WO2011042111A1 - Elektrochemische zelle und verfahren zur herstellung einer solchen zelle - Google Patents

Elektrochemische zelle und verfahren zur herstellung einer solchen zelle Download PDF

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Publication number
WO2011042111A1
WO2011042111A1 PCT/EP2010/005604 EP2010005604W WO2011042111A1 WO 2011042111 A1 WO2011042111 A1 WO 2011042111A1 EP 2010005604 W EP2010005604 W EP 2010005604W WO 2011042111 A1 WO2011042111 A1 WO 2011042111A1
Authority
WO
WIPO (PCT)
Prior art keywords
layer
electrode layer
electrode
electrochemical cell
edge
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.)
Ceased
Application number
PCT/EP2010/005604
Other languages
German (de)
English (en)
French (fr)
Inventor
Joerg Kaiser
Claus-Rupert Hohenthanner
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Li Tec Battery GmbH
Original Assignee
Li Tec Battery GmbH
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Li Tec Battery GmbH filed Critical Li Tec Battery GmbH
Priority to EP10754695A priority Critical patent/EP2486614A1/de
Priority to US13/500,388 priority patent/US20120282517A1/en
Priority to JP2012532475A priority patent/JP2013506967A/ja
Priority to CN2010800443777A priority patent/CN102687312A/zh
Priority to BR112012007806A priority patent/BR112012007806A2/pt
Publication of WO2011042111A1 publication Critical patent/WO2011042111A1/de
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/02Details
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/04Construction or manufacture in general
    • H01M10/0413Large-sized flat cells or batteries for motive or stationary systems with plate-like electrodes
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/058Construction or manufacture
    • H01M10/0585Construction or manufacture of accumulators having only flat construction elements, i.e. flat positive electrodes, flat negative electrodes and flat separators
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/13Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/10Primary casings; Jackets or wrappings
    • H01M50/102Primary casings; Jackets or wrappings characterised by their shape or physical structure
    • H01M50/103Primary casings; Jackets or wrappings characterised by their shape or physical structure prismatic or rectangular
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/052Li-accumulators
    • H01M10/0525Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/42Methods or arrangements for servicing or maintenance of secondary cells or secondary half-cells
    • H01M2010/4292Aspects relating to capacity ratio of electrodes/electrolyte or anode/cathode
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50Manufacturing or production processes characterised by the final manufactured product
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T29/00Metal working
    • Y10T29/49Method of mechanical manufacture
    • Y10T29/49002Electrical device making
    • Y10T29/49108Electric battery cell making

Definitions

  • the invention relates to an electrochemical cell having an electrode stack with in particular a plurality of layers of active material. Furthermore, the invention relates to a method for producing an aforementioned electrochemical cell. Furthermore, the invention relates to a battery with at least one aforementioned electrochemical cell.
  • There are lithium-ion cells are known in which anodes and cathodes are arranged alternately, wherein between the anodes and the cathodes in each case a separator is provided.
  • the cathodes generally have a smaller areal extent than the anodes.
  • an electrochemical cell comprising at least one electrode stack, which is arranged within a sheath of the electrochemical cell, wherein the electrode stack at least one cathode layer and one anode layer wherein a separator layer is arranged between the first electrode layer and the second electrode layer, and wherein the cathode layer has a smaller areal extent than the anode layer.
  • This electrochemical cell is further characterized in that an edge layer is arranged adjacent to the first electrode layer. The edge layer is preferably made mechanically stabilizing.
  • an electrode stack is to be understood as a device which, as an assembly of a galvanic cell, also serves to store chemical energy and to deliver electrical energy.
  • the electrode stack has a plurality of plate-shaped elements, at least two electrodes, namely in particular anode and cathode, and a separator which at least partially receives the electrolyte.
  • at least one anode, a separator and a cathode are stacked or stacked, wherein the separator is at least partially disposed between the anode and the cathode.
  • This sequence of anode, separator and cathode can be repeated as often as desired within the electrode stack.
  • the plate-shaped elements are wound into an electrode winding.
  • electrode stack is also used for electrode windings: Before the electrical energy is emitted, stored chemical energy is converted into electrical energy. During charging, the electrical energy supplied to the electrode stack or the galvanic cell is converted into chemical energy and stored a plurality of electrode pairs and separators, particularly preferably some of the electrodes are electrically connected to one another.
  • an at least partial limitation is to be understood, which delimits the electrode stack to the outside.
  • the envelope is preferably gas and liquid tight, so that a material exchange with the environment can not take place.
  • the electrode Stacks are located within the enclosure. At least one current conductor, in particular two current conductors extend out of the enclosure and serve to connect the electrode stacks.
  • the outwardly extending current conductors preferably represent the positive pole connection and the negative pole connection of the electrochemical cell. However, it is also possible for a plurality of current conductors to extend out of the enclosure, in particular four current arresters. If the electrochemical cell has two electrode stacks which are connected in series with one another, two electrodes of different electrode stacks are connected to one another.
  • a current collector is an element which is made of an electrically conductive material. It is used to conduct electricity between two geometrically separated points.
  • a current collector is connected to an electrode stack.
  • the current conductor is connected to all similar electrodes of an electrode stack, i. either with the cathodes or with the anodes. It goes without saying that a current conductor is not connected to the cathodes and anodes of an electrode stack at the same time, since this would lead to a short circuit.
  • a current collector may be connected to different electrodes of different electrode stacks, e.g. in a series connection of the two electrode stacks. At least one current collector extends from the enclosure and may serve to connect the electrochemical cell to the outside.
  • the current collector may be integrally formed with one or more electrodes. A distinction between current collector and electrode can be seen in that the current conductor is not coated in particular with active electrode material.
  • the cathode layer By providing the edge layer on the first electrode layer, the cathode layer can be mechanically enlarged. The enlargement results in a reduced surface pressure on the electrode layers, in particular on the cathode layer, while the pressure remains constant.
  • the cathode layer and the edge layer are preferably in a common Plane arranged.
  • the separator layer which is in contact with the first electrode layer and in particular overlaps the cathode layer in an edge region of the first electrode layer, can thereby be supported by the edge layer.
  • the anode layer which is arranged on the side of the separator layer facing away from the first electrode layer, is indirectly supported by the edge layer.
  • the edge layer is preferably arranged at least on one side of the first electrode layer.
  • the boundary layer is arranged on one side of the first electrode layer, from which a current conductor is connected to the cathode layer.
  • the current conductor is preferably not coated with active electrode material.
  • the current arrester may have a cross-sectional thickness which is less than the cross-sectional thickness of the first electrode layer.
  • the cross-sectional thickness of the current conductor can be summed up by a certain cross-sectional thickness of the edge layer, in particular to a cross-sectional thickness which corresponds to the cross-sectional thickness of the cathode layer in the region of the interface between the current conductor and the first electrode layer.
  • the edge layer is preferably arranged on at least two mutually opposite sides of the first electrode layer.
  • the edge layer can be split into several, in particular not interconnected, portions of the edge layer.
  • the edge layer is arranged circumferentially around the cathode layer.
  • a circumferential area around the cathode layer can be reinforced.
  • the anode layer is thereby supported in a peripheral region of the edge layer.
  • the edge layer may form a particular supporting frame around the cathode layer.
  • the electrode layer preferably forms a composite layer together with the edge layer.
  • the composite layer preferably has the mechanical properties that would have a continuous cathode layer. As a result, all the disadvantages can be compensated, which can result from the smaller areal extent of the first electrode layer.
  • a length of the composite layer corresponds to a length of the second electrode layer.
  • a width of the composite layer corresponds to a width of the second electrode layer.
  • An outline of the composite layer preferably corresponds to an outline of the second electrode layer.
  • corresponding is meant a wide-ranging concept of size, which is to be understood in particular as manufacturing-related tolerances
  • deviations in the single-digit percentage range between the two length specifications may well lie in. However, the deviations are preferably smaller, in particular smaller than 5%. based on the geometric surface area.
  • the edge layer has a cross-sectional thickness that substantially corresponds to a cross-sectional thickness of the first electrode layer.
  • the edge layer has a hardness which corresponds approximately to the hardness of the first electrode layer.
  • the edge layer can simulate an enlarged cathode layer.
  • the first layer may be a cathode layer and the second layer may be an anode layer.
  • the invention is achieved by a method for producing a generic electrochemical cell, wherein at least on one side of the electrode layer, an edge layer is attached.
  • the edge layer and the first electrode layer can be arranged in a common plane.
  • the edge layer can be arranged at least on one side of the first electrode layer, in particular on one side of the first electrode layer, of which a current conductor is connected to the first electrode layer.
  • the edge layer can be arranged at least on two respective opposite sides of the first electrode layer. More preferably, the edge layer can be arranged circumferentially around the first electrode layer.
  • a composite layer is formed together from the first electrode layer with the edge layer.
  • Fig. 1 shows an inventive electrochemical cell in flat construction in the
  • FIG. 2 shows a detail view of an electrochemical cell according to FIG. 1 in FIG
  • FIG. 3 is a detail view of an electrochemical cell according to FIG. 1 in FIG.
  • FIG. 4 a Cross section after the application of a boundary layer; 4 a) a cathode of the electrochemical cell according to FIG. 1 before the application of an edge layer, FIG.
  • FIG. 5 a an alternative cathode according to FIG. 1 before the application of a
  • FIG. 1 shows an electrochemical cell 1 according to the invention.
  • the electrochemical cell 1 comprises an electrode stack 2 which is accommodated within an enclosure 4.
  • the envelope 4 consists essentially of two moldings, which were made of packaging film. The moldings were brought into their illustrated form in a deep drawing process.
  • the sheath 4 has a limited resistance to externally acting forces, since the sheath 4 is largely elastic, so that forces acting on externally can be passed on to the electrode stack. It can be seen that forces in the edge region F R of the electrochemical cell 1 can be greater than forces occurring in the central region F z .
  • FIG. 1 it can not be seen that a plurality of current conductors 3, which extend through the sheath 4, are electrically conductively connected to the electrode stack 2.
  • FIG 2 shows a detail of the electrode stack 2 of an electrochemical cell of Figure 1 shown enlarged.
  • the electrode stack 2 has a plurality of first electrode layers 5 and a plurality of second electrode layers 6.
  • the electrode layers 5, 6 are designed flat and arranged parallel to a plane E.
  • the first electrode layers 5 and the second electrode layers Layers 6 are arranged alternately.
  • a separator layer 7 is arranged between the first electrode layer 5, which in the present case is a cathode layer, and the second electrode layer 6, which in the present case is an anode layer.
  • the current conductors 3 can be seen, which are arranged outside the electrode layers 5, 6. Extensions of the current conductor 3 within the electrode layers 5, 6 form the electrodes 13, 14.
  • a cathode 13 is provided within the cathode layer 5; Within the anode layer 6, an anode 14 is provided.
  • the current conductors 3 may be integrally formed with the respective electrodes 13, 14; However, the current conductor 3 can also be formed separately from the electrodes 13, 14 and be connected to them in an electrically conductive manner.
  • the cathode layer 5 has a smaller areal extent than the anode layer 6. Thus, it can be seen that in an edge region 11, the anode layer 6 projects beyond the cathode layer 5.
  • gaps 12 are formed between two anode layers 6, which are bounded on one side by a side 9 of the cathode layer 5. Due to the gap 12, the anode layers 6 in the case of external Karataufbringung perpendicular to the respective planes E of the layers no resistance counteracted, so that the anode layers 6 can bend in the edge region 11 into the gaps 12, which is indicated by the dashed lines , This can lead to signs of aging on the electrode stacks.
  • FIG. 3 shows the detail of the electrode stack 2 according to FIG. 2 after an edge layer 8 has been applied. It can be seen that the gap 12 is completely filled by the edge layer 8 of polyurethane.
  • the edge layer 8 is attached to one side 9 of the cathode layer 5 and arranged with this in a plane E.
  • the cathode layer 5 and the edge layer 8 forms a composite layer 10, which is arranged between two respective anode layers 6.
  • the edge layer 8 in this case has a hardness which corresponds to the hardness of the cathode layer 5.
  • the edge layer 8 acts mechanically stabilizing, in particular on the anode layer. 6
  • FIG. 4 a shows a cathode layer 5 before the application of an edge layer.
  • the cathode layer 5 has a length Li and a width B.
  • In one side 9 of the current conductor 3 is connected to the cathode.
  • FIG. 4b shows a development of the invention as shown in FIG. On the cathode layer 5, according to FIG. 5b), an edge layer 1 1 is attached circumferentially around the cathode layer 5, so that a composite layer 10 is formed therefrom. Both the length L 2 and the width B 2 of the composite layer 10 are thus greater than the length U as well as the width Bt of the cathode layer 5.
  • FIG. 5c shows by way of example an anode layer 6 of the electrochemical cell according to the invention.
  • the length L 2 corresponds to the length L 2 of the composite layer 10.
  • the width B 2 of the anode layer 6 corresponds to the width B 2 of the composite layer 10.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Battery Electrode And Active Subsutance (AREA)
  • Secondary Cells (AREA)
  • Primary Cells (AREA)
  • Cell Separators (AREA)
PCT/EP2010/005604 2009-10-05 2010-09-13 Elektrochemische zelle und verfahren zur herstellung einer solchen zelle Ceased WO2011042111A1 (de)

Priority Applications (5)

Application Number Priority Date Filing Date Title
EP10754695A EP2486614A1 (de) 2009-10-05 2010-09-13 Elektrochemische zelle und verfahren zur herstellung einer solchen zelle
US13/500,388 US20120282517A1 (en) 2009-10-05 2010-09-13 Electrochemical cell and method for producing such a cell
JP2012532475A JP2013506967A (ja) 2009-10-05 2010-09-13 電気化学的電池およびこのような電池の製造方法
CN2010800443777A CN102687312A (zh) 2009-10-05 2010-09-13 电化学电池和制造该类电池的方法
BR112012007806A BR112012007806A2 (pt) 2009-10-05 2010-09-13 célula eletroquímica, bateria e método para produzir uma célula eletroquímica

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102009048237A DE102009048237A1 (de) 2009-10-05 2009-10-05 Elektrochemische Zelle und Verfahren zur Herstellung einer solchen Zelle
DE102009048237.7 2009-10-05

Publications (1)

Publication Number Publication Date
WO2011042111A1 true WO2011042111A1 (de) 2011-04-14

Family

ID=43086181

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/EP2010/005604 Ceased WO2011042111A1 (de) 2009-10-05 2010-09-13 Elektrochemische zelle und verfahren zur herstellung einer solchen zelle

Country Status (8)

Country Link
US (1) US20120282517A1 (https=)
EP (1) EP2486614A1 (https=)
JP (1) JP2013506967A (https=)
KR (1) KR20120091184A (https=)
CN (1) CN102687312A (https=)
BR (1) BR112012007806A2 (https=)
DE (1) DE102009048237A1 (https=)
WO (1) WO2011042111A1 (https=)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2997234B1 (fr) * 2012-10-22 2016-05-06 Renault Sa Cellule electrochimique de stockage d'electricite.
DE102018221344A1 (de) * 2018-12-10 2020-06-10 Robert Bosch Gmbh Elektrodenstapel für eine galvanische Zelle
DE102021125288A1 (de) * 2021-09-29 2023-03-30 Volkswagen Aktiengesellschaft Batteriezelle und Verfahren zu deren Herstellung

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20040048150A1 (en) * 2002-09-06 2004-03-11 Crouch Dell Albert Battery cell having edge support and method of making the same
US20060172185A1 (en) * 2005-01-28 2006-08-03 Kazuya Mimura Multilayer secondary battery and method of making same
EP2086044A2 (en) * 2008-02-04 2009-08-05 Fuji Jukogyo Kabushiki Kaisha Electric storage device

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4932263B2 (ja) * 2005-01-28 2012-05-16 Necエナジーデバイス株式会社 積層型二次電池及びその製造方法
DE102005042916A1 (de) * 2005-09-08 2007-03-22 Degussa Ag Stapel aus abwechselnd übereinander gestapelten und fixierten Separatoren und Elektroden für Li-Akkumulatoren
JP5099407B2 (ja) * 2006-11-30 2012-12-19 住友電気工業株式会社 電池
JP5526481B2 (ja) * 2007-06-06 2014-06-18 日産自動車株式会社 二次電池およびその製造方法
JP5515267B2 (ja) * 2008-10-07 2014-06-11 日産自動車株式会社 非水電解質二次電池

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20040048150A1 (en) * 2002-09-06 2004-03-11 Crouch Dell Albert Battery cell having edge support and method of making the same
US20060172185A1 (en) * 2005-01-28 2006-08-03 Kazuya Mimura Multilayer secondary battery and method of making same
EP2086044A2 (en) * 2008-02-04 2009-08-05 Fuji Jukogyo Kabushiki Kaisha Electric storage device

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See also references of EP2486614A1 *

Also Published As

Publication number Publication date
JP2013506967A (ja) 2013-02-28
CN102687312A (zh) 2012-09-19
BR112012007806A2 (pt) 2016-08-30
EP2486614A1 (de) 2012-08-15
KR20120091184A (ko) 2012-08-17
DE102009048237A1 (de) 2011-04-21
US20120282517A1 (en) 2012-11-08

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