Classifications

• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M4/00—Electrodes
  • H01M4/02—Electrodes composed of, or comprising, active material
  • H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M10/00—Secondary cells; Manufacture thereof
  • H01M10/04—Construction or manufacture in general
  • H01M10/0431—Cells with wound or folded 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
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M10/00—Secondary cells; Manufacture thereof
  • H01M10/05—Accumulators with non-aqueous electrolyte
  • H01M10/052—Li-accumulators
  • H01M10/0525—Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M10/00—Secondary cells; Manufacture thereof
  • H01M10/05—Accumulators with non-aqueous electrolyte
  • H01M10/058—Construction or manufacture
  • H01M10/0587—Construction or manufacture of accumulators having only wound construction elements, i.e. wound positive electrodes, wound negative electrodes and wound separators
• • 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
  • H01M4/0402—Methods of deposition of the material
  • H01M4/0404—Methods of deposition of the material by coating on electrode collectors
• • 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
  • H01M4/0402—Methods of deposition of the material
  • H01M4/0409—Methods of deposition of the material by a doctor blade method, slip-casting or roller coating
• • 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
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
  • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
  • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
  • Y02E60/10—Energy storage using batteries
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
  • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
  • Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
  • Y02P70/50—Manufacturing or production processes characterised by the final manufactured product

Definitions

• the present invention relates to field of battery, more particularly to a battery electrode plate suitable for a lithium secondary battery, a forming method thereof and a battery having the same.
• Lithium ion battery has high energy density, long cycle life span and high open circuit voltage, and it is also safe and environment amicable. Therefore it is widely used in laptop computer, digital camera, video camera, PDA, MP3, Bluetooth, PMP as well as power for other personal electronic devices for communication or entertainment. And lithium ion batteries are gradually expanding to electric bicycles or electric car field. The market share of lithium batteries is above 90% currently.
• lithium ion battery is the most competitive and already commercialized new secondary power sources.
• the edges of the electrode material region will extend to certain extent, and the extension rates of the dressing and the current collector itself are different, thus the edges of the plates may have current drapes, and the plates may brake during coiling and thus may affect the battery performance severely.
• the present invention is directed to solve at least one of the problems existing in the prior art. Accordingly, the present invention needs to provide a battery electrode plate which may not drape or wrinkle during rolling whereas the yield rate thereof may be improved. Further, a method of forming the battery electrode plate and a battery having the same are needed to be provided accordingly.
• a battery electrode plate comprising a squared current collector with electrode material being coated on at least a portion of the current collector.
• the portion of the current collector has a first thickness region, a second thickness region which has a thickness smaller than that of the first thickness region and a transition region tapering from the first thickness region toward the second thickness region.
• a method of forming a battery electrode plate comprising the steps of: coating slurry of electrode material on a current collector, and drying and rolling the coated current collector to obtain the electrode plate.
• a thinning step may be performed to form a first thickness region, a second thickness region and a transition region tapering from the first thickness region toward the second thickness region for the coated electrode material, in which a thickness of the electrode material in the first thickness region may be greater than that in the second thickness region.
• a battery comprising: a battery shell, a battery core and electrolyte both encapsulated in the battery shell.
• the battery core is formed of a positive electrode plate, a negative electrode plate and a separator disposed between the positive and negative electrode plates.
• At least the positive electrode plate may be made of the battery electrode plate as described hereinabove or made from the method as described hereinabove.
• the current collector in the present invention may not break or drape or wrinkle during rolling and as a result yield rate of the electrode plates may be improved and it is adapted for large scale industrial production. And the battery according to the present invention may have improved safety performance.
• Fig 1 shows a battery electrode plate according to an embodiment of the invention.
• Fig 2 shows a perspective view of a battery core according to an embodiment of the invention.
• Fig 3 shows a cross section view of a battery core according to an embodiment of the invention.
• Electrode current collector 6. Separator
• the present invention discloses a battery electrode plate comprising a squared current collector and electrode material coated on the current collector.
• the portion of the current collector coated with electrode material has a first thickness region and a second thickness region.
• the coated electrode material of the first thickness region is thicker than the second thickness region.
• the first thickness region, the transition region, the second thickness region and the tab region can be divided as follows: take the direction which is parallel with the current collector as a length direction, and take the direction which is vertical to the length direction as a width direction. In the width direction, the electrode material region contained on the current collector is in turns as follows: the first thickness region, the transition region and the second thickness region.
• the current collector can be prepared from any material that is known in the art.
• the positive current collector can be Al foil and the negative current collector can be Cu foil.
• the positive electrode material is known in the art.
• the positive electrode material comprises positive adhesive agents, positive active material and positive conductive agents.
• the contents of the positive adhesive agents, positive active material and positive conductive agents are conventional.
• the positive active material can be purchased from the market, for example LiFePO 4 , Li 3 V 2 (PO 4 ) S » LiMn 2 O 4 , LiMnO 2 , LiNiO 2 , LiCoO 2 , LiVPO 4 F, LiFeO 2 ; or triple series Lii+ a Li _ b - c M b N c 0 2 , -0.1 ⁇ a ⁇ 0.2, O ⁇ b ⁇ l , O ⁇ c ⁇ l , 0 ⁇ b+c ⁇ l, in which L, M, N are one or more selected from Co, Mn, Ni, Al, Mg, Ga and 3d transition metal elements.
• the positive conductive agent can be any positive conductive agent known in the art.
• it can be one or more selected from Graphite, Carbon fiber, carbon black, metal powder and fiber.
• the positive material is mixed with solvent to obtain positive slurry.
• the solvent can be any solvent known in the art, for example, which can be one or more selected from N-methyl pyrrolidone (NMP), dimethylformamide(DMF), diethyl formamide(DEF), dimethyl sulfoxide(DMSO), tetrahydrofuran(THF), H 2 O and alcohols.
• NMP N-methyl pyrrolidone
• DMF dimethylformamide
• DEF diethyl formamide
• DMSO dimethyl sulfoxide
• THF tetrahydrofuran
• the present invention does not have special limitation for the negative material and it can be any conventional negative material in the prior art.
• the negative material normally comprises negative active material, negative adhesive agent and negative conductive agent.
• the negative active material can be purchased from the market, for example, graphite and lithium- titanium- oxygen (LiTiO) compound.
• the negative conductive agent can be Ni powder and/or Cu powder.
• the negative adhesive agent can be any adhesive agent used in the lithium secondary batteries that is known in the art. For example it can be one or more selected from polyvinylidene fluoride(PVDF), polytetrafluoroethylene(PTFE), sodium carboxymethylcellulose(CMC) and styrene-butadiene rubber(SBR).
• the width of the transition region is about 1-lOmm, and the width of second thickness region is about 1-1 Omm.
• the width of the transition region is about 3 -8mm, the width of the second thickness region is about 3 -8mm.
• the thickness of the electrode material in the transition region is not greater than that in the first thickness region.
• the thickness of the electrode material in the second thickness region is not great than that in the transition region.
• the transition region is smoothly connected with the first thickness region and the second thickness region.
• the electrode material in the first thickness region has a thickness of about 20-350um.
• the electrode material in the transition region has a thickness of about 15-300um.
• the electrode material in the second thickness region has a thickness of about 10-250um.
• the maximum thickness of the electrode material in the transition region is equal to that of the first thickness region, and the minimum thickness of the electrode material in the transition region is equal to that of the second thickness region.
• a ratio of a thickness of the electrode material in the first thickness region to a thickness of the electrode material in the second thickness region can be about 2-10:1.
• the descending gradient of the thickness of the electrode material in the transition region is about 5-300um/mm. In an embodiment of the invention, it may be 10-150um/mm.
• the calculation method of the descending gradient is as follows:
• the descending gradient (the maximum thickness of the transition region-the minimum thickness of the transition region) / the width of transition region.
• the thickness of the electrode material of the first thickness region and the second thickness region is uniform in a thickness direction of the battery electrode plate respectively, and the descending gradients are the same.
• the battery electrode plate further comprises tab regions without electrode material being coated thereon.
• the tab region is formed at a lateral side of the second thickness region facing away from the transition region with a width of substantially 10- 100mm in a direction from the first thickness region to the second thickness region. In an embodiment of the invention, it has a width of substantially 20-70mm.
• the method thereof can be as follows: mixing the positive active material, conductive agent, adhesive agent and solvent and stirring the mixture to obtain the positive slurry.
• the positive active material, conductive agent, adhesive agent, solvent are the same as above mentioned, and the detailed description is omitted here for brevity purpose.
• the present invention further discloses a method of forming the battery electrode plate comprising: coating slurry of electrode material on a current collector, and drying and rolling the coated current collector to obtain the electrode plate, wherein before rolling, a thinning step is performed to form a first thickness region, a second thickness region and a transition region tapering from the first thickness region toward the second thickness region for the coated electrode material, in which a thickness of the electrode material in the first thickness region is greater than that in the second thickness region.
• the thinning step can be scraping or coating directly to form the first thickness region, transition region and second thickness region.
• the method disclosed in the present embodiment comprises: coating electrode slurry on the current collector to form a first thickness region, transition region and second thickness region.
• the thickness of the electrode material in the first thickness region is greater than that in the second thickness region and the thickness of the electrode material is decreasing in the direction from first thickness region to second thickness region. Then drying the coated current collector and rolling it to obtain the electrode plate.
• the above mentioned method of coating electrode slurry onto the current collector to form a first thickness region, transition region and second thickness region is: the current collector moves along the length direction, and coating the current collector in the width direction by controlling the slurry flux.
• the flux of the slurry differs.
• the flux of the slurry remains the same.
• the flux of the slurry remains the same too.
• the slurry flux decreases from the first thickness region to the second thickness region.
• the specific flux is related to the moving speed of the current collector providing that the thickness of the electrode slurry in the first thickness region is greater than that in the second thickness region.
• the thickness of the electrode slurry decreases in the direction from the first thickness region to the second thickness region.
• the above mentioned method of coating electrode slurry onto the current collector to form a first thickness region, transition region and second thickness region further can be: while coating the slurry, a blocking board is set at the exit of the electrode plate.
• the lower portion of the blocking board is spaces from the electrode plate by a certain distance, which is the thickness of the electrode slurry on the electrode plate.
• the current collector moves in the length direction, and the blocking board is set at the width direction of the current collector. In the corresponding widths direction of the first thickness region, the transition region and the second thickness region, the distance between the lower portion of the blocking board and the electrode plate corresponds with the required thickness of the electrode slurry.
• the thickness of the electrode slurry and the descending trend of the transition region can be controlled by controlling the distance between the lower portion of the blocking board and the electrode plate, and the electrode plate with the first thickness region, the transition region and the second thickness region can be obtained.
• the location on the current collector is selected according to the required widths of the first thickness region, the transition region and the second thickness region. Then the slurry is coated in the first thickness region location, the transition region location and the second thickness region location in such a manner that the electrode slurry in the first thickness region is thicker than that in the second thickness region, and the thickness of the slurry tapers from the first thickness region to the second thickness region. Then the coated current collector is dried and rolled to obtain the desired battery electrode plate.
• the first thickness region, the transition region and the second thickness region mean the electrode material or electrode slurry on the battery electrode plate provided in the present invention.
• the first thickness region location, the transition region location and the second thickness region location means the locations that the electrode material or slurry is occupied on the electrode plate respectively provided in the present invention.
• the detailed method is as follows: coating electrode slurry on the current collector, then scraping the coated slurry to form the first thickness region, the transition region and the second thickness region.
• the thickness of the electrode material in the first thickness region is greater than that in the second thickness region, and the thickness of the electrode material is decreasing gradually in the direction from first thickness region to the second thickness region.
• the coated current collector is dried and rolled to obtain the battery electrode plate.
• the above method is as follows: the locations of the first thickness region, the transition region and the second thickness region are selected respectively. Then the slurry is coated in the first thickness region location, the transition region location and the second thickness region location, and the thickness of the coating is the required thickness of the first thickness region.
• the electrode slurry is scraped in the transition region location and the second thickness region location to form the transition region and the second thickness region.
• the electrode slurry in the first thickness region is thicker than that in the second thickness region, and the thickness of the slurry in the transition region tapers or decreases gradually in the direction from the first thickness region to the second thickness region.
• the coated current collector is dried and rolled to obtain the battery electrode plate.
• the method further can be: before rolling and after drying, scraping the electrode material to form the first thickness region, the transition region and the second thickness region.
• the electrode slurry in the first thickness region is thicker than that in the second thickness region, and the thickness of the slurry descends from the first thickness region to the second thickness region. Then drying and rolling the coated current collector to obtain the battery electrode plate.
• the above method can also be as follows: coating the electrode slurry on the current collector and then scraping the electrode slurry to form the transition region.
• the thickness of the electrode slurry in the transition region decreases in the direction from the first thickness region to the second thickness region. Then the electrode slurry is coated in the second thickness region such that the second thickness region is smoothly connected with the transition region.
• the coated current collector is dried and rolled to obtain the battery electrode plate.
• the above mentioned method is as follows: selecting the location of the first thickness region, the transition region and the second thickness region.
• the electrode slurry is coated in the first thickness region location, the transition region location, and the thickness of the coating is the required thickness of the first thickness region.
• the electrode slurry is scraped in the transition region location to form the transition region.
• the thickness of the slurry in the transition region descends or tapers in the direction from the first thickness region to the second thickness region.
• the electrode slurry is coated in the second thickness region to form the second thickness region, and the thickness of the coating is the required thickness of the second thickness region.
• the coated current collector is dried and rolled to obtain the battery electrode plate.
• the method further can be: before rolling and after drying, scraping the electrode material to form the first thickness region, the transition region and the second thickness region.
• the electrode slurry in the first thickness region is thicker than that in the second thickness region, and the thickness of the slurry descends from the first thickness region to the second thickness region.
• the coated current collector is dried and rolled to obtain the battery electrode plate.
• the above mentioned method is: selecting the location of the first thickness region, the transition region and the second thickness region.
• the electrode slurry is coated in the first thickness region location, the transition region location and the second thickness region location, and the thickness of the coating is the required thickness of the first thickness region. And the coated current collector is dried.
• the electrode slurry in the transition region location and the second thickness region location is scraped to form the transition region and the second thickness region.
• the electrode slurry in the first thickness region is thicker than that in the second thickness region, and the thickness of the slurry in the transition region descends in the direction from the first thickness region to the second thickness region.
• the coated current collector is rolled to obtain the desired battery electrode plate.
• the scraping method can be any method in the prior art, for example, scraping using a blade, and this can be done manually or by a machine. If the descending gradient of the electrode material in the transition region needs to be remained constant, the transition region can be scraped along two lines where the first thickness region and the second thickness region join with the transition region respectively.
• the electrode material in the first thickness region has a thickness of about 20-350um.
• the electrode material in the second thickness region has a thickness of about 10-250um.
• the descending gradient of the electrode material in the transition region is about 5-300um/mm.
• the drying method is the common method used in the prior art, for example, drying under 100 ° C .
• the rolling method is also the method known in the art, for example, rolling under a pressure of about 2.0MPa.
• the thickness and/or width of the electrode material in each region may vary slightly, however the data will be still in the above mentioned range.
• the thickness of the electrode material or the electrode slurry in the first thickness region is about 25-350um
• the thickness of the electrode material or the electrode slurry in the second thickness region is about 15-250um.
• the forming method can be performed by directly coating the above mentioned thickness of electrode slurry.
• the electrode plate prepared according to the above method may have lower risk of drape or wrinkle and the battery having the same may have improved safety performance.
• the positive electrode plate and the negative electrode plate are aligned based on one side in the length direction and overlapped together, and the plates are placed in a staggering manner in the width direction such that the tab regions without coating materials on the positive electrode and negative electrode will be exposed.
• a separator is disposed between the positive electrode plate and the negative electrode plate. The electrode material portion on the negative electrode plate totally covers the electrode material portion on the positive electrode plate. Then the overlapped electrode plates and the separator are coiled to obtain the battery core.
• the separator is the separator known in the field, for example polyethylene.
• an insulating layer is further covered on the electrode material.
• the insulating layer covers at least the transition region and the second thickness region.
• the thickness of the insulating layer may vary in a relatively large range. In an embodiment of the invention, the thickness of the insulating layer is about 5-150um.
• the insulating material can be any material that is commonly used in the field, for example, it can be one or more selected from polyphenylene sulfide, polyurethane, polyethylene and polypropylene.
• the insulating layer can be formed directly by attaching an adhesive tape of the above mentioned material or directly coating the above mention adhesive agent. Normally, it is only required to form an insulating layer on the transition region and the second thickness region of the positive electrode plate. In an embodiment of the invention, attaching an adhesive tape is selected.
• the adhesive tape can be purchased from the market.
• the battery prepared according to the above method may enhance the safety performance of the battery.
• the invention further disclosed a battery comprising a battery shell, a core and electrolyte.
• the battery core and electrolyte are sealed in the battery shell.
• the battery core comprises a positive electrode plate, a negative electrode plate and a separator disposed in between the positive electrode plate and negative electrode plate.
• At least the positive electrode plate is the electrode plate provided in the present invention or formed according to the method in the present invention.
• the battery safety performance may be enhanced by employing the above mentioned electrode plate.
• the method of the battery provided in the invention is known in the art.
• the method comprises coiling the positive electrode plate, negative electrode plate and the separator in between into a core; disposing the battery core in the battery shell, injecting electrolyte into the battery shell and sealing the battery shell.
• the positive electrode comprises a current collector and the positive material coated on the current collector, the positive material comprises positive active material, conductive agent and adhesive agent.
• the coiling and sealing methods are known in the art.
• the dosage of the electrolyte is conventional.
• the battery core is formed by first overlapping the positive electrode plate, the separator, the negative electrode plate and then coiling the overlapped plates and the separator.
• the length of the separator is able to make the terminating end of the separator be longer than the terminating ends of the positive electrode plates and the negative electrode plates.
• the separator is able to encircle at least a circle after the terminating end of the positive electrode plate and the negative electrode plate.
• the separator is able to encircle 1-10 circles after the terminating end of the positive electrode plate and the negative electrode plate. In an embodiment of the invention, the separator is able to encircle 2-6 circles after the terminating end of the positive electrode plate and the negative electrode plate.
• the separator circle at the outer of the battery core will swell during both soakage of the electrolyte and charging-discharging, and the swelling rate is consistent with the battery core, so drape of the battery may be decreased and safety performance may be improved. Meanwhile, the method may enhance the electrolyte soakage and maintain battery performance.
• the manufacturing process may be simplified and the assembly efficiency may be enhanced and thus manpower as well as cost may be decreased.
• the battery core is formed by coiling the overlapped positive electrode plate, separator and negative electrode plate and at least a portion of the circumferential line is arc.
• the terminating end of the positive electrode plate and/or the terminating end of the negative electrode plate is in the arc region of the battery core.
• the battery core may be formed with at least a portion of a curved region in a circumferential direction so that the terminating end of the positive electrode plate and/or the terminating end of the negative electrode plate may terminate therein.
• the curved region may be formed with an arc or semi-circular shape, and the terminating ends of the positive electrode plate and the negative electrode plate may be positioned in the same curved region.
• the circumferential line is the edge line of the battery core in the coiling direction.
• the arc line comprises the lines except for beelines.
• the curved region means the surface area of the battery core where the arc line is located.
• the terminating ends of the positive electrode plate and the negative electrode plate are in the same arc region. That is to say, the curved region may be formed with an arc or semi-circular shape, and the terminating ends of the positive electrode plate and the negative electrode plate may be positioned in the same curved region.
• the inventors further found that, during charging and discharging, as the electrode plate expands and the thickness of the battery core increases and press against the battery shell, the battery shell further counter press the battery core correspondingly.
• the terminating end of the positive electrode plate and/or the terminating end of the negative electrode plate and/or the terminating end of the separator is in the curved region of the battery core. As the curved region is not very close to the battery shell and there is still some space therebetween, thus while the battery core expands, the space between the curved region and the battery shell will buffer and may avoid large stress concentration in the arc area and may prevent drape or wrinkle of the battery core during use.
• the space is bigger between the positive and negative electrode plates where the drape locates and thus charging and discharging may not be uniform, which is beneficial for lithium dendrites to grow. So a lot of lithium dendrites may grow in the drape region and may affect the safety performance of the battery. Setting the terminating end of the positive electrode plate and/or the terminating end of the negative electrode plate and/or the terminating end of the separator in the curved region of the battery core may decrease the negative effects of the lithium dendrites.
• the first embodiment explains the battery electrode plate and the battery using the same according to an embodiment of the invention.
• the positive material, conductive agent, adhesive agent and solvent are mixed and stirred to prepare the positive slurry.
• the current collector is divided according to the above mentioned method into first thickness region location, the transition region location, second thickness region location and the tab region.
• the transition region location has a width of about 4mm.
• the width of the second thickness region location is about 4mm.
• the thickness of the tab region is about 30mm.
• the positive slurry is coated uniformly in the first thickness region location and the transition region location.
• the thickness of the positive slurry is about lOOum.
• the positive slurry in the transition region is thinned gradually using a blade by controlling a machine and obtained the transition region positive slurry with a maximum thickness of about lOOum, a minimum thickness of about 25um and a descending gradient of about 18.75um/mm. Then slurry is coated in the second thickness region location and the thickness of the positive slurry in the second thickness region is about 25um.
• the coated current collector is then dried and rolled and obtained the positive electrode plate.
• the negative material, conductive agent, adhesive agent and solvent are mixed and stirred to prepare the negative slurry.
• Preserving a tab region with a width of 25mm on the negative current collector in the width direction the negative slurry is coated uniformly on the non tab region of the negative current collector and the thickness of the coated slurry is about 90um, then the coated current collector is dried and rolled to obtain the negative electrode plate.
• the positive electrode plate, separator and the negative electrode plate are overlapped such that the positive tab region is relative to the negative tab region and the electrode material on the negative electrode plate fully covers the electrode material on the positive electrode plate, then the overlapped plates and the separator are coiled to obtain the battery core.
• the battery core is then disposed in the battery shell and electrolyte is injected into the battery core, the battery shell is sealed and the obtained battery is denoted as Al .
• Second Embodiment The second embodiment is used to explain the battery electrode plate and the battery according to an embodiment of the invention.
• the method is the same as the example 1, the only difference is that: before coiling, a polyphenylene sulfide tape having a thickness of about 80um is attached on the positive material of the transition region and the second thickness region and the obtained battery is denoted as A2.
• the third embodiment explains the battery electrode plate and the battery using the same according to an embodiment of the invention.
• the positive material, conductive agent, adhesive agent and solvent are mixed and stirred to prepare the positive slurry.
• the current collector is divided according to the above mentioned method to be the first thickness region location, the transition region location, the second thickness region location and the tab region.
• the width of the transition region location is about 6mm
• the width of the second thickness region location is about
• the thickness of the tab region is about 50mm.
• the positive slurry is coated uniformly in the first thickness region location and the transition region location.
• the thickness of the positive slurry is about 90um.
• the positive slurry in the transition region is thinned gradually by a blade mechanically controlled and obtains the transition region positive slurry with a maximum thickness of about
• slurry is coated in the second thickness region location and the thickness of the positive slurry in the second thickness region is about 30um.
• the coated current collector is then dried and rolled and obtains the positive electrode plate.
• the negative material, conductive agent, adhesive agent and solvent are mixed and stirred to prepare the negative slurry.
• the method of the negative electrode plate is basically the same as the above mentioned method of the positive electrode plate, the differences are: the width of the transition region location is about 5mm.
• the width of the second thickness region location is about 5mm.
• the width of the tab region is about 40mm.
• the thickness of the negative slurry is about lOOum.
• the negative slurry in the transition region is thinned gradually by a blade mechanically controlled and obtains the transition region negative slurry with a maximum thickness of about lOOum, a minimum thickness of about 20um and a descending gradient of 16um/mm.
• slurry is coated in the second thickness region location and the thickness of the negative slurry in the second thickness region is about 20um.
• the coated current collector is then dried and rolled to obtain the negative electrode plate.
• the comparative embodiment explains the battery electrode plate and the battery using the same according to the prior art.
• the electrode plate and the battery preparing method is the same as those in the first embodiment, the only difference lies in that the electrode plates are not thinned and the obtained battery is denoted as Dl .
• the fourth embodiment explains the battery according to an embodiment of the invention.
• the method is basically the same as the third embodiment, the only difference is that: before coiling, a polyphenylene sulfide tape having a thickness of about 50um is attached onto the positive material of the transition region and the second thickness region.
• a polyphenylene sulfide tape having a thickness of about 50um is attached onto the positive material of the transition region and the second thickness region.
• the above positive electrode plate, the propylene separator and the negative electrode plate are coiled into a scroll core. While the positive electrode plate and negative electrode plate terminates, the free end of the separator continues coiling the battery core for one more circle and forms a layer of separator out of the positive and negative electrode plates. Then the separator is cut and fixed by the adhesive tape as shown in Fig 2.
• the fifth embodiment explains the battery according to an embodiment of the invention.
• the method of the positive and negative electrode plates and the assembly of the battery are basically the same as the third embodiment, the only difference is that:
• the above positive electrode plate, the propylene separator and the negative electrode plate are coiled into a scroll core, the terminating ends of the positive electrode plate, the negative electrode plate and the separator terminate in the curved region of the battery core.
• the present comparative embodiment explains the battery according to an embodiment of the invention.
• the terminating ends of the positive electrode plate, the negative electrode plate and the separator do not terminate in the curved region of the battery core.
• the obtained battery prepared according to the above method is denoted as D2.
• the present embodiment explains the battery according to an embodiment of the invention.
• the method of the positive and negative electrode plates and the assembly of the battery are basically the same as the first embodiment, the only difference is that: the positive slurry is coated uniformly on the first thickness region location, transition region location and the second thickness region location and the thickness of the coated positive slurry is about lOOum.
• the positive slurry in the transition region and the second thickness region is thinned gradually using a blade mechanically controlled.
• the obtained transition region positive slurry had a maximum thickness of about lOOum, a minimum thickness of about 25um and a descending gradient of about 18.75um/mm. and the thickness in the second thickness region is about 25um.
• the coated electrode plates are dried and rolled to obtain the positive electrode plate.
• the width of the first thickness region is about 4mm and the thickness of the positive material is about 90um.
• the width of the transition region is about 4mm and the positive material had a maximum thickness of 90um, a minimum thickness of 21um.
• the thickness of the positive material in the second thickness region is about 21um.
• the battery prepared according to the above method is denoted as A6.
• the present embodiment explains the battery according to an embodiment of the invention.
• the method of the positive and negative electrode plates and the assembly of the battery are basically the same as the sixth embodiment, the only difference is that: the positive slurry is coated uniformly on the first thickness region location, transition region location and the second thickness region location.
• the thickness of the coated positive slurry is about lOOum.
• the coated current collector is dried.
• the positive slurry in the transition region and the second thickness region is thinned gradually using a blade by controlling the machine.
• the obtained transition region positive slurry had a maximum thickness of about lOOum, a minimum thickness of about 25um and a descending gradient of about 18.75um/mm and the thickness in the second thickness region is about 25um.
• the coated electrode plates are dried and rolled to obtain the positive electrode plate.
• the width of the first thickness region is about 4mm and the thickness of the positive material is about 88um.
• the width of the transition region is about 4mm and the positive material had a maximum thickness of 88um, a minimum thickness of 20um.
• the thickness of the positive material in the second thickness region is about 20um.
• the battery prepared according to the above method is denoted as A7.
• the electrode plates according to the present invention have high yield rates and the safety performances thereof are improved greatly. Further, after adding insulating layer on the transition region and the second thickness region is beneficial for battery safety performance.
• Battery Core Performance Test Batteries according to the above first to fifth embodiments and the first, second comparative embodiments are prepared, and 100 batteries each for Al, A2, A3, A4, A5 and Dl and D2 are obtained respectively.
• the batteries are charged under a constant current of 3.2 A, the upper limit charging voltage is 3.8V, the lower limit charging limit is 2.2V, the cutoff current is 0.2A, and laying aside for 10 minutes.
• the batteries are discharged at a constant current of 8 A with a cutoff voltage of 2.0V
• the batteries are charged and discharged for 10 cycles. And then the batteries are detached to determine if the battery core has any drape or macroscopic dendrite or alloy.
• Battery core draping rate the amount of the batteries having drape/100
• the dendrite rate is used to describe a probability rate of the dendrite or alloy occurred in the battery core, viz:
• Dendrite rate the amount of the batteries having dendrite or alloy/100. The test result is shown in the following table 2. Table 2
• the separator encircles another circle of the battery core, or the terminating ends of the electrode plates and/or separator are located in the curved region, the rate of drape, dendrite or alloy in the battery during charging or discharging thus further enhances the battery safety performance.

Landscapes

• Chemical & Material Sciences (AREA)
• Engineering & Computer Science (AREA)
• Chemical Kinetics & Catalysis (AREA)
• Electrochemistry (AREA)
• General Chemical & Material Sciences (AREA)
• Manufacturing & Machinery (AREA)
• Materials Engineering (AREA)
• Secondary Cells (AREA)
• Battery Electrode And Active Subsutance (AREA)
• Cell Electrode Carriers And Collectors (AREA)

Priority Applications (3)

Applications Claiming Priority (8)

Publications (1)

Family

ID=41789893

Family Applications (1)

Country Status (5)

Cited By (9)

Families Citing this family (27)

Citations (5)

Family Cites Families (15)

• 2008
  • 2008-11-14 CN CN2008101818163A patent/CN101662011B/zh active Active
• 2009
  • 2009-08-27 KR KR1020117005993A patent/KR101324213B1/ko active Active
  • 2009-08-27 JP JP2011524170A patent/JP5685536B2/ja active Active
  • 2009-08-27 WO PCT/CN2009/073582 patent/WO2010022669A1/en not_active Ceased
  • 2009-08-27 EP EP09809254.7A patent/EP2319109B1/en active Active

Patent Citations (5)

Non-Patent Citations (1)

Also Published As

Similar Documents

Legal Events