50% by volume of active material 45% by volume of ion-conductive glass / ceramic and 5% by volume of carbon phase
- LiNi x Mn y Co z 0 2 with x + y + z l (NMC)
- a Li 2 0-B 2 0 3 glass with other additives and graphite can be used as carbon.
Landscapes
- Chemical & Material Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Inorganic Chemistry (AREA)
- Materials Engineering (AREA)
- Composite Materials (AREA)
- General Physics & Mathematics (AREA)
- Condensed Matter Physics & Semiconductors (AREA)
- Physics & Mathematics (AREA)
- Secondary Cells (AREA)
- Battery Electrode And Active Subsutance (AREA)
- Cell Electrode Carriers And Collectors (AREA)
Abstract
Description
Claims
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE102016212050.6A DE102016212050A1 (de) | 2016-07-01 | 2016-07-01 | Komposit-Kathodenschichtaufbau für Festkörperbatterien auf Lithiumbasis und ein Verfahren zu seiner Herstellung |
| PCT/EP2017/066274 WO2018002302A1 (de) | 2016-07-01 | 2017-06-30 | Komposit-kathodenschichtaufbau für festkörperbatterien auf lithiumbasis und ein verfahren zu seiner herstellung |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| EP3479424A1 true EP3479424A1 (de) | 2019-05-08 |
Family
ID=59258230
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP17734313.4A Withdrawn EP3479424A1 (de) | 2016-07-01 | 2017-06-30 | Komposit-kathodenschichtaufbau für festkörperbatterien auf lithiumbasis und ein verfahren zu seiner herstellung |
Country Status (5)
| Country | Link |
|---|---|
| US (1) | US20190157670A1 (de) |
| EP (1) | EP3479424A1 (de) |
| CN (1) | CN109417147A (de) |
| DE (1) | DE102016212050A1 (de) |
| WO (1) | WO2018002302A1 (de) |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE102018219480A1 (de) * | 2018-11-15 | 2020-05-20 | Robert Bosch Gmbh | Halbelektrodenstapel und Verfahren zu dessen Herstellung sowie dessen Verwendung |
| US11031631B2 (en) * | 2019-01-02 | 2021-06-08 | International Business Machines Corporation | Fabrication of all-solid-state energy storage devices |
| CN111490247B (zh) * | 2019-12-16 | 2022-11-29 | 电子科技大学 | 一种锂电池正极结构、全固态薄膜锂电池结构 |
| CN112599847B (zh) * | 2020-12-25 | 2021-12-28 | 哈尔滨工业大学 | 一种用于锂电池的双层固态电解质薄膜及其制备方法 |
| KR20220169810A (ko) | 2021-06-21 | 2022-12-28 | 삼성전자주식회사 | 복합양극활물질, 그 제조방법, 이를 포함하는 양극, 이차전지 |
| KR20230013567A (ko) | 2021-07-19 | 2023-01-26 | 삼성전자주식회사 | 복합양극활물질, 그 제조방법, 이를 포함하는 양극 및 이차전지 |
Family Cites Families (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20080057386A1 (en) * | 2002-10-15 | 2008-03-06 | Polyplus Battery Company | Ionically conductive membranes for protection of active metal anodes and battery cells |
| CN100380712C (zh) * | 2002-10-15 | 2008-04-09 | 波利普拉斯电池有限公司 | 用于保护活性金属阳极的离子导电复合体 |
| JP2009181873A (ja) * | 2008-01-31 | 2009-08-13 | Ohara Inc | リチウムイオン二次電池の製造方法 |
| JP2011520214A (ja) * | 2008-03-25 | 2011-07-14 | エイ 123 システムズ,インク. | 高エネルギー高出力電極および電池 |
| WO2010091075A2 (en) * | 2009-02-03 | 2010-08-12 | Ceramatec, Inc. | Electrochemical cell comprising ionically conductive ceramic membrane and porous multiphase electrode |
| MX2012002732A (es) * | 2009-09-03 | 2012-10-09 | Molecular Nanosystems Inc | Metodos y sistemas para producir electrodos que tienen al menos un grandiente funcional en los mismos y los dispositivos resultantes de los mismos. |
| FR2956523B1 (fr) * | 2010-02-18 | 2012-04-27 | Centre Nat Rech Scient | Procede de preparation d'une batterie monolithique par frittage sous courant pulse |
| WO2013008676A1 (ja) * | 2011-07-08 | 2013-01-17 | 株式会社 村田製作所 | 全固体電池およびその製造方法 |
| DE102011085224A1 (de) * | 2011-09-27 | 2013-03-28 | Siemens Aktiengesellschaft | Speicherelement und Verfahren zu dessen Herstellung |
| JP2016119257A (ja) * | 2014-12-22 | 2016-06-30 | 株式会社日立製作所 | 固体電解質、それを用いた全固体電池及び固体電解質の製造方法 |
| JP6596947B2 (ja) * | 2015-06-09 | 2019-10-30 | セイコーエプソン株式会社 | 電極複合体および電池 |
| EP3326983A4 (de) * | 2015-07-30 | 2018-07-11 | Central Glass Co., Ltd. | Sinterkörper mit lithium-titanat und lithium-lanthan-titanat, verfahren zur herstellung davon und lithiumbatterie |
-
2016
- 2016-07-01 DE DE102016212050.6A patent/DE102016212050A1/de not_active Ceased
-
2017
- 2017-06-30 CN CN201780041474.2A patent/CN109417147A/zh active Pending
- 2017-06-30 US US16/314,761 patent/US20190157670A1/en not_active Abandoned
- 2017-06-30 EP EP17734313.4A patent/EP3479424A1/de not_active Withdrawn
- 2017-06-30 WO PCT/EP2017/066274 patent/WO2018002302A1/de not_active Ceased
Also Published As
| Publication number | Publication date |
|---|---|
| CN109417147A (zh) | 2019-03-01 |
| WO2018002302A1 (de) | 2018-01-04 |
| US20190157670A1 (en) | 2019-05-23 |
| DE102016212050A1 (de) | 2018-01-04 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| EP3479425B1 (de) | Verfahren zur herstellung einer elektrochemischen zelle sowie eine mit dem verfahren hergestellte elektrochemische zelle | |
| WO2018002302A1 (de) | Komposit-kathodenschichtaufbau für festkörperbatterien auf lithiumbasis und ein verfahren zu seiner herstellung | |
| EP2792007B1 (de) | Festkörperelektrolyt für den einsatz in lithium-luft- oder lithium-wasser-akkumulatoren | |
| DE112019001409T5 (de) | Festkörperbatterie | |
| DE112018002925T5 (de) | Vollfeststoff-Natriumionen-Sekundärbatterie | |
| DE112019000374T5 (de) | Festkörper-lithium-ionen-sekundärbatterie | |
| EP3269005B1 (de) | Natriumionen leitendes element für die anwendung in elektrochemischen zellen sowie ein verfahren zu dessen herstellung | |
| DE102016015191B3 (de) | Lithium- lonen- Festkörperakkumulator sowie Verfahren zur Herstellung desselben | |
| DE112017004899T5 (de) | Festkörper-lithiumionen-sekundärbatterie | |
| DE102016214398A1 (de) | Verfahren zur Herstellung einer elektrochemischen Zelle mit Lithiumelektrode und elektrochemische Zelle | |
| DE102016215064A1 (de) | Beschichteter Festkörperelektrolyt | |
| DE102013017594A1 (de) | Herstellungsverfahren für elektrochemische Zellen einer Festkörperbatterie | |
| JP2019087346A (ja) | 全固体電池およびその製造方法 | |
| EP3893309B1 (de) | Feststoff-elektrolytmaterial für elektrochemische sekundärzelle | |
| CN113745649B (zh) | 固体电解质及其制造方法、以及全固体电池及其制造方法 | |
| WO2022185710A1 (ja) | 全固体電池及びその製造方法 | |
| JP7299105B2 (ja) | 全固体電池およびその製造方法 | |
| DE112020001241T5 (de) | Festkörperakkumulator | |
| DE102016216549A1 (de) | Festkörperzelle mit Haftungsvermittlungsschicht | |
| DE102022108265A1 (de) | Verfahren zur herstellung dreidimensionaler festelektrolytstrukturen | |
| CN111755738B (zh) | 全固体电池 | |
| DE102019203820B4 (de) | Lithiummetall-Elektrode und Verfahren zu deren Herstellung | |
| JP7425600B2 (ja) | 全固体電池およびその製造方法 | |
| WO2023247073A1 (de) | Verfahren zur herstellung einer si-anode-feststoffelektrolyt-verbindung sowie eine festkörper-li-ionen-batteriezelle und festkörper-li-ionen-batterie | |
| DE102022111809A1 (de) | Verfahren zur Herstellung eines Feststoff-Separators für eine Batteriezelle sowie Separator |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: UNKNOWN |
|
| STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: THE INTERNATIONAL PUBLICATION HAS BEEN MADE |
|
| PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
| STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: REQUEST FOR EXAMINATION WAS MADE |
|
| 17P | Request for examination filed |
Effective date: 20190129 |
|
| AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR |
|
| AX | Request for extension of the european patent |
Extension state: BA ME |
|
| DAV | Request for validation of the european patent (deleted) | ||
| DAX | Request for extension of the european patent (deleted) | ||
| STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: EXAMINATION IS IN PROGRESS |
|
| 17Q | First examination report despatched |
Effective date: 20200402 |
|
| STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: THE APPLICATION IS DEEMED TO BE WITHDRAWN |
|
| 18D | Application deemed to be withdrawn |
Effective date: 20200813 |