Classifications

• • 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
  • H01M10/42—Methods or arrangements for servicing or maintenance of secondary cells or secondary half-cells
  • H01M10/4235—Safety or regulating additives or arrangements in electrodes, separators or electrolyte
• • 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
  • H01M10/42—Methods or arrangements for servicing or maintenance of secondary cells or secondary half-cells
  • H01M10/44—Methods for charging or discharging
• • 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
  • H01M10/42—Methods or arrangements for servicing or maintenance of secondary cells or secondary half-cells
  • H01M10/44—Methods for charging or discharging
  • H01M10/443—Methods for charging or discharging in response to temperature
• • 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
  • H01M10/42—Methods or arrangements for servicing or maintenance of secondary cells or secondary half-cells
  • H01M10/48—Accumulators combined with arrangements for measuring, testing or indicating the condition of cells, e.g. the level or density of the electrolyte
  • H01M10/486—Accumulators combined with arrangements for measuring, testing or indicating the condition of cells, e.g. the level or density of the electrolyte for measuring temperature
• • 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
  • H01M50/431—Inorganic material
• • 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
  • H01M50/431—Inorganic material
  • H01M50/434—Ceramics
• • 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
  • H01M50/449—Separators, membranes or diaphragms characterised by the material having a layered structure
• • 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
  • H01M50/449—Separators, membranes or diaphragms characterised by the material having a layered structure
  • H01M50/454—Separators, membranes or diaphragms characterised by the material having a layered structure comprising a non-fibrous layer and a fibrous layer superimposed on one another
• • 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
  • H01M50/489—Separators, membranes, diaphragms or spacing elements inside the cells, characterised by their physical properties, e.g. swelling degree, hydrophilicity or shut down properties
  • H01M50/497—Ionic conductivity
• • 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
  • 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
  • H01M50/443—Particulate material
• • 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
  • H01M50/489—Separators, membranes, diaphragms or spacing elements inside the cells, characterised by their physical properties, e.g. swelling degree, hydrophilicity or shut down properties
• • 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 secondary battery, particularly a lithium ion secondary battery, a charge control system for a secondary battery, a galvanic cell for a secondary battery, an assembly of at least one electrode and a separator for such a galvanic cell, and a method for performing a rapid charge a secondary battery.
• An important aspect in the provision of secondary batteries is the charging time or charging time within which the secondary battery can be recharged from a discharge state. In particular, it plays an important role in the operation of high-energy and high-performance secondary batteries, in particular of the lithium-ion battery type, as traction batteries in motorized vehicles. Such secondary batteries have due to the high energy storage requirements correspondingly high capacities.
• the object of the present invention is to provide a secondary battery, in particular a lithium-ion secondary battery, a charge control system for a secondary battery, a galvanic cell for a secondary battery, an arrangement of at least one electrode and a separator for such a galvanic cell, and a method for Carry out a rapid charge of a secondary battery, which allow a fast charge and at the same time are safe.
• the present invention solves this object by the subject matter of the independent claims, in particular with the secondary battery according to claim 1, with the charge control system for a secondary battery according to claim 12, with the galvanic cell for a secondary battery according to claim 13, with the arrangement of at least one Elekt- and a separator for such a galvanic cell according to claim 14, and with the method for carrying out a rapid charging of a secondary battery according to claim 15.
• Preferred embodiments of the invention are subject of the subclaims.
• the secondary battery of the present invention is a lithium-ion secondary battery, but may be another type of secondary battery besides a Li-ion secondary battery, and has quick-charging capability.
• the secondary battery comprises at least one galvanic cell and an electrical charge control system, wherein the galvanic cell has at least two electrodes and at least one separator, wherein the charge control system for controlling the charging of the secondary battery is designed such that it at least temporarily provides a relative charging current with a charging current value, wherein the relative charge current is the charging current with unit C (A / Ah) related to the capacity of the secondary battery, and wherein this charge current value is at least 1C, and the separator has a coating comprising an ion conducting material having at least one inorganic component, wherein the coating is formed so that it is stable in the presence of this charging current.
• the secondary battery in particular a lithium-ion secondary battery, the charge control system for a secondary battery, a galvanic cell for a secondary battery, an arrangement of at least one electrode and a separator for a galvanic cell, and a A method for performing a rapid charging of a secondary battery, according to the invention described.
• general technical definitions in the field of battery technology can be found in the book "Handbook of Batteries,” David Linden, Thomes B. Reddy, Third Edition, 2002, MacGraw-Hill Publishing.
• the secondary battery of the present invention, the charge control system, the galvanic cell, and the electrode and separator assembly for the galvanic cell are preferable In particular for use as a drive battery of a motorized vehicle designed or optimized for this use
• vehicles of all kinds are understood that relate their kinetic energy at least partially from an engine that takes energy from an energy source (energy storage)
• Typical examples of such motorized vehicles are, inter alia, motor vehicles for road traffic, for example single-lane (eg bicycles) or two-lane motor vehicles, locomotives, ships and aircraft.
• Engines include, but are not limited to, internal combustion engines, electric motors and motors Combinations of such Antebesaggregaten, so-called hybrid drives, into consideration
• the invention is not limited to use in motorized vehicles, but can be used in particular wherever fast-charging batteries are useful, for example in mobile telephones and notebooks and other electronic entertainment or household appliances or tools, especially for home improvement or Professional supplies and the like
• a lithium-ion battery is a lithium-ion battery, a lithium-ion secondary battery, a lithium-ion battery or a lithium-ion cell, from the serial or series connection of individual lithium-ion batteries.
• lithium-ion battery is used herein as a generic term for the terms used in the prior art.
• Fast charge or fast charge capability is understood here to mean that the battery Loading the Sekundarbatte ⁇ e from a discharged state of preferably 5% or preferably 20% in a charged state of preferably either 60%, preferably 85% or preferably 95% of its full capacity within a charging time can be done or takes place, this charging time each preferably a maximum of 240 min, 180 mm, 120 min, 90 min, and more preferably, maximum 60 min, 45 min, 30 min, 15 min 5 minutes or 1 minute under "full capacity” is understood to mean the capacity that the Sekundarbatte ⁇ e currently reach a maximum due to their state of use can. For example, this full capacity may be less than or equal to the nominal capacity or original maximum capacity of the secondary battery.
• the relative charging current with which the secondary battery is charged is usually defined as the charging current related to the capacity of the secondary battery or battery cell, so that e.g. a 10 Ah (ampere-hour) secondary battery charging with an absolute charging current of 10A has a relative charge current of 1C (unit
• the charging current value is preferably at least 1C, 2C, 4C, 6C, 8C, 10C, 12C, 15C, 2OC, 4OC, 8OC or 100C.
• the inventors have found that the use of a particular coating for the separator makes it possible, especially using given materials for the electrodes, to provide a fast-charging secondary battery and to provide a corresponding fast-charging galvanic cell and a fast-charge electrode and separator arrangement.
• the resulting rapid charge capability of the secondary battery is due on the one hand to the particular ion-conducting properties of the separator and also to the fact that both the coating, the corresponding Separa- tor, the corresponding arrangement of electrode and separator, the corresponding galvanic cell and the battery itself a higher have thermal load, whereby higher charging currents are tolerated and consequently shorter charging times can be achieved.
• This superiority is particularly evident over such known secondary batteries whose separators are e.g. only have a polyethylene base.
• the coating comprises an ion-conducting material having at least one inorganic component.
• the inorganic component of the separator preferably has a microporous layer for impregnation with an electrolyte whose pore sizes are in particular substantially smaller than 4, 2 or 1 ⁇ m.
• the coating or inorganic component is also preferably ceramic or preferably has a ceramic component.
• the ceramic is preferably an oxide ceramic and may each comprise, alone or in any combination, alumina, magnesia, zirconia, titania.
• the coating particularly preferably comprises magnesium oxide.
• the inorganic component of the separator preferably corresponds to an inorganic component of the commercially available separator composite material having the trade name SEPARION available from Evonik AG, Germany. This coating also preferably corresponds to the coating material SEPARION.
• Separator composite material is to be understood as meaning a material for separating or separating the electrodes in an electrochemical device, in particular a lithium-ion battery, as known, for example, by the name of Separion® or as described, for example, in WO 2004/021499 or US Pat WO 2004/021477 and in particular EP 1 017 476 B1.
• the coating of the separator or a separator also means an electrically insulating device which separates and spaces an anode from a cathode.
• a separator layer is applied to an anode layer and / or a cathode layer.
• the porous functional layer may also be directly on the electrode, e.g. be applied to the active layer of a negative electrode.
• the separator layer or separator also at least partially accommodates an electrolyte, wherein the electrolyte preferably contains lithium ions.
• the electrolyte is also electrochemically connected to adjacent layers of the electrode stack.
• the geometric shape of a separator substantially corresponds to the shape of an anode of the electrode stack.
• a separator is thin-walled, for example 4-25 microns thick, formed, more preferably as a microporous film.
• a separator is formed with a fleece of electrically non-conductive fibers, wherein the fleece is coated on at least one side with an inorganic material.
• EP 1 017 476 B1 describes such a separator and a method for its production.
• the separator layer or the separator is wetted with an additive, which also increases the mobility of the separator layer or of the separator. Particular preference is given to wetting with an ionic additive.
• the separator layer or the separator at least partially extends over a boundary edge of at least one electrode.
• the separator layer or the separator extends beyond all boundary edges of adjacent electrodes.
• the use of the separator according to the invention with this coating can reduce the risk of thermal runaway during the fast charging of the secondary battery, which makes the operation of the secondary battery with rapid charging capability safer. Thermal runaway is the fast and uncontrolled release and decomposition of active material of the electrodes under heavy pressure build-up and temperature release, which is difficult to stop.
• the short circuit current can be closer Heat up the area around the damaged area so that the surrounding areas are also affected.
• the process expands and releases the stored energy in the accumulator abruptly. This effect can skip over to the surrounding cells and a cascade effect occurs. As a result, the total energy and reaction energy of a Li battery can be released.
• the mechanism of the thermal runaway reaction can occur at temperatures above 180 0 C, but can occur even at temperatures above 80 - 150 0 C when the SEI (solid electrolyte interface) layer of the negative electrode is damaged and this example in a exothermic reduction of the electrolyte reacts with lithiated intercalation graphite.
• a first phase especially at a first temperature regime to 80 - 15O 0 C, usually no thermal runaway reaction occurs.
• a second phase in particular at a second temperature regime up to 180 0 C and above, an additional reaction of the electrolyte can begin on the cathode surface, so that Ie built up a pressure inside the newspaper.
• a third phase in particular at a third temperature regime above 180 ° C.
• decomposition of the cathode active material can take place with a large-scale exothermic reaction.
• the anode passivation layers can be completely destroyed and free electrolyte can be exothermically decomposed.
• the decomposition of the cathode material can cause very high temperatures and heavy smoke.
• the coating is designed to be stable in the presence of the charging current, which is as large as possible to achieve fast charging; "stable" means that under normal circumstances, when there are no other disturbances than temperature, no thermal runaway
• it is preferably designed such that it exhibits the smallest possible electrical resistance for the (ion) current and, in particular, that the resulting internal resistance of the secondary battery is as small as possible in that, depending on the electrolyte used, the ion conductivity is as large as possible, in particular the conductivity for lithium ions
• the average size of the micropores of the coating be selected such that the coating is present the charge current is stable kept as large as possible, in particular between 1 and 5 microns or between 1 and 4 microns or between 2 and 4 microns or between 3 and 4 microns in diameter.
• the coating preferably comprises molecular building blocks which form amorphous or crystalline arrangements which promote the (lithium) ion flow and in particular allow the (lithium) ion flow in three spatial
• the charging control system is preferably part of a battery management system (BMS) or is a BMS or is contained in a BMS.
• BMS battery management system
• Such battery management systems monitor not only the electrical operating parameters of a (lithium-ion) accumulator, but also its temperature using conventional, on the (lithium-ion) accumulator arranged temperature sensors.
• the temperature sensors are mounted on the outside of the housing of a (lithium-ion) accumulator, so that a particular excessive heating or even a local overheating tion can not be detected at the arranged inside the housing, the current-carrying elements of the battery directly or only with a time delay.
• At least one temperature sensor assigned to the charge control system is provided in the secondary battery, or a plurality of temperature sensors are provided, whereby a temperature of the galvanic cell or several temperatures are detected.
• the cell temperature can be measured, making the battery safer.
• the charging time may be shortened if the charge control system is designed to maximize the charge current as a function of the permitted cell temperature limit.
• This limit temperature is preferably selected depending on the particular -and- optimized DAS material of the separator or its coating and is preferably between 60 0 C and 18O 0 C, preferably between 7O 0 C and 100 ° C, preferably between 8O 0 C and 150 ° C, preferably between 80 ° C and 12O 0 C or preferably between 100 0 C and 120 0 C.
• the limit temperature can take into account a temperature safety distance to the purely material technically possible limit temperatures, taking into account empirically expected or calculated Probuchslichteits temperament the probability of Thermal runaways further reduced.
• the charging control system is preferably designed to control the charging process, taking into account a cell temperature of the galvanic cell and a predetermined limit temperature.
• the charging control system may comprise electrical circuits, in particular programmable electrical circuits, by means of which, in particular, a program for fast charging of the secondary battery can be carried out.
• the charging control system can implement a method, in particular that of claim 15, for carrying out a rapid charging of a secondary battery.
• the charging control system is preferably designed to control the charging process in dependence on the cell temperature and the limit temperature, and in particular reduces or almost completely shuts off the absolute charging current (eg below 5% of the initial value of a temporarily constant charging current) or completely when the cell temperature exceeds the limit temperature reached.
• the charging control system is further preferably configured to charge in the constant current (CC) charging method, in the pulse charging method, in the constant voltage (CV) charging method, in the constant current constant charging method (CCCV), or in a constant current charging method Procedure is done that combines these procedures
• the charging control system is further preferably designed for fast charging, in particular for charging the Sekundarbatte ⁇ e from a discharged state of 20% in a charged state of preferably 60% or 85% of its full capacity is formed within a charging time, said charging time each preferably a maximum of 240 min, 180 mm, 120 min, 90 min and more preferably not more than 60 min, 45 min, 30 min, 15 min, 5 min or 1 mm
• the charge control system for a Sekundarbatte ⁇ e is preferably designed for performing a rapid charge according to the method of claim 15.
• the charge control system is further preferably designed such that the charging current value is preferably at least 2C, 4C, 6C, 8C, 10C, 12C, 15C, 2OC, 4OC, 8OC or 100C, or between any two of these values
• An electrode of the galvanic cell in particular the positive electrode (corresponds to the discharge of the battery of the cathode) preferably has an active layer, which preferably comprises a phosphate compound, in particular a lithium iron phosphate.
• An active layer may in particular be constructed as in EP 0
• the negative electrode of a lithium-ion battery is to be understood as meaning the electrode during which the positively charged lithium ions which are supplied by the electrolyte from the counter-electrode (the positive electrode or cathode) and from the lithium ions migrate during discharge back into the counter electrode
• an active layer of an electrode of the galvanic cell, in particular of the positive electrode to comprise a metal oxide, in particular the metal oxides of the metals nickel and / or manganese and / or cobalt.
• the active layer has NMC (lithiated nickel-manganese-cobalt oxides), in particular with a weight fraction of 85-95% and in particular in the quantitative ratio of 1 Li with in each case 1/3 Ni, Mn and Co.
• a thermal runaway reaction during fast charging occurs only in the temperature region of> 180 ° C and the combination in the temperature ranges ⁇ 180 ° C remained stable.
• This observation applies in particular to secondary battery (stack) cells having capacities of preferably greater than 10 Ah, preferably greater than 20 Ah, preferably greater than 30 Ah, preferably greater than 40 Ah, and applies, for example, to a large-format stack cell with> 40 Ah and nominally 3.6 V.
• An active layer can be formed from active material particles having a particle size of, for example, 5-40 ⁇ m.
• the layer is to be understood, in which proceed the electrochemical processes of the addition of lithium ions during charging or the return of lithium ions to the electrolyte during the discharge.
• the active layer can consist, for example, of graphite, so-called “hard carbon” (an amorphous carbon modification) or of nanocrystalline, amorphous silicon, the lithium ions accumulating in the abovementioned materials by so-called intercalation during charging If the negative electrode consists of graphite , Lithium ions move between the graphite planes (nC) of the negative electrode during charging and form an intercalation compound (LinxnC) with the carbon.
• the active layer can also consist of lithium titanate (Li4Ti5O12).
• the active layer may also consist of any mixture
• active material particles are the, for example, crystalline particles of the active layer forming material, between which the lithium ions accumulate during charging, to understand.
• an active mass particle may also be a graphite plane.
• the active material particles can also be connected to one another or adhesively bonded to one another by means of a binder for forming the active layer.
• the active layer can essentially consist of active material particles adhering to one another, and the outer surface of the active layer is essentially formed by the surfaces of the active mass particles exposed to the outer side of the active layer.
• the "surface exposed to the outside of the active layer” is to be understood as meaning the surface of the active material particles forming the active layer which is accessible for the accumulation of the lithium ions.
• This outer surface of the active layer may be at least partially coated with nanoparticles or other nanoparticles.
• An electrode and / or the separator may comprise a carrier or a carrier structure or a carrier layer.
• the carrier layer can essentially consist of carrier fibers and the outer surface of the carrier layer is then essentially formed by the surface of the carrier fibers exposed to the outside of the carrier layer.
• the formation of the carrier layer of carrier fibers causes the carrier layer is self-supporting.
• At least the uppermost fiber layer of the carrier fibers forming the carrier layer can be substantially coated on all sides with nanoparticles.
• This embodiment is advantageous if a nanoparticle-coated fiber layer is applied to a substrate of non-nanoparticle-treated fiber layers to form the carrier layer.
• the carrier fibers forming the carrier layer can also be substantially coated on all sides with nanoparticles. This embodiment is advantageous if the coating of the fibers with nanoparticles, in particular for reasons of adhesion, is carried out prior to processing the carrier fibers to the carrier layer
• the carrier layer can consist of woven or non-woven carrier fibers. In this way both woven and nonwoven fabrics are possible.
• the carrier fibers can be polymer fibers or steel wires suitable for forming a fabric, in particular stainless steel wires. Polymer fibers and steel wires are readily available and inexpensive starting materials for forming the Carrier Layer for the Separate Composite Mate ⁇ al
• the carrier layer is a stainless steel mesh or a polymer fleece. These are particularly inexpensive and diverse available raw material materials for the carrier layer
• the active layers of the electrodes and / or the separator or the carrier may each be wholly or partly coated with nanoparticles (eg aluminum oxide (Al 2 O 3), zirconium oxide (Zro 2) or silicon oxide (S ⁇ O 2) or a mixture of these or NMC) in the present case preferably particles having a dimension, for example a diameter or a thickness, of less than 500 nm.
• nanoparticles eg aluminum oxide (Al 2 O 3), zirconium oxide (Zro 2) or silicon oxide (S ⁇ O 2) or a mixture of these or NMC
• nanoparticles eg aluminum oxide (Al 2 O 3), zirconium oxide (Zro 2) or silicon oxide (S ⁇ O 2) or a mixture of these or NMC
• nanoparticles eg aluminum oxide (Al 2 O 3), zirconium oxide (Zro 2) or silicon oxide (S ⁇ O 2) or a mixture of these or NMC
• nanoparticles eg aluminum oxide (Al 2 O 3), zi
• the galvanic cell according to the invention for a secondary battery having fast charging capability comprises at least two electrodes and at least one separator, which undergoes essentially no structural damage, in particular at temperatures up to 18O 0 C.
• a galvanic cell is to be understood as meaning a device which also serves for emitting electrical energy and for converting chemical energy into electrical energy.
• the galvanic cell has at least two electrodes of different polarity and the electrolyte is depending on the design
• the galvanic cell is also able to absorb electrical energy during charging, convert it into chemical energy and store it.
• the conversion of electrical energy into chemical energy is lossy and accompanied by irreversible chemical reactions.
• An electric current into or out of a galvanic cell can cause an electric shock Heating effect This electric heating power can increase the temperature of the galvanic cell.
• irreversible chemical reactions increase.
• These irreversible chemical reactions can cause areas of a galvanic cell to undergo transformation and / or storage With an increasing number of charging processes, these areas gain in volume
• the usable charging capacity of a galvanic cell or the device decreases
• the galvanic cell can comprise an electrode stack or multiple galvanic cells can form an electrode stack
• an electrode stack is also understood to mean a device which also serves as an assembly of a galvanic cell for the storage of chemical energy and for the release of electrical energy. Before the release of electrical energy, stored chemical energy is converted into electrical energy
• the electrode stack has several layers, at least one anode layer, one cathode layer and one separator layer. The layers are stacked or stacked, the separator layer at least partially between an anode layer and a cathode layer This sequence of layers within the electrode stack is preferably repeated several times. Preferably, some electrodes are in particular electrically connected to one another, in particular connected in parallel Preferably, the layers are wound up into an electrode winding.
• electrode stack is also used for electrode windings
• the arrangement according to the invention which has rapid charging capability, comprises at least one electrode and a separator for a galvanic cell, wherein the separator comprises a coating which suffers substantially no structural damage, especially at temperatures up to 180 ° C., and which optionally is applied to an electrode is.
• the inventive method for carrying out a rapid charging of a secondary battery, in particular a secondary battery according to the invention comprising at least one galvanic cell having at least two electrodes and at least one separator comprising a coating comprising an ion-conducting material with at least one inorganic component, wherein the coating so is designed to be stable in the presence of the charging current, comprising the steps: - at least temporarily providing a relative charging current having a charging current value which is in particular at least 1 C; preferably: using a limit temperature, which is preferably chosen as a function of the choice of material of the coating of a separator, measuring a cell temperature of the galvanic cell; - Preferably: controlling the charging process in dependence on the cell temperature and the limit temperature and in particular reducing the absolute charging current or interrupting the charging current when the cell temperature reaches the limit temperature. Further preferred steps of the process may be readily deduced by those skilled in the art from the description of the secondary battery and its components.
• a lithium-ion secondary battery according to the invention in the example comprises a large-scale galvanic stack cell with> 40 Ah and nominal 3.6 V voltage. It has an electrode stack.
• the galvanic cell has graphite-based negative electrodes, NMC-based (NMC: lithiated nickel-manganese-cobalt oxide) based electrodes, and electrolyte with alkyl carbonates, additives, and Li-conducting salt.
• a separator is arranged, which is provided with a coating, for example from the coating material Separion®.
• a coating for example from the coating material Separion®.
• the separator comprises a support comprising stainless steel mesh or a polymer fleece provided with a permanent ceramic as a ceramic membrane as a separator in the thickness 4-45 microns.
• the active material of the negative electrode is comb-like coated with nanoparticles (aluminum and zirconium oxide).
• the positive electrode active material has NMC.
• the galvanic cell has arresters.
• the arresters are part of a discharge device.
• a discharge device is to be understood as meaning a device which, when discharging, emits electrons from a galvanic cell in the direction of an electrical current
• the at least one discharge device is assigned to one of the electrodes of the galvanic cell, in particular electrically conductively connected to this electrode.
• a discharge device allows a flow of current in the opposite direction.
• the at least one discharge device is also connected in a heat-conducting manner to a galvanic cell.
• a discharge device in the sense of the invention also makes a transport of heat energy out of a galvanic cell.
• the discharge device comprises a metal.
• the discharge device comprises copper or aluminum.
• the galvanic cell has temperature sensors near the electrode conductors. Near the arrester, the temperature of the galvanic can increase particularly strong, since there a high charging current can cause high temperatures. In these areas, the temperature monitoring is therefore particularly useful, in particular to avoid a thermal runaway reaction.
• the secondary battery includes a charge control system that is part of a BMS.
• the BMS is connected to the temperature sensors and determines the temperatures near the arrester of the galvanic cell, in particular when charging and / or discharging the cell.
• the BMS is by programming with a control software code designed to keep the charging current so high that a threshold temperature of 150 0 C is not exceeded at each of the temperature sensors.
• the BMS regulates the charging current so that the threshold temperature is within a tolerance range of, for example, 130 to 150 0 C, so that the possible charging current to achieve the shortest possible charging time is also used.
• a constant current with a relative charging current of 1 C is first used.
• the charging control system needs a charging time of 2 hours. In this way, the quick charging ability can be shown.
• this electrode-separator arrangement causes the thermal runaway, which can be initiated in conventional arrangements in all temperature regimes, ultimately only in the temperature range> 180 ° C may occur and does not occur here, so that the operation of the secondary battery is safe.
• This result was surprising and demonstrates the performance and improved safety performance of the electrode separator assembly and method of the present invention.

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• Chemical & Material Sciences (AREA)
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• General Chemical & Material Sciences (AREA)
• Engineering & Computer Science (AREA)
• Manufacturing & Machinery (AREA)
• Inorganic Chemistry (AREA)
• Ceramic Engineering (AREA)
• Secondary Cells (AREA)
• Cell Separators (AREA)
• Battery Electrode And Active Subsutance (AREA)

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• 2009
  • 2009-07-07 DE DE102009032050A patent/DE102009032050A1/de not_active Withdrawn
• 2010
  • 2010-06-22 KR KR1020127003291A patent/KR20120107923A/ko not_active Withdrawn
  • 2010-06-22 JP JP2012518781A patent/JP2012532428A/ja active Pending
  • 2010-06-22 EP EP10728136A patent/EP2452383A1/de not_active Withdrawn
  • 2010-06-22 CN CN2010800306534A patent/CN102625958A/zh active Pending
  • 2010-06-22 BR BR112012000361A patent/BR112012000361A2/pt not_active IP Right Cessation
  • 2010-06-22 US US13/382,399 patent/US20120169297A1/en not_active Abandoned
  • 2010-06-22 WO PCT/EP2010/003810 patent/WO2011003513A1/de active Application Filing

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