WO2023184246A1 - Negative electrode sheet, electrochemical apparatus, and electronic apparatus - Google Patents

Negative electrode sheet, electrochemical apparatus, and electronic apparatus Download PDF

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Publication number
WO2023184246A1
WO2023184246A1 PCT/CN2022/084118 CN2022084118W WO2023184246A1 WO 2023184246 A1 WO2023184246 A1 WO 2023184246A1 CN 2022084118 W CN2022084118 W CN 2022084118W WO 2023184246 A1 WO2023184246 A1 WO 2023184246A1
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Prior art keywords
region
active material
negative electrode
present application
material particles
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PCT/CN2022/084118
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French (fr)
Chinese (zh)
Inventor
李铎
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宁德新能源科技有限公司
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Priority to PCT/CN2022/084118 priority Critical patent/WO2023184246A1/en
Priority to CN202280005053.5A priority patent/CN116097465A/en
Publication of WO2023184246A1 publication Critical patent/WO2023184246A1/en

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    • 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
    • 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
    • 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
    • H01M4/133Electrodes based on carbonaceous material, e.g. graphite-intercalation compounds or CFx
    • 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
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • 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
    • H01M4/64Carriers or collectors
    • 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

Definitions

  • the present application relates to the field of energy storage, and specifically relates to a negative electrode plate, an electrochemical device and an electronic device.
  • the purpose of this application is to provide a negative electrode plate, an electrochemical device and an electronic device.
  • the negative electrode plate can not only increase the energy density of the electrochemical device, but also keep the electrochemical device in good condition. cycle performance.
  • the present application provides a negative electrode sheet, which includes a current collector and a negative active material layer.
  • the negative active material layer includes a first region and a second region, wherein the porosity of the first region is smaller than that of the second region.
  • the porosity of the region, the ratio of the Dv50 of the active material particles in the first region to the Dv50 of the active material particles in the second region, is 0.3 to 0.9.
  • the negative electrode plate includes a first region and a second region.
  • the first region includes at least one dense region composed of small particles
  • the above-mentioned second region includes at least one non-dense region composed of large particles.
  • the first area can not only increase the energy density of the electrochemical device, but also has strong adhesion to the pole piece and is difficult to demould, thereby effectively improving the stability of the pole piece and avoiding pole piece deformation.
  • the particle size of the second area is relatively large and the porosity is large, which is conducive to the storage of electrolyte, and provides a rapid diffusion channel for the electrolyte inside the pole piece, which is conducive to the rapid diffusion and retention of electrolyte, and works in conjunction with the surrounding dense areas , reducing the electrolyte transport path in the first area and improving dynamics.
  • the Dv50 of the active material particles in the first region is 5 ⁇ m to 20 ⁇ m.
  • the Dv50 of the active material particles in the second region is 20 ⁇ m to 50 ⁇ m.
  • the Dv50 of the active material particles in the first region and the second region meets the above range.
  • the negative active material layer can maintain appropriate electrode plate reactivity and reduce unreasonable particle size while ensuring its overall wettability in the electrolyte. Side reactions caused by distribution, reduce production difficulty, and improve the yield rate during the pole piece production process.
  • the first region has a porosity of 15% to 30%.
  • the second region has a porosity of 30% to 45%.
  • the porosity of the first region and the porosity of the second region meet the above range.
  • the negative active material layer can reduce the concentration polarization of the electrochemical device and reduce the internal resistance while ensuring the wettability and diffusion ability of the electrolyte. Significantly improve the energy density of the pole piece.
  • the thickness of the negative active material layer is 50 ⁇ m to 300 ⁇ m.
  • the thickness of the negative active material layer is within the above range, which can further improve the electrolyte wettability and diffusion ability of the electrode piece in the thickness direction while optimizing the energy density of the electrochemical device.
  • the thickness of the negative active material layer is 100 ⁇ m to 250 ⁇ m.
  • the active material particles in the first region and/or the second region are arranged in an array or in a non-array arrangement.
  • the active material particles in the first region and/or the second region are arranged in an array, and the aspect ratio of the active material particles is 1.1 to 5.
  • the active material particles in the first region and the second region are arranged in an array, which is conducive to the rapid insertion and extraction of lithium ions.
  • an angle between the active material particles in the first region and/or the second region and the current collector along the long diameter direction is 45° to 135°.
  • the active material particles are arranged with the current collector within this angle range, which shortens the diffusion path of lithium ions, which is beneficial to improving dynamics.
  • the projected area of the second region accounts for 5% to 50%. In this range, the electrolyte diffusion efficiency can be improved , which is beneficial to improving dynamics.
  • the second area is distributed in a stripe shape or an island shape.
  • the second region is disposed through the negative electrode plate in the width direction.
  • the bonding force of the negative electrode piece is 5 N/m to 15 N/m.
  • the particle size of the active material particles in the second region is smaller, the specific surface area is larger, and the interaction force with the binder is stronger.
  • the larger the contact area between the second region and the current collector the stronger the bonding force, and the greater its own bonding force;
  • the strong bonding force can prevent the pole piece from being demolded during processing and use or abuse of the electrode assembly.
  • the ratio of the width of the first area to the width of the second area is 1 to 20, and the second area is distributed in a stripe shape or an island shape. According to some embodiments of the present application, the ratio of the first area width to the second area width is 1 to 10.
  • the first area width and the second area width refer to the first area width and the second area width of the negative electrode plate surface layer.
  • the first area width is 1 mm to 50 mm.
  • the second area is distributed in an island shape and the shape of each island is a square or a rectangle.
  • the ratio of the thickness of the first region to the thickness of the second region is 1 to 2.
  • the ratio of the thickness of the first region to the thickness of the second region within this range can improve the electrolyte diffusion efficiency and is beneficial to improving dynamics.
  • a primer layer is further provided between the current collector and the negative active material layer.
  • the setting of the undercoat can increase the adhesion between the negative active material and the current collector, and effectively reduce demoulding, deformation and other phenomena caused by the differentiated design of different areas of the negative electrode piece.
  • the base coating includes conductive materials, binders, and dispersants.
  • the conductive material in the undercoat layer includes at least one of conductive carbon black, carbon fiber, Ketjen black, acetylene black, carbon nanotubes and graphene.
  • the adhesive includes styrene-butadiene rubber.
  • the dispersant includes sodium carboxymethylcellulose.
  • the active material particles in the first region and/or the second region are arranged in a non-array arrangement, and the thickness of the undercoat layer is 0.5 ⁇ m to 1.5 ⁇ m.
  • the active material particles in the first region and/or the second region are arranged in an array, and the thickness of the undercoat layer is 1.5 ⁇ m to 3.0 ⁇ m. This is because after the active material particles are arranged in an array, The adhesion ability to the current collector becomes poor. Increasing the thickness of the primer layer can improve the adhesion and prevent demolding.
  • the present application provides an electrochemical device, which includes the negative electrode piece as described in the first aspect of the present application.
  • the present application provides an electronic device, including the electrochemical device according to the second aspect of the present application.
  • the negative electrode sheet provided by this application can not only increase the energy density of the electrochemical device, but also maintain good cycle performance of the electrochemical device.
  • Figure 1 is a schematic cross-sectional view of a negative electrode sheet in the length direction according to some embodiments of the present application, where 1 is a copper current collector, 2 is an undercoat layer, 3 is a small particle dense area, and 4 is a large particle non-dense area.
  • Figure 2 is a schematic cross-sectional view of the negative electrode sheet in the length direction according to other embodiments of the present application, in which 1 is a copper current collector, 2 is an undercoat layer, 3 is a small particle dense area, and 4 is a large particle non-dense area. .
  • FIG. 3 is a schematic top view of a negative electrode plate according to some embodiments of the present application, in which the second area is distributed in a strip shape.
  • FIG. 4 is a schematic top view of a negative electrode sheet according to other embodiments of the present application, in which the second area is distributed in a strip shape.
  • FIG. 5 is a schematic top view of a negative electrode piece according to other embodiments of the present application, in which the second area is distributed in an island shape.
  • a list of items connected by the terms “at least one of,” “at least one of,” “at least one of,” or other similar terms may mean any combination of the listed items. For example, if items A and B are listed, the phrase “at least one of A and B” means only A; only B; or A and B. In another example, if the items A, B, and C are listed, then the phrase "at least one of A, B, and C" means only A; or only B; only C; A and B (excluding C); A and C (excluding B); B and C (excluding A); or all of A, B and C.
  • Item A may contain a single component or multiple components.
  • Item B may contain a single component or multiple components.
  • Item C may contain a single component or multiple components.
  • the present application provides a negative electrode sheet, which includes a current collector and a negative active material layer.
  • the negative active material layer includes a first region and a second region, wherein the porosity of the first region is smaller than that of the second region.
  • the porosity of the region, the ratio of the Dv50 of the active material particles in the first region to the Dv50 of the active material particles in the second region, is 0.3 to 0.9.
  • the negative electrode piece has two regions, a first region composed of small particles and a second region composed of large particles.
  • the first area mainly contributes to the energy density of the electrochemical device;
  • the second area has a relatively large particle size and a large porosity, which is conducive to storing electrolyte and providing a fast channel for the electrolyte to diffuse into the interior of the pole piece, which is conducive to the rapid development of electrolyte.
  • Diffusion and liquid retention simultaneously bring electrolyte supply to the surrounding first area, reduce the electrolyte transport path in the first area, and improve dynamics.
  • the Dv50 of the active material particles in the first region is 5 ⁇ m to 20 ⁇ m. In some embodiments, the Dv50 of the active material particles in the first region is in a range of 5 ⁇ m, 8 ⁇ m, 12 ⁇ m, 15 ⁇ m, 18 ⁇ m, 20 ⁇ m, or any two thereof. According to some embodiments of the present application, the Dv50 of the active material particles in the second region is 20 ⁇ m to 50 ⁇ m.
  • the Dv50 of the active material particles in the second region is a range of 20 ⁇ m, 25 ⁇ m, 28 ⁇ m, 32 ⁇ m, 35 ⁇ m, 42 ⁇ m, 45 ⁇ m, 50 ⁇ m, or any two thereof.
  • the Dv50 of the active material particles in the first region and the second region meets the above range.
  • the negative active material layer can maintain appropriate electrode plate reactivity and reduce unreasonable particle size while ensuring its overall wettability in the electrolyte. Side reactions caused by distribution, reduce production difficulty, and improve the yield rate during the pole piece production process.
  • the first region has a porosity of 15% to 30%. In some embodiments, the porosity of the first region ranges from 15%, 18%, 20%, 25%, 28%, 30%, or any two thereof.
  • the second region has a porosity of 30% to 45%. In some embodiments, the porosity of the second region ranges from 30%, 35%, 40%, 45%, or any two thereof. The porosity of the first region and the porosity of the second region meet the above range.
  • the negative active material layer can significantly increase the energy density of the pole piece while ensuring the electrolyte wettability and diffusion ability of the first region.
  • the thickness of the negative active material layer is 50 ⁇ m to 300 ⁇ m. In some embodiments, the thickness of the negative active material layer is 50 ⁇ m, 60 ⁇ m, 70 ⁇ m, 80 ⁇ m, 90 ⁇ m, 100 ⁇ m, 120 ⁇ m, 150 ⁇ m, 180 ⁇ m, 200 ⁇ m, 220 ⁇ m, 240 ⁇ m, 260 ⁇ m, 280 ⁇ m, 300 ⁇ m, or any two thereof. scope. The thickness of the negative active material layer is within the above range, which can ensure the wettability and diffusion ability of the electrolyte and significantly increase the energy density of the electrode piece. According to some embodiments of the present application, the thickness of the negative active material layer is 100 ⁇ m to 250 ⁇ m.
  • the active material particles in the first region and/or the second region are arranged in an array or in a non-array arrangement. According to some embodiments of the present application, the active material particles in the first region and/or the second region are arranged in an array, and the aspect ratio of the active material particles is 1.1 to 5. The active material particles in the first region and the second region are arranged in an array, which is conducive to the rapid insertion and extraction of lithium ions. According to some embodiments of the present application, the active material particles have an aspect ratio of 1.5 to 5. According to some embodiments of the present application, the active material particles have an aspect ratio of 2 to 5.
  • an angle between the active material particles in the first region and/or the second region and the current collector along the long diameter direction is 45° to 135°.
  • the angle between the active material particles in the first region and the current collector along the long diameter direction is 45° to 135°, such as 45°, 50°, 55°, 60°, 65°, 70°, 75°, 80°, 85°, 90°, 95°, 100°, 105°, 110°, 115°, 120°, 125°, 130°, 135° or a range consisting of any two of them.
  • the angle between the active material particles in the second region and the current collector along the long diameter direction is 45° to 135°, such as 45°, 50°, 55°, 60°, 65°, 70°, 75°, 80°, 85°, 90°, 95°, 100°, 105°, 110°, 115°, 120°, 125°, 130°, 135° or a range consisting of any two of them.
  • the active material particles are arranged with the current collector within this angle range, which shortens the diffusion path of lithium ions, which is beneficial to improving dynamics.
  • the projected area of the second region accounts for 5% to 50%. In this range, the electrolyte diffusion efficiency can be improved , which is beneficial to improving dynamics.
  • the projected area ratio of the second region is 5%, 10%, 15%, 20%, 25%, 30% , 35%, 40%, 45%, 50% or a range consisting of any two of them.
  • the projected area of the second region accounts for 15% to 30%.
  • the second area is distributed in a strip shape or in an island shape.
  • the second region is disposed through the negative electrode plate in the width direction.
  • the bonding force of the negative electrode piece is 5 N/m to 15 N/m.
  • the bonding force of the negative electrode piece is 5N/m, 6N/m, 7N/m, 8N/m, 9N/m, 10N/m, 11N/m, 12N/m, 13N/m, 14N/m, 15N/m or a range consisting of any two of them.
  • the particle size of the active material particles in the second region is smaller, the specific surface area is larger, and the interaction force with the binder is stronger. The larger the contact area between the second region and the current collector, the stronger the bonding force, and the greater its own bonding force; The strong bonding force can prevent the pole piece from being demolded during processing and use or abuse of the electrode assembly.
  • the ratio of the width of the first area to the width of the second area is 1 to 20, and the second area is distributed in a stripe shape or an island shape.
  • the ratio of the width of the first region to the width of the second region is a range of 1, 3, 5, 7, 10, 12, 15, 18, 20, or any two of them.
  • the ratio of the first area width to the second area width is 1 to 10.
  • the first area width and the second area width refer to the first area width and the second area width of the negative electrode plate surface layer.
  • the width of the first area is 1 mm to 50 mm, such as a range of 1 mm, 5 mm, 10 mm, 15 mm, 20 mm, 25 mm, 30 mm, 35 mm, 40 mm, 45 mm, 50 mm or any two of them.
  • the second area is distributed in an island shape and the shape of each island is a square or a rectangle.
  • the ratio of the thickness of the first region to the thickness of the second region is 1 to 2.
  • the ratio of the thickness of the first region to the thickness of the second region is a range consisting of 1, 1.2, 1.4, 1.6, 1.8, 2, or any two of them. The ratio of the thickness of the first region to the thickness of the second region within this range can improve the electrolyte diffusion efficiency and is beneficial to improving dynamics.
  • a primer layer is further provided between the current collector and the negative active material layer.
  • the setting of the undercoat can increase the adhesion between the negative active material and the current collector, and effectively reduce demoulding, deformation and other phenomena caused by the differentiated design of different areas of the negative electrode piece.
  • the conductive material in the undercoat layer includes at least one of conductive carbon black, carbon fiber, Ketjen black, acetylene black, carbon nanotubes and graphene.
  • the adhesive includes styrene-butadiene rubber.
  • the dispersant includes sodium carboxymethylcellulose.
  • the active material particles in the first region and/or the second region are arranged in a non-array arrangement, and the thickness of the undercoat layer is 0.5 ⁇ m to 1.5 ⁇ m.
  • the active material particles in the first region and/or the second region are arranged in an array, and the thickness of the undercoat layer is 1.5 ⁇ m to 3.0 ⁇ m. This is because after the active material particles are arranged in an array, The adhesion ability to the current collector becomes poor. Increasing the thickness of the primer layer can improve the adhesion and prevent demolding.
  • the active material in the negative active material layer is graphite.
  • the negative electrode also includes a current collector, which may include: copper foil, nickel foil, stainless steel foil, titanium foil, nickel foam, copper foam, coated with conductive material.
  • the negative active material layer is metal. Polymer base or any combination thereof.
  • the negative active material layer may further include a conductive agent and/or a binder.
  • the conductive agent includes at least one of conductive carbon black, acetylene black, carbon nanotubes, Ketjen black, conductive graphite, or graphene. In some embodiments, the conductive agent accounts for 0.5% to 10% by mass of the active material layer.
  • the binder includes polyvinylidene fluoride, vinylidene fluoride-hexafluoropropylene copolymer, polyamide, polyacrylonitrile, polyacrylic ester, polyacrylic acid, polyacrylate, sodium carboxymethylcellulose , at least one of polyvinylpyrrolidone, polyvinyl ether, polymethylmethacrylate, polytetrafluoroethylene, polyhexafluoropropylene or styrene-butadiene rubber. In some embodiments, the binder accounts for 0.5% to 10% by mass of the active material layer.
  • the electrochemical device of the present application includes any device that generates electrochemical reactions, and specific examples thereof include all types of primary batteries and secondary batteries.
  • the electrochemical device is a lithium secondary battery, including a lithium metal secondary battery, a lithium ion secondary battery, a lithium polymer secondary battery or a lithium ion polymer secondary battery.
  • the electrochemical device of the present application includes a positive electrode, a negative electrode, a separator and an electrolyte.
  • the negative electrode in the electrochemical device of the present application includes the negative electrode piece of the first aspect.
  • the materials, composition and manufacturing methods of the positive electrode that can be used in the embodiments of the present application include any technology disclosed in the prior art.
  • the positive electrode includes a current collector and a positive active material layer located on the current collector.
  • the cathode active material includes, but is not limited to: lithium cobalt oxide (LiCoO 2 ), lithium nickel cobalt manganate (NCM), lithium nickel cobalt aluminate, lithium iron phosphate (LiFePO 4 ) or manganese Lithium oxide (LiMn 2 O 4 ).
  • the positive active material layer further includes a binder and optionally a conductive material.
  • the binder improves the binding of the positive active material particles to each other and also improves the binding of the positive active material to the current collector.
  • the binder includes: polyvinyl alcohol, hydroxypropyl cellulose, diacetyl cellulose, polyvinyl chloride, carboxylated polyvinyl chloride, polyvinyl fluoride, ethylene oxide-containing polymers , polyvinylpyrrolidone, polyurethane, polytetrafluoroethylene, polyvinylidene fluoride, polyethylene, polypropylene, styrene-butadiene rubber, acrylic (ester) styrene-butadiene rubber, epoxy resin or nylon, etc.
  • conductive materials include, but are not limited to: carbon-based materials, metal-based materials, conductive polymers, and mixtures thereof.
  • the carbon-based material is selected from carbon black, acetylene black, Ketjen black, carbon fiber, carbon nanotubes, or any combination thereof.
  • the metal-based material is selected from metal powders, metal fibers, copper, nickel, aluminum, or silver.
  • the conductive polymer is a polyphenylene derivative.
  • the current collector may include, but is not limited to: aluminum.
  • the electrolyte solution that can be used in the embodiments of the present application may be an electrolyte solution known in the art.
  • the electrolyte includes an organic solvent, a lithium salt, and additives.
  • the organic solvent of the electrolyte solution according to the present application may be any organic solvent known in the prior art that can be used as a solvent for the electrolyte solution.
  • the electrolyte used in the electrolyte solution according to the present application is not limited, and it can be any electrolyte known in the prior art.
  • the additives of the electrolyte according to the present application may be any additives known in the art that can be used as electrolyte additives.
  • organic solvents include, but are not limited to: ethylene carbonate (EC), propylene carbonate (PC), diethyl carbonate (DEC), ethyl methyl carbonate (EMC), dimethyl carbonate (DMC) ), propylene carbonate or ethyl propionate.
  • lithium salts include, but are not limited to: lithium hexafluorophosphate LiPF 6 , lithium tetrafluoroborate LiBF 4 , lithium difluorophosphate LiPO 2 F 2 , lithium bistrifluoromethanesulfonimide LiN (CF 3 SO 2 ) 2 (abbreviated as LiTFSI), lithium bis(fluorosulfonyl)imide Li(N(SO 2 F) 2 ) (abbreviated as LiFSI), lithium bisoxalatoborate LiB(C 2 O 4 ) 2 (abbreviated as LiBOB) or Lithium difluorooxalate borate LiBF 2 (C 2 O 4 ) (abbreviated as LiDFOB).
  • LiTFSI lithium bistrifluoromethanesulfonimide LiN (CF 3 SO 2 ) 2
  • LiFSI lithium bis(fluorosulfonyl)imide Li(N(SO 2 F) 2 )
  • LiBOB lithium bis
  • the concentration of lithium salt in the electrolyte is: 0.5 mol/L to 3 mol/L, 0.5 mol/L to 2 mol/L, or 0.8 mol/L to 1.5 mol/L.
  • the isolation membrane used in the electrochemical device of the present application are not particularly limited, and it can be any technology disclosed in the prior art.
  • the isolation membrane includes polymers or inorganic substances formed of materials that are stable to the electrolyte of the present application.
  • the isolation film may include a base material layer and a surface treatment layer.
  • the base material layer is a non-woven fabric, film or composite film with a porous structure.
  • the base material layer is made of at least one material selected from the group consisting of polyethylene, polypropylene, polyethylene terephthalate and polyimide.
  • polypropylene porous membrane, polyethylene porous membrane, polypropylene non-woven fabric, polyethylene non-woven fabric or polypropylene-polyethylene-polypropylene porous composite membrane can be used.
  • a surface treatment layer is provided on at least one surface of the base layer.
  • the surface treatment layer may be a polymer layer or an inorganic layer, or may be a layer formed by mixing a polymer and an inorganic layer.
  • the inorganic layer includes inorganic particles and a binder.
  • the inorganic particles are selected from aluminum oxide, silicon oxide, magnesium oxide, titanium oxide, hafnium dioxide, tin oxide, ceria, nickel oxide, zinc oxide, calcium oxide, zirconium oxide, At least one of yttrium oxide, silicon carbide, boehmite, aluminum hydroxide, magnesium hydroxide, calcium hydroxide and barium sulfate.
  • the binder is selected from polyvinylidene fluoride, vinylidene fluoride-hexafluoropropylene copolymer, polyamide, polyacrylonitrile, polyacrylate, polyacrylic acid, polyacrylate, polyvinylpyrrolidone, polyethylene alkoxy , at least one of polymethylmethacrylate, polytetrafluoroethylene and polyhexafluoropropylene.
  • the polymer layer contains a polymer, and the material of the polymer is selected from polyamide, polyacrylonitrile, acrylate polymer, polyacrylic acid, polyacrylate, polyvinylpyrrolidone, polyethylene alkoxy, polyvinylidene fluoride, At least one of poly(vinylidene fluoride-hexafluoropropylene).
  • the present application further provides an electronic device, which includes the electrochemical device of the second aspect of the present application.
  • electronic devices of the present application include, but are not limited to, notebook computers, pen-input computers, mobile computers, e-book players, portable telephones, portable fax machines, portable copiers, portable printers, and stereo headsets. , VCR, LCD TV, portable cleaner, portable CD player, mini disc, transceiver, electronic notepad, calculator, memory card, portable recorder, radio, backup power supply, drone, motor, car, motorcycle, Power bicycles, bicycles, lighting equipment, toys, game consoles, clocks, power tools, flashlights, cameras, large household batteries and lithium-ion capacitors, etc.
  • DC internal resistance test Charge the lithium-ion battery to 50% SOC at 0.2C, let it sit for 30 minutes, then discharge it at 0.1C for 1s, and then discharge it at 1C for 1s. Calculate the ratio of the voltage difference to the current difference at the end of the two discharge points. Get the DC internal resistance.
  • Rate discharge test charge to 4.4V at a constant voltage of 0.2C, then charge to a constant voltage of 0.02C, let it sit for 30 minutes, discharge it to 3.0V at 0.2C to get the actual capacity of the lithium-ion battery, and then fully charge it in the same way and let it stand. After 30 minutes, 3C was discharged to 3.0V to obtain the lithium-ion battery capacity, and compared with the actual capacity, the capacity retention rate was calculated.
  • Preparation of the positive electrode Use 12 ⁇ m aluminum foil as the current collector of the positive electrode, mix the positive active material lithium cobalt oxide, conductive agent conductive carbon black, and polyvinylidene fluoride in a weight ratio of 97.5:1.5:1.0, and use electrostatic spraying to spray the powder onto the aluminum current collector, and then undergo cold pressing and cutting to obtain the positive electrode piece with the required thickness and size.
  • the first powder is sprayed onto a copper current collector with a thickness of 6 ⁇ m to prepare the first area; then graphite with a Dv50 of 30 ⁇ m, sodium carboxymethylcellulose (CMC) and binder styrene-butadiene rubber are used in a weight ratio of 97.7:1.3: 1 is mixed to obtain a second powder, and electrostatic spraying is used to spray the second powder onto the corresponding second area on the copper current collector. Then, the negative electrode piece is obtained through cold pressing and cutting.
  • CMC sodium carboxymethylcellulose
  • electrostatic spraying is used to spray the second powder onto the corresponding second area on the copper current collector.
  • isolation film The base material of the isolation film is 8 ⁇ m thick polyethylene (PE). A 2 ⁇ m alumina ceramic layer is coated on both sides of the isolation film base material. Finally, 2.5 ⁇ m alumina ceramic layer is coated on both sides of the ceramic layer. mg/cm 2 binder polyvinylidene fluoride (PVDF), dried.
  • PE polyethylene
  • PVDF polyvinylidene fluoride
  • EC ethylene carbonate
  • PC propylene carbonate
  • DEC diethyl carbonate
  • DMC dimethyl carbonate
  • Preparation of lithium-ion battery Stack the positive electrode sheet, isolation film, and negative electrode sheet in order, so that the isolation film is between the positive electrode sheet and the negative electrode sheet for isolation, and wind it to obtain the electrode assembly.
  • the electrode assembly is placed in the outer packaging aluminum plastic film, and after the moisture is removed at 80°C, the above-mentioned electrolyte is injected and packaged. After formation, degassing, trimming and other processes, a lithium-ion battery is obtained.
  • Example 1-1 to Example 1-11 Comparative Example 1-3 and Comparative Example 1-4 in Table 1: the appropriate distribution of the first region and the second region in the negative active material layer, specifically , the thickness ratio, width ratio, area ratio, particle size and porosity of the first region and the second region are within the scope of the present application.
  • the DC internal resistance of the lithium-ion battery is significantly reduced, thereby achieving a relatively high rate of discharge at a high rate. High capacity retention rate.
  • Comparative Example 1-1 nor Comparative Example 1-2 has the first region and the second region of the present application.
  • Comparative Example 1-1 only has small particles of graphite.
  • Examples 2-1 to 2-8 all adopt the stripe morphology in the length direction of the pole piece (as shown in Figure 4), as detailed in Table 2 below.
  • the thickness ratio, width ratio, area ratio, particle size and porosity of the first region and the second region are all within the scope of the present application. It is beneficial to improve the electrolyte diffusion efficiency, and the DC internal resistance of the lithium-ion battery is significantly reduced, thereby achieving a higher capacity retention rate under high-rate discharge, which is beneficial to improving the dynamic performance of the electrochemical device.
  • Examples 3-1 to 3-7 all adopt island-like distribution morphology (as shown in Figure 5), as detailed in Table 3 below.
  • the thickness ratio, width ratio, area ratio, particle size and porosity of the first region and the second region are within the scope of this application, which is beneficial to By improving the electrolyte diffusion efficiency, the DC internal resistance of the lithium-ion battery is significantly reduced, thereby achieving a higher capacity retention rate under high-rate discharge, which is beneficial to improving the kinetic performance of the electrochemical device.
  • the active material particles in the first region and the second region are arranged in a non-array, according to Embodiments 1-1 to 1-8, Embodiments 2-1 to 2-8 and Comparison of Examples 3-1 to 3-8 found that in the technical solution in which the second region is provided along the width direction of the pole piece, the DC internal resistance and discharge capacity retention rate of the electrochemical device are better than that in which the second region is provided along the length direction. This may be due to the fact that when the electrode assembly is wound along the length direction, the electrolyte can be infiltrated from both ends of the wound electrode assembly, and the second area arranged through the width direction of the pole piece is helpful for electrolysis.
  • the regional diffusion of the liquid improves the DC internal resistance of the electrochemical device and maintains a better capacity retention rate in higher rate discharges.
  • the proportion of the second region is small, so the DC internal resistance is relatively large, and the 3C discharge rate capacity retention rate is low, but the increased proportion of the first region can increase the energy density.
  • Preparation of array negative electrode Dissolve small particle size graphite, sodium carboxymethylcellulose (CMC) and binder styrene-butadiene rubber in deionized water at a weight ratio of 97.7:1.3:1 to form a small particle negative electrode slurry.
  • CMC carboxymethylcellulose
  • binder styrene-butadiene rubber Dissolve small particle size graphite, sodium carboxymethylcellulose (CMC) and binder styrene-butadiene rubber in deionized water at a weight ratio of 97.7:1.3:1 to form a small particle negative electrode slurry.
  • the solid content is 70%; the preparation of large-particle anode slurry is the same as that of small particles; 3D printing technology is used to extrude the small-particle anode slurry perpendicularly to the current collector onto a 6 ⁇ m Cu current collector, and a thermal light source is used to volatilize water at the same time, and the printed The slurry is cured in a short time to form the required morphology; then 3D printing is used to print the large particle slurry to the corresponding position, and then cold pressed and cut to obtain the array negative electrode piece, in which the aspect ratio of the active material particle raw material is 2 to 5.
  • the thickness of array-arranged graphite can be 120 ⁇ m to reach the kinetic level of 100 ⁇ m for non-array-arranged graphite.
  • Examples 5-1 to 5-7 all adopt the stripe morphology in the length direction of the pole piece, as detailed in Table 5 below.
  • the thickness ratio, width ratio, area ratio, particle size and porosity of the first region and the second region are all within the scope of the present application. It is beneficial to improve the electrolyte diffusion efficiency, and the DC internal resistance of the lithium-ion battery is significantly reduced, thereby achieving a higher capacity retention rate under high-rate discharge, which is beneficial to improving the dynamic performance of the electrochemical device.
  • Example 2-7 By comparing Example 2-7 with Example 5-1 or by comparing Example 2-8 with Example 5-5, it can be seen that since the negative electrode adopts an array arrangement , the kinetic performance of the electrochemical device can be further improved.
  • Examples 6-1 to 6-7 all adopt island morphology, as shown in Table 6 below.
  • the thickness ratio, width ratio, area ratio, particle size and porosity of the first region and the second region are within the scope of this application, which is beneficial to improving The electrolyte diffusion efficiency and the DC internal resistance of lithium-ion batteries are significantly reduced, thereby achieving a higher capacity retention rate under high-rate discharge, which is beneficial to improving the kinetic performance of the electrochemical device. .
  • Example 3-7 By comparing the examples in Table 3 and Table 6, for example, by comparing Example 3-7 with Example 6-1, it can be seen that since the negative electrode is arranged in an array, the kinetic performance of the electrochemical device can be further improved.

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Abstract

A negative electrode sheet, comprising a current collector and a negative electrode active material layer. The negative electrode active material layer comprises a first region and a second region, the porosity of the first region being lower than that of the second region, and the ratio of active material particles Dv50 of the first region to active material particles Dv50 of the second region being 0.3-0.9. An electrochemical apparatus, comprising a negative electrode sheet.

Description

一种负极极片、电化学装置和电子装置Negative electrode plate, electrochemical device and electronic device 技术领域Technical field
本申请涉及储能领域,具体涉及一种负极极片、电化学装置和电子装置。The present application relates to the field of energy storage, and specifically relates to a negative electrode plate, an electrochemical device and an electronic device.
背景技术Background technique
市场对锂电池能量密度提升仍保持着强烈的需求,然而提升能量密度的常规手段存在各自的问题。提升能量密度的一种手段是增加极片活性材料的涂覆重量,但是如此会带来动力学的恶化,特别是负极材料会出现严重的浓差极化,导致充电放电倍率大的情况下温升高,低温析锂等问题。提升能量密度的另外一种手段是提高压实密度,但是同样会带来动力学恶化,而且过大的压实密度会造成保液量不足,容易出现循环容量衰减的问题。The market still maintains a strong demand for increasing the energy density of lithium batteries. However, conventional means of increasing energy density have their own problems. One way to increase the energy density is to increase the coating weight of the active material of the pole piece. However, this will cause deterioration of the kinetics. In particular, the negative electrode material will have severe concentration polarization, resulting in high temperature at high charge and discharge rates. Increase, low temperature lithium precipitation and other issues. Another way to increase energy density is to increase compaction density, but this will also lead to deterioration of dynamics, and excessive compaction density will result in insufficient liquid retention and prone to circulation capacity attenuation.
发明内容Contents of the invention
针对现有技术存在的问题,本申请的目的在于提供一种负极极片、电化学装置和电子装置,该负极极片不仅能够提升电化学装置的能量密度,同时还使电化学装置保持较好的循环性能。In view of the problems existing in the prior art, the purpose of this application is to provide a negative electrode plate, an electrochemical device and an electronic device. The negative electrode plate can not only increase the energy density of the electrochemical device, but also keep the electrochemical device in good condition. cycle performance.
在第一方面,本申请提供一种负极极片,该负极极片包括集流体和负极活性材料层,负极活性材料层包括第一区域和第二区域,其中第一区域的孔隙率小于第二区域的孔隙率,第一区域的活性材料颗粒Dv50与第二区域的活性材料颗粒Dv50的比值为0.3至0.9。In a first aspect, the present application provides a negative electrode sheet, which includes a current collector and a negative active material layer. The negative active material layer includes a first region and a second region, wherein the porosity of the first region is smaller than that of the second region. The porosity of the region, the ratio of the Dv50 of the active material particles in the first region to the Dv50 of the active material particles in the second region, is 0.3 to 0.9.
本申请中,负极极片包括第一区域和第二区域,上述第一区域包括至少一个由小颗粒组成的致密区,上述第二区域包括至少一个由大颗粒组成的非致密区。第一区域不仅能够提升电化学装置的能量密度,而且第一区域与极片的粘接力强,不易脱模,从而能够有效提升极片稳定性,避免极片变形。第二区域的颗粒度比较大,孔隙率较大,有利于电解液的存储,并提供电解液在极片内部的快速扩散通道,利于电解液快速扩散和保液,与周边的致密区协同工作,减小第一区域的电解液输送路径,提升动力学。In this application, the negative electrode plate includes a first region and a second region. The first region includes at least one dense region composed of small particles, and the above-mentioned second region includes at least one non-dense region composed of large particles. The first area can not only increase the energy density of the electrochemical device, but also has strong adhesion to the pole piece and is difficult to demould, thereby effectively improving the stability of the pole piece and avoiding pole piece deformation. The particle size of the second area is relatively large and the porosity is large, which is conducive to the storage of electrolyte, and provides a rapid diffusion channel for the electrolyte inside the pole piece, which is conducive to the rapid diffusion and retention of electrolyte, and works in conjunction with the surrounding dense areas , reducing the electrolyte transport path in the first area and improving dynamics.
根据本申请的一些实施方式,第一区域的活性材料颗粒的Dv50为5μm至20μm。根据本申请的一些实施方式,第二区域的活性材料颗粒的Dv50为20μm至50μm。第一区 域和第二区域的活性材料颗粒的Dv50满足上述范围,负极活性材料层能够在保证其在电解液中的整体浸润性的同时,维持适当的极片反应活性,减少不合理的粒径分布导致的副反应,并降低生产难度,提高极片生产过程中的良品率。According to some embodiments of the present application, the Dv50 of the active material particles in the first region is 5 μm to 20 μm. According to some embodiments of the present application, the Dv50 of the active material particles in the second region is 20 μm to 50 μm. The Dv50 of the active material particles in the first region and the second region meets the above range. The negative active material layer can maintain appropriate electrode plate reactivity and reduce unreasonable particle size while ensuring its overall wettability in the electrolyte. Side reactions caused by distribution, reduce production difficulty, and improve the yield rate during the pole piece production process.
根据本申请的一些实施方式,第一区域的孔隙率为15%至30%。根据本申请的一些实施方式,第二区域的孔隙率为30%至45%。第一区域的孔隙率和第二区域的孔隙率满足上述范围,负极活性材料层能够在保证电解液浸润性和扩散能力的同时,降低电化学装置的浓差极化,减小内阻,并显著提升极片的能量密度。According to some embodiments of the present application, the first region has a porosity of 15% to 30%. According to some embodiments of the present application, the second region has a porosity of 30% to 45%. The porosity of the first region and the porosity of the second region meet the above range. The negative active material layer can reduce the concentration polarization of the electrochemical device and reduce the internal resistance while ensuring the wettability and diffusion ability of the electrolyte. Significantly improve the energy density of the pole piece.
根据本申请的一些实施方式,负极活性材料层的厚度为50μm至300μm。负极活性材料层的厚度在上述范围内,能够在优化电化学装置能量密度的同时,进一步提升极片在厚度方向上的电解液浸润性和扩散能力。根据本申请的一些实施方式,负极活性材料层的厚度为100μm至250μm。According to some embodiments of the present application, the thickness of the negative active material layer is 50 μm to 300 μm. The thickness of the negative active material layer is within the above range, which can further improve the electrolyte wettability and diffusion ability of the electrode piece in the thickness direction while optimizing the energy density of the electrochemical device. According to some embodiments of the present application, the thickness of the negative active material layer is 100 μm to 250 μm.
根据本申请的一些实施方式,第一区域和/或第二区域的活性材料颗粒为阵列排布或非阵列排布。According to some embodiments of the present application, the active material particles in the first region and/or the second region are arranged in an array or in a non-array arrangement.
根据本申请的一些实施方式,所述第一区域和/或所述第二区域的活性材料颗粒为阵列排布,且活性材料颗粒的长径比为1.1至5。第一区域域和第二区域的活性材料颗粒都是阵列排布,利于锂离子快速嵌入和脱出。According to some embodiments of the present application, the active material particles in the first region and/or the second region are arranged in an array, and the aspect ratio of the active material particles is 1.1 to 5. The active material particles in the first region and the second region are arranged in an array, which is conducive to the rapid insertion and extraction of lithium ions.
根据本申请的一些实施方式,第一区域和/或第二区域的活性材料颗粒沿长径方向与集流体之间的角度为45°至135°。活性材料颗粒在此角度范围内与集流体排布,使得锂离子的扩散路径变短,有利于提升动力学。According to some embodiments of the present application, an angle between the active material particles in the first region and/or the second region and the current collector along the long diameter direction is 45° to 135°. The active material particles are arranged with the current collector within this angle range, which shortens the diffusion path of lithium ions, which is beneficial to improving dynamics.
根据本申请的一些实施方式,沿极片厚度方向,基于所述活性材料层的投影面积,所述第二区域的投影面积占比为5%至50%,在此范围可以提高电解液扩散效率,有利于提升动力学。According to some embodiments of the present application, along the thickness direction of the pole piece, based on the projected area of the active material layer, the projected area of the second region accounts for 5% to 50%. In this range, the electrolyte diffusion efficiency can be improved , which is beneficial to improving dynamics.
根据本申请的一些实施方式,所述第二区域为条形分布或者岛状分布。According to some embodiments of the present application, the second area is distributed in a stripe shape or an island shape.
根据本申请的一些实施方式,所述第二区域沿所述负极极片宽度方向贯通设置。According to some embodiments of the present application, the second region is disposed through the negative electrode plate in the width direction.
根据本申请的一些实施方式,所述负极极片的粘结力为5N/m至15N/m。第二区域的活性材料颗粒粒径较小,比表面积大,与粘结剂的作用力强,第二区域与集流体接触面积越大,粘结力越强,且自身粘结力大;粘结力强可以避免极片在加工和电极组件使用或者滥用发生脱模现象。According to some embodiments of the present application, the bonding force of the negative electrode piece is 5 N/m to 15 N/m. The particle size of the active material particles in the second region is smaller, the specific surface area is larger, and the interaction force with the binder is stronger. The larger the contact area between the second region and the current collector, the stronger the bonding force, and the greater its own bonding force; The strong bonding force can prevent the pole piece from being demolded during processing and use or abuse of the electrode assembly.
根据本申请的一些实施方式,第一区域宽度与第二区域宽度的比值为1至20,第二 区域为条形分布或者岛状分布。根据本申请的一些实施方式,第一区域宽度与第二区域宽度的比值为1至10。本申请中,第一区域宽度和第二区域宽度指的是负极极片表层的第一区域宽度和第二区域宽度。According to some embodiments of the present application, the ratio of the width of the first area to the width of the second area is 1 to 20, and the second area is distributed in a stripe shape or an island shape. According to some embodiments of the present application, the ratio of the first area width to the second area width is 1 to 10. In this application, the first area width and the second area width refer to the first area width and the second area width of the negative electrode plate surface layer.
根据本申请的一些实施方式,第一区域宽度为1mm至50mm。根据本申请的一些实施方式,第二区域为岛状分布且为每个岛的形状为正方形或长方形。According to some embodiments of the present application, the first area width is 1 mm to 50 mm. According to some embodiments of the present application, the second area is distributed in an island shape and the shape of each island is a square or a rectangle.
根据本申请的一些实施方式,第一区域的厚度与第二区域的厚度的比值为1至2。第一区域的厚度与第二区域的厚度的比值在此范围可以提高电解液扩散效率,有利于提升动力学。According to some embodiments of the present application, the ratio of the thickness of the first region to the thickness of the second region is 1 to 2. The ratio of the thickness of the first region to the thickness of the second region within this range can improve the electrolyte diffusion efficiency and is beneficial to improving dynamics.
根据本申请的一些实施方式,在集流体和负极活性材料层之间还设置有底涂层。底涂层的设置可以增加负极活性材料与集流体的粘接力,有效减少负极极片不同区域差异化设计导致的脱模、变形等现象。According to some embodiments of the present application, a primer layer is further provided between the current collector and the negative active material layer. The setting of the undercoat can increase the adhesion between the negative active material and the current collector, and effectively reduce demoulding, deformation and other phenomena caused by the differentiated design of different areas of the negative electrode piece.
根据本申请的一些实施方式,底涂层包括导电材料、粘结剂和分散剂。According to some embodiments of the present application, the base coating includes conductive materials, binders, and dispersants.
根据本申请的一些实施方式,底涂层中的导电材料包括导电碳黑、碳纤维、科琴黑、乙炔黑、碳纳米管和石墨烯中的至少一种。According to some embodiments of the present application, the conductive material in the undercoat layer includes at least one of conductive carbon black, carbon fiber, Ketjen black, acetylene black, carbon nanotubes and graphene.
根据本申请的一些实施方式,粘结剂包括丁苯橡胶。According to some embodiments of the present application, the adhesive includes styrene-butadiene rubber.
根据本申请的一些实施方式,分散剂包括羧甲基纤维素钠。According to some embodiments of the present application, the dispersant includes sodium carboxymethylcellulose.
根据本申请的一些实施方式,第一区域和/或第二区域的活性材料颗粒为非阵列排布,并且底涂层的厚度为0.5μm至1.5μm。根据本申请的另一些实施方式,第一区域和/或第二区域的活性材料颗粒为阵列排布,并且底涂层的厚度为1.5μm至3.0μm,这是因为活性材料颗粒阵列排布以后与集流体的附着能力变差,增加底涂层的厚度可以提升附着力,防止脱模。According to some embodiments of the present application, the active material particles in the first region and/or the second region are arranged in a non-array arrangement, and the thickness of the undercoat layer is 0.5 μm to 1.5 μm. According to other embodiments of the present application, the active material particles in the first region and/or the second region are arranged in an array, and the thickness of the undercoat layer is 1.5 μm to 3.0 μm. This is because after the active material particles are arranged in an array, The adhesion ability to the current collector becomes poor. Increasing the thickness of the primer layer can improve the adhesion and prevent demolding.
在第二方面,本申请提供了一种电化学装置,该电化学装置包括如本申请第一方面所述的负极极片。In a second aspect, the present application provides an electrochemical device, which includes the negative electrode piece as described in the first aspect of the present application.
在第三方面,本申请提供了一种电子装置,包括如本申请第二方面所述的电化学装置。In a third aspect, the present application provides an electronic device, including the electrochemical device according to the second aspect of the present application.
本申请提供的负极极片不仅能够提升电化学装置的能量密度,同时还使电化学装置保持较好的循环性能。The negative electrode sheet provided by this application can not only increase the energy density of the electrochemical device, but also maintain good cycle performance of the electrochemical device.
附图说明Description of drawings
图1是根据本申请的一些实施方式的负极极片的长度方向的剖面示意图,其中,1为 铜集流体,2为底涂层,3为小颗粒致密区,4为大颗粒非致密区。Figure 1 is a schematic cross-sectional view of a negative electrode sheet in the length direction according to some embodiments of the present application, where 1 is a copper current collector, 2 is an undercoat layer, 3 is a small particle dense area, and 4 is a large particle non-dense area.
图2是根据本申请的另一些实施方式的负极极片的长度方向的剖面示意图,其中,1为铜集流体,2为底涂层,3为小颗粒致密区,4为大颗粒非致密区。Figure 2 is a schematic cross-sectional view of the negative electrode sheet in the length direction according to other embodiments of the present application, in which 1 is a copper current collector, 2 is an undercoat layer, 3 is a small particle dense area, and 4 is a large particle non-dense area. .
图3是根据本申请的一些实施方式的负极极片的俯视示意图,其中第二区域为条形分布。FIG. 3 is a schematic top view of a negative electrode plate according to some embodiments of the present application, in which the second area is distributed in a strip shape.
图4是根据本申请的另一些实施方式的负极极片的俯视示意图,其中第二区域为条形分布。FIG. 4 is a schematic top view of a negative electrode sheet according to other embodiments of the present application, in which the second area is distributed in a strip shape.
图5是根据本申请的另一些实施方式的负极极片的俯视示意图,其中第二区域为岛状分布。FIG. 5 is a schematic top view of a negative electrode piece according to other embodiments of the present application, in which the second area is distributed in an island shape.
具体实施方式Detailed ways
下面结合具体实施方式,进一步阐述本申请。应理解,这些具体实施方式仅用于说明本申请。The present application will be further elaborated below in conjunction with specific embodiments. It should be understood that these specific embodiments are only used to illustrate the present application.
为使本申请的目的、技术方案和优点更加清楚,下面将结合附图和实施例对本申请的技术方案进行清楚、完整地描述,显然,所描述的实施例是本申请一部分实施例,而不是全部的实施例。在此所描述的有关实施例为说明性质的且用于提供对本申请的基本理解。本申请的实施例不应该被解释为对本申请的限制。为了简明,本文仅具体地公开了一些数值范围。然而,任意下限可以与任何上限组合形成未明确记载的范围;以及任意下限可以与其它下限组合形成未明确记载的范围,同样任意上限可以与任意其它上限组合形成未明确记载的范围。此外,每个单独公开的点或单个数值自身可以作为下限或上限与任意其它点或单个数值组合或与其它下限或上限组合形成未明确记载的范围。In order to make the purpose, technical solutions and advantages of the present application clearer, the technical solutions of the present application will be clearly and completely described below in conjunction with the drawings and embodiments. Obviously, the described embodiments are part of the embodiments of the present application, not All examples. The related embodiments described herein are illustrative in nature and are intended to provide a basic understanding of the present application. The embodiments of the present application should not be construed as limitations of the present application. For the sake of simplicity, only certain numerical ranges are specifically disclosed herein. However, any lower limit can be combined with any upper limit to form an unexpressed range; and any lower limit can be combined with other lower limits to form an unexpressed range, and likewise any upper limit can be combined with any other upper limit to form an unexpressed range. Furthermore, each individually disclosed point or single value may itself serve as a lower or upper limit in combination with any other point or single value or with other lower or upper limits to form a range not expressly recited.
除非另有说明,本申请中使用的术语具有本领域技术人员通常所理解的公知含义。除非另有说明,本申请中提到的各参数的数值可以用本领域常用的各种测量方法进行测量(例如,可以按照在本申请的实施例中给出的方法进行测试)。Unless otherwise stated, terms used in this application have their commonly understood meanings as generally understood by those skilled in the art. Unless otherwise stated, the values of each parameter mentioned in this application can be measured using various measurement methods commonly used in the art (for example, they can be tested according to the methods given in the examples of this application).
术语“中的至少一者”、“中的至少一个”、“中的至少一种”或其他相似术语所连接的项目的列表可意味着所列项目的任何组合。例如,如果列出项目A及B,那么短语“A及B中的至少一者”意味着仅A;仅B;或A及B。在另一实例中,如果列出项目A、B及C,那么短语“A、B及C中的至少一者”意味着仅A;或仅B;仅C;A及B(排除C);A及C(排除B);B及C(排除A);或A、B及C的全部。项目A可包 含单个组分或多个组分。项目B可包含单个组分或多个组分。项目C可包含单个组分或多个组分。A list of items connected by the terms "at least one of," "at least one of," "at least one of," or other similar terms may mean any combination of the listed items. For example, if items A and B are listed, the phrase "at least one of A and B" means only A; only B; or A and B. In another example, if the items A, B, and C are listed, then the phrase "at least one of A, B, and C" means only A; or only B; only C; A and B (excluding C); A and C (excluding B); B and C (excluding A); or all of A, B and C. Item A may contain a single component or multiple components. Item B may contain a single component or multiple components. Item C may contain a single component or multiple components.
负极极片Negative pole piece
在第一方面,本申请提供一种负极极片,该负极极片包括集流体和负极活性材料层,负极活性材料层包括第一区域和第二区域,其中第一区域的孔隙率小于第二区域的孔隙率,第一区域的活性材料颗粒Dv50与第二区域的活性材料颗粒Dv50的比值为0.3至0.9。In a first aspect, the present application provides a negative electrode sheet, which includes a current collector and a negative active material layer. The negative active material layer includes a first region and a second region, wherein the porosity of the first region is smaller than that of the second region. The porosity of the region, the ratio of the Dv50 of the active material particles in the first region to the Dv50 of the active material particles in the second region, is 0.3 to 0.9.
本申请中,负极极片具有两个区域,小颗粒组成的第一区域和大颗粒组成的第二区域,。第一区域主要对电化学装置的能量密度有贡献;第二区域的颗粒度比较大,孔隙率较大,有利于储存电解液和提供电解液扩散到极片内部的快速通道,利于电解液快速扩散和保液,同时为周边的第一区域带来电解液供应,减小第一区域的电解液输送路径,提升动力学。In this application, the negative electrode piece has two regions, a first region composed of small particles and a second region composed of large particles. The first area mainly contributes to the energy density of the electrochemical device; the second area has a relatively large particle size and a large porosity, which is conducive to storing electrolyte and providing a fast channel for the electrolyte to diffuse into the interior of the pole piece, which is conducive to the rapid development of electrolyte. Diffusion and liquid retention simultaneously bring electrolyte supply to the surrounding first area, reduce the electrolyte transport path in the first area, and improve dynamics.
根据本申请的一些实施方式,第一区域的活性材料颗粒的Dv50为5μm至20μm。在一些实施例中,第一区域的活性材料颗粒的Dv50为5μm、8μm、12μm、15μm、18μm、20μm或它们中任意二者组成的范围。根据本申请的一些实施方式,第二区域的活性材料颗粒的Dv50为20μm至50μm。在一些实施例中,第二区域的活性材料颗粒的Dv50为20μm、25μm、28μm、32μm、35μm、42μm、45μm、50μm或它们中任意二者组成的范围。第一区域和第二区域的活性材料颗粒的Dv50满足上述范围,负极活性材料层能够在保证其在电解液中的整体浸润性的同时,维持适当的极片反应活性,减少不合理的粒径分布导致的副反应,并降低生产难度,提高极片生产过程中的良品率。According to some embodiments of the present application, the Dv50 of the active material particles in the first region is 5 μm to 20 μm. In some embodiments, the Dv50 of the active material particles in the first region is in a range of 5 μm, 8 μm, 12 μm, 15 μm, 18 μm, 20 μm, or any two thereof. According to some embodiments of the present application, the Dv50 of the active material particles in the second region is 20 μm to 50 μm. In some embodiments, the Dv50 of the active material particles in the second region is a range of 20 μm, 25 μm, 28 μm, 32 μm, 35 μm, 42 μm, 45 μm, 50 μm, or any two thereof. The Dv50 of the active material particles in the first region and the second region meets the above range. The negative active material layer can maintain appropriate electrode plate reactivity and reduce unreasonable particle size while ensuring its overall wettability in the electrolyte. Side reactions caused by distribution, reduce production difficulty, and improve the yield rate during the pole piece production process.
根据本申请的一些实施方式,第一区域的孔隙率为15%至30%。在一些实施例中,第一区域的孔隙率为15%、18%、20%、25%、28%、30%或它们中任意二者组成的范围。根据本申请的一些实施方式,第二区域的孔隙率为30%至45%。在一些实施例中,第二区域的孔隙率为30%、35%、40%、45%或它们中任意二者组成的范围。第一区域的孔隙率和第二区域的孔隙率满足上述范围,负极活性材料层能够在保证第一区域的电解液浸润性和扩散能力的同时,显著提升极片的能量密度。According to some embodiments of the present application, the first region has a porosity of 15% to 30%. In some embodiments, the porosity of the first region ranges from 15%, 18%, 20%, 25%, 28%, 30%, or any two thereof. According to some embodiments of the present application, the second region has a porosity of 30% to 45%. In some embodiments, the porosity of the second region ranges from 30%, 35%, 40%, 45%, or any two thereof. The porosity of the first region and the porosity of the second region meet the above range. The negative active material layer can significantly increase the energy density of the pole piece while ensuring the electrolyte wettability and diffusion ability of the first region.
根据本申请的一些实施方式,负极活性材料层的厚度为50μm至300μm。在一些实施例中,负极活性材料层的厚度为50μm、60μm、70μm、80μm、90μm、100μm、120μm、150μm、180μm、200μm、220μm、240μm、260μm、280μm、300μm或它们中任意二者组成的范围。负极活性材料层的厚度在上述范围内,能够保证电解液浸润性和扩散能力的同时,显著提升极片的能量密度。根据本申请的一些实施方式,负极活性材料层的厚度为 100μm至250μm。According to some embodiments of the present application, the thickness of the negative active material layer is 50 μm to 300 μm. In some embodiments, the thickness of the negative active material layer is 50 μm, 60 μm, 70 μm, 80 μm, 90 μm, 100 μm, 120 μm, 150 μm, 180 μm, 200 μm, 220 μm, 240 μm, 260 μm, 280 μm, 300 μm, or any two thereof. scope. The thickness of the negative active material layer is within the above range, which can ensure the wettability and diffusion ability of the electrolyte and significantly increase the energy density of the electrode piece. According to some embodiments of the present application, the thickness of the negative active material layer is 100 μm to 250 μm.
根据本申请的一些实施方式,第一区域和/或第二区域的活性材料颗粒为阵列排布或非阵列排布。根据本申请的一些实施方式,所述第一区域和/或所述第二区域的活性材料颗粒为阵列排布,且活性材料颗粒的长径比为1.1至5。第一区域域和第二区域的活性材料颗粒都是阵列排布,利于锂离子快速嵌入和脱出。根据本申请的一些实施方式,活性材料颗粒的长径比为1.5至5。根据本申请的一些实施方式,活性材料颗粒的长径比为2至5。According to some embodiments of the present application, the active material particles in the first region and/or the second region are arranged in an array or in a non-array arrangement. According to some embodiments of the present application, the active material particles in the first region and/or the second region are arranged in an array, and the aspect ratio of the active material particles is 1.1 to 5. The active material particles in the first region and the second region are arranged in an array, which is conducive to the rapid insertion and extraction of lithium ions. According to some embodiments of the present application, the active material particles have an aspect ratio of 1.5 to 5. According to some embodiments of the present application, the active material particles have an aspect ratio of 2 to 5.
根据本申请的一些实施方式,第一区域和/或第二区域的活性材料颗粒沿长径方向与集流体之间的角度为45°至135°。在一些实施例中,第一区域的活性材料颗粒沿长径方向与集流体之间的角度为45°至135°,例如45°、50°、55°、60°、65°、70°、75°、80°、85°、90°、95°、100°、105°、110°、115°、120°、125°、130°、135°或它们中任意二者组成的范围。在一些实施例中,第二区域的活性材料颗粒沿长径方向与集流体之间的角度为45°至135°,例如45°、50°、55°、60°、65°、70°、75°、80°、85°、90°、95°、100°、105°、110°、115°、120°、125°、130°、135°或它们中任意二者组成的范围。活性材料颗粒在此角度范围内与集流体排布,使得锂离子的扩散路径变短,有利于提升动力学。According to some embodiments of the present application, an angle between the active material particles in the first region and/or the second region and the current collector along the long diameter direction is 45° to 135°. In some embodiments, the angle between the active material particles in the first region and the current collector along the long diameter direction is 45° to 135°, such as 45°, 50°, 55°, 60°, 65°, 70°, 75°, 80°, 85°, 90°, 95°, 100°, 105°, 110°, 115°, 120°, 125°, 130°, 135° or a range consisting of any two of them. In some embodiments, the angle between the active material particles in the second region and the current collector along the long diameter direction is 45° to 135°, such as 45°, 50°, 55°, 60°, 65°, 70°, 75°, 80°, 85°, 90°, 95°, 100°, 105°, 110°, 115°, 120°, 125°, 130°, 135° or a range consisting of any two of them. The active material particles are arranged with the current collector within this angle range, which shortens the diffusion path of lithium ions, which is beneficial to improving dynamics.
根据本申请的一些实施方式,沿极片厚度方向,基于所述活性材料层的投影面积,所述第二区域的投影面积占比为5%至50%,在此范围可以提高电解液扩散效率,有利于提升动力学。在一些实施例中,沿极片厚度方向,基于所述活性材料层的投影面积,所述第二区域的投影面积占比为5%、10%、15%、20%、25%、30%、35%、40%、45%、50%或它们中任意二者组成的范围。在一些实施方式中,沿极片厚度方向,基于所述活性材料层的投影面积,所述第二区域的投影面积占比为15%至30%。According to some embodiments of the present application, along the thickness direction of the pole piece, based on the projected area of the active material layer, the projected area of the second region accounts for 5% to 50%. In this range, the electrolyte diffusion efficiency can be improved , which is beneficial to improving dynamics. In some embodiments, along the thickness direction of the pole piece, based on the projected area of the active material layer, the projected area ratio of the second region is 5%, 10%, 15%, 20%, 25%, 30% , 35%, 40%, 45%, 50% or a range consisting of any two of them. In some embodiments, along the thickness direction of the pole piece, based on the projected area of the active material layer, the projected area of the second region accounts for 15% to 30%.
根据本申请的一些实施方式,第二区域为条形分布或者岛状分布。According to some embodiments of the present application, the second area is distributed in a strip shape or in an island shape.
根据本申请的一些实施方式,第二区域沿所述负极极片宽度方向贯通设置。According to some embodiments of the present application, the second region is disposed through the negative electrode plate in the width direction.
根据本申请的一些实施方式,负极极片的粘结力为5N/m至15N/m。在一些实施例中,负极极片的粘结力为5N/m、6N/m、7N/m、8N/m、9N/m、10N/m、11N/m、12N/m、13N/m、14N/m、15N/m或它们中任意二者组成的范围。第二区域的活性材料颗粒粒径较小,比表面积大,与粘结剂的作用力强,第二区域与集流体接触面积越大,粘结力越强,且自身粘结力大;粘结力强可以避免极片在加工和电极组件使用或者滥用发生脱模现象。According to some embodiments of the present application, the bonding force of the negative electrode piece is 5 N/m to 15 N/m. In some embodiments, the bonding force of the negative electrode piece is 5N/m, 6N/m, 7N/m, 8N/m, 9N/m, 10N/m, 11N/m, 12N/m, 13N/m, 14N/m, 15N/m or a range consisting of any two of them. The particle size of the active material particles in the second region is smaller, the specific surface area is larger, and the interaction force with the binder is stronger. The larger the contact area between the second region and the current collector, the stronger the bonding force, and the greater its own bonding force; The strong bonding force can prevent the pole piece from being demolded during processing and use or abuse of the electrode assembly.
根据本申请的一些实施方式,第一区域宽度与第二区域宽度的比值为1至20,第二区域为条形分布或者岛状分布。在一些实施例中,第一区域宽度与第二区域宽度的比值为1、3、5、7、10、12、15、18、20或它们中任意二者组成的范围。根据本申请的一些实施方式,第一区域宽度与第二区域宽度的比值为1至10。本申请中,第一区域宽度和第二区域宽度指的是负极极片表层的第一区域宽度和第二区域宽度。According to some embodiments of the present application, the ratio of the width of the first area to the width of the second area is 1 to 20, and the second area is distributed in a stripe shape or an island shape. In some embodiments, the ratio of the width of the first region to the width of the second region is a range of 1, 3, 5, 7, 10, 12, 15, 18, 20, or any two of them. According to some embodiments of the present application, the ratio of the first area width to the second area width is 1 to 10. In this application, the first area width and the second area width refer to the first area width and the second area width of the negative electrode plate surface layer.
根据本申请的一些实施方式,第一区域的宽度为1mm至50mm,例如1mm、5mm、10mm、15mm、20mm、25mm、30mm、35mm、40mm、45mm、50mm或它们中任意二者组成的范围。According to some embodiments of the present application, the width of the first area is 1 mm to 50 mm, such as a range of 1 mm, 5 mm, 10 mm, 15 mm, 20 mm, 25 mm, 30 mm, 35 mm, 40 mm, 45 mm, 50 mm or any two of them.
根据本申请的一些实施方式,第二区域为岛状分布且为每个岛的形状为正方形或长方形。According to some embodiments of the present application, the second area is distributed in an island shape and the shape of each island is a square or a rectangle.
根据本申请的一些实施方式,第一区域的厚度与第二区域的厚度的比值为1至2。在一些实施例中,第一区域的厚度与第二区域的厚度的比值为1、1.2、1.4、1.6、1.8、2或它们中任意二者组成的范围。第一区域的厚度与第二区域的厚度的比值在此范围可以提高电解液扩散效率,有利于提升动力学。According to some embodiments of the present application, the ratio of the thickness of the first region to the thickness of the second region is 1 to 2. In some embodiments, the ratio of the thickness of the first region to the thickness of the second region is a range consisting of 1, 1.2, 1.4, 1.6, 1.8, 2, or any two of them. The ratio of the thickness of the first region to the thickness of the second region within this range can improve the electrolyte diffusion efficiency and is beneficial to improving dynamics.
根据本申请的一些实施方式,在集流体和负极活性材料层之间还设置有底涂层。底涂层的设置可以增加负极活性材料与集流体的粘接力,有效减少负极极片不同区域差异化设计导致的脱模、变形等现象。According to some embodiments of the present application, a primer layer is further provided between the current collector and the negative active material layer. The setting of the undercoat can increase the adhesion between the negative active material and the current collector, and effectively reduce demoulding, deformation and other phenomena caused by the differentiated design of different areas of the negative electrode piece.
根据本申请的一些实施方式,底涂层中的导电材料包括导电碳黑、碳纤维、科琴黑、乙炔黑、碳纳米管和石墨烯中的至少一种。According to some embodiments of the present application, the conductive material in the undercoat layer includes at least one of conductive carbon black, carbon fiber, Ketjen black, acetylene black, carbon nanotubes and graphene.
根据本申请的一些实施方式,粘结剂包括丁苯橡胶。According to some embodiments of the present application, the adhesive includes styrene-butadiene rubber.
根据本申请的一些实施方式,分散剂包括羧甲基纤维素钠。According to some embodiments of the present application, the dispersant includes sodium carboxymethylcellulose.
根据本申请的一些实施方式,第一区域和/或第二区域的活性材料颗粒为非阵列排布,并且底涂层的厚度为0.5μm至1.5μm。根据本申请的另一些实施方式,第一区域和/或第二区域的活性材料颗粒为阵列排布,并且底涂层的厚度为1.5μm至3.0μm,这是因为活性材料颗粒阵列排布以后与集流体的附着能力变差,增加底涂层的厚度可以提升附着力,防止脱模。According to some embodiments of the present application, the active material particles in the first region and/or the second region are arranged in a non-array arrangement, and the thickness of the undercoat layer is 0.5 μm to 1.5 μm. According to other embodiments of the present application, the active material particles in the first region and/or the second region are arranged in an array, and the thickness of the undercoat layer is 1.5 μm to 3.0 μm. This is because after the active material particles are arranged in an array, The adhesion ability to the current collector becomes poor. Increasing the thickness of the primer layer can improve the adhesion and prevent demolding.
根据本申请的一些实施方式,负极活性材料层中的活性材料为石墨。本申请中,负极还包括集流体,集流体可以包括:铜箔、镍箔、不锈钢箔、钛箔、泡沫镍、泡沫铜、覆有导电根据本申请的一些实施方式,负极活性材料层金属的聚合物基底或其任意组合。According to some embodiments of the present application, the active material in the negative active material layer is graphite. In this application, the negative electrode also includes a current collector, which may include: copper foil, nickel foil, stainless steel foil, titanium foil, nickel foam, copper foam, coated with conductive material. According to some embodiments of the present application, the negative active material layer is metal. Polymer base or any combination thereof.
负极活性材料层还可以包括导电剂和/或粘结剂。在一些实施例中,导电剂包括导电炭黑、乙炔黑、碳纳米管、科琴黑、导电石墨或石墨烯中的至少一种。在一些实施例中,导电剂占活性物质层的质量百分含量为0.5%至10%。在一些实施例中,粘结剂包括聚偏氟乙烯、偏氟乙烯-六氟丙烯的共聚物、聚酰胺、聚丙烯腈、聚丙烯酯、聚丙烯酸、聚丙烯酸盐、羧甲基纤维素钠、聚乙烯吡咯烷酮、聚乙烯醚、聚甲基丙烯酸甲酯、聚四氟乙烯、聚六氟丙烯或丁苯橡胶中的至少一种。在一些实施例中,粘结剂占活性物质层的质量百分含量为0.5%至10%。The negative active material layer may further include a conductive agent and/or a binder. In some embodiments, the conductive agent includes at least one of conductive carbon black, acetylene black, carbon nanotubes, Ketjen black, conductive graphite, or graphene. In some embodiments, the conductive agent accounts for 0.5% to 10% by mass of the active material layer. In some embodiments, the binder includes polyvinylidene fluoride, vinylidene fluoride-hexafluoropropylene copolymer, polyamide, polyacrylonitrile, polyacrylic ester, polyacrylic acid, polyacrylate, sodium carboxymethylcellulose , at least one of polyvinylpyrrolidone, polyvinyl ether, polymethylmethacrylate, polytetrafluoroethylene, polyhexafluoropropylene or styrene-butadiene rubber. In some embodiments, the binder accounts for 0.5% to 10% by mass of the active material layer.
电化学装置electrochemical device
本申请的电化学装置包括发生电化学反应的任何装置,它的具体实例包括所有种类的一次电池、二次电池。特别地,该电化学装置是锂二次电池,包括锂金属二次电池、锂离子二次电池、锂聚合物二次电池或锂离子聚合物二次电池。在一些实施例中,本申请的电化学装置包括正极、负极、隔离膜和电解液。The electrochemical device of the present application includes any device that generates electrochemical reactions, and specific examples thereof include all types of primary batteries and secondary batteries. In particular, the electrochemical device is a lithium secondary battery, including a lithium metal secondary battery, a lithium ion secondary battery, a lithium polymer secondary battery or a lithium ion polymer secondary battery. In some embodiments, the electrochemical device of the present application includes a positive electrode, a negative electrode, a separator and an electrolyte.
1、负极1. Negative pole
本申请的电化学装置中的负极包括第一方面的负极极片。The negative electrode in the electrochemical device of the present application includes the negative electrode piece of the first aspect.
2、正极2. Positive electrode
可用于本申请的实施例中正极的材料、构成和其制造方法包括任何现有技术中公开的技术。The materials, composition and manufacturing methods of the positive electrode that can be used in the embodiments of the present application include any technology disclosed in the prior art.
根据本申请的一些实施方式,正极包括集流体和位于该集流体上的正极活性材料层。根据本申请的一些实施方式,正极活性材料包括,但不限于:钴酸锂(LiCoO 2)、镍钴锰酸锂(NCM)、镍钴铝酸锂、磷酸亚铁锂(LiFePO 4)或锰酸锂(LiMn 2O 4)。 According to some embodiments of the present application, the positive electrode includes a current collector and a positive active material layer located on the current collector. According to some embodiments of the present application, the cathode active material includes, but is not limited to: lithium cobalt oxide (LiCoO 2 ), lithium nickel cobalt manganate (NCM), lithium nickel cobalt aluminate, lithium iron phosphate (LiFePO 4 ) or manganese Lithium oxide (LiMn 2 O 4 ).
根据本申请的一些实施方式,正极活性材料层还包括粘合剂,并且可选地包括导电材料。粘合剂提高正极活性材料颗粒彼此间的结合,并且还提高正极活性材料与集流体的结合。在一些实施方式中,粘结剂包括:聚乙烯醇、羟丙基纤维素、二乙酰基纤维素、聚氯乙烯、羧化的聚氯乙烯、聚氟乙烯、含亚乙基氧的聚合物、聚乙烯吡咯烷酮、聚氨酯、聚四氟乙烯、聚偏1,1-二氟乙烯、聚乙烯、聚丙烯、丁苯橡胶、丙烯酸(酯)化的丁苯橡胶、环氧树脂或尼龙等。According to some embodiments of the present application, the positive active material layer further includes a binder and optionally a conductive material. The binder improves the binding of the positive active material particles to each other and also improves the binding of the positive active material to the current collector. In some embodiments, the binder includes: polyvinyl alcohol, hydroxypropyl cellulose, diacetyl cellulose, polyvinyl chloride, carboxylated polyvinyl chloride, polyvinyl fluoride, ethylene oxide-containing polymers , polyvinylpyrrolidone, polyurethane, polytetrafluoroethylene, polyvinylidene fluoride, polyethylene, polypropylene, styrene-butadiene rubber, acrylic (ester) styrene-butadiene rubber, epoxy resin or nylon, etc.
根据本申请的一些实施方式,导电材料包括,但不限于:基于碳的材料、基于金属的材料、导电聚合物和它们的混合物。在一些实施例中,基于碳的材料选自碳黑、乙炔黑、 科琴黑、碳纤维、碳纳米管或其任意组合。在一些实施例中,基于金属的材料选自金属粉、金属纤维、铜、镍、铝或银。在一些实施例中,导电聚合物为聚亚苯基衍生物。According to some embodiments of the present application, conductive materials include, but are not limited to: carbon-based materials, metal-based materials, conductive polymers, and mixtures thereof. In some embodiments, the carbon-based material is selected from carbon black, acetylene black, Ketjen black, carbon fiber, carbon nanotubes, or any combination thereof. In some embodiments, the metal-based material is selected from metal powders, metal fibers, copper, nickel, aluminum, or silver. In some embodiments, the conductive polymer is a polyphenylene derivative.
根据本申请的一些实施方式,集流体可以包括,但不限于:铝。According to some embodiments of the present application, the current collector may include, but is not limited to: aluminum.
3、电解液3. Electrolyte
可用于本申请实施例的电解液可以为现有技术中已知的电解液。The electrolyte solution that can be used in the embodiments of the present application may be an electrolyte solution known in the art.
在一些实施例中,电解液包括有机溶剂、锂盐和添加剂。根据本申请的电解液的有机溶剂可为现有技术中已知的任何可作为电解液的溶剂的有机溶剂。根据本申请的电解液中使用的电解质没有限制,其可为现有技术中已知的任何电解质。根据本申请的电解液的添加剂可为现有技术中已知的任何可作为电解液添加剂的添加剂。In some embodiments, the electrolyte includes an organic solvent, a lithium salt, and additives. The organic solvent of the electrolyte solution according to the present application may be any organic solvent known in the prior art that can be used as a solvent for the electrolyte solution. The electrolyte used in the electrolyte solution according to the present application is not limited, and it can be any electrolyte known in the prior art. The additives of the electrolyte according to the present application may be any additives known in the art that can be used as electrolyte additives.
在一些实施例中,有机溶剂包括,但不限于:碳酸乙烯酯(EC)、碳酸丙烯酯(PC)、碳酸二乙酯(DEC)、碳酸甲乙酯(EMC)、碳酸二甲酯(DMC)、碳酸亚丙酯或丙酸乙酯。In some embodiments, organic solvents include, but are not limited to: ethylene carbonate (EC), propylene carbonate (PC), diethyl carbonate (DEC), ethyl methyl carbonate (EMC), dimethyl carbonate (DMC) ), propylene carbonate or ethyl propionate.
在一些实施例中,锂盐包括,但不限于:六氟磷酸锂LiPF 6、四氟硼酸锂LiBF 4、二氟磷酸锂LiPO 2F 2、双三氟甲烷磺酰亚胺锂LiN(CF 3SO 2) 2(缩写为LiTFSI)、双(氟磺酰)亚胺锂Li(N(SO 2F) 2)(缩写为LiFSI)、双草酸硼酸锂LiB(C 2O 4) 2(缩写为LiBOB)或二氟草酸硼酸锂LiBF 2(C 2O 4)(缩写为LiDFOB)。 In some embodiments, lithium salts include, but are not limited to: lithium hexafluorophosphate LiPF 6 , lithium tetrafluoroborate LiBF 4 , lithium difluorophosphate LiPO 2 F 2 , lithium bistrifluoromethanesulfonimide LiN (CF 3 SO 2 ) 2 (abbreviated as LiTFSI), lithium bis(fluorosulfonyl)imide Li(N(SO 2 F) 2 ) (abbreviated as LiFSI), lithium bisoxalatoborate LiB(C 2 O 4 ) 2 (abbreviated as LiBOB) or Lithium difluorooxalate borate LiBF 2 (C 2 O 4 ) (abbreviated as LiDFOB).
在一些实施例中,电解液中锂盐的浓度为:0.5mol/L至3mol/L、0.5mol/L至2mol/L或0.8mol/L至1.5mol/L。In some embodiments, the concentration of lithium salt in the electrolyte is: 0.5 mol/L to 3 mol/L, 0.5 mol/L to 2 mol/L, or 0.8 mol/L to 1.5 mol/L.
4、隔离膜4. Isolation film
本申请的电化学装置中使用的隔离膜的材料和形状没有特别限制,其可为任何现有技术中公开的技术。在一些实施例中,隔离膜包括由对本申请的电解液稳定的材料形成的聚合物或无机物等。The material and shape of the isolation membrane used in the electrochemical device of the present application are not particularly limited, and it can be any technology disclosed in the prior art. In some embodiments, the isolation membrane includes polymers or inorganic substances formed of materials that are stable to the electrolyte of the present application.
例如隔离膜可包括基材层和表面处理层。基材层为具有多孔结构的无纺布、膜或复合膜,基材层的材料选自聚乙烯、聚丙烯、聚对苯二甲酸乙二醇酯和聚酰亚胺中的至少一种。具体的,可选用聚丙烯多孔膜、聚乙烯多孔膜、聚丙烯无纺布、聚乙烯无纺布或聚丙烯-聚乙烯-聚丙烯多孔复合膜。For example, the isolation film may include a base material layer and a surface treatment layer. The base material layer is a non-woven fabric, film or composite film with a porous structure. The base material layer is made of at least one material selected from the group consisting of polyethylene, polypropylene, polyethylene terephthalate and polyimide. Specifically, polypropylene porous membrane, polyethylene porous membrane, polypropylene non-woven fabric, polyethylene non-woven fabric or polypropylene-polyethylene-polypropylene porous composite membrane can be used.
基材层的至少一个表面上设置有表面处理层,表面处理层可以是聚合物层或无机物层,也可以是混合聚合物与无机物所形成的层。A surface treatment layer is provided on at least one surface of the base layer. The surface treatment layer may be a polymer layer or an inorganic layer, or may be a layer formed by mixing a polymer and an inorganic layer.
无机物层包括无机颗粒和粘结剂,无机颗粒选自氧化铝、氧化硅、氧化镁、氧化钛、二氧化铪、氧化锡、二氧化铈、氧化镍、氧化锌、氧化钙、氧化锆、氧化钇、碳化硅、勃 姆石、氢氧化铝、氢氧化镁、氢氧化钙和硫酸钡中的至少一种。粘结剂选自聚偏氟乙烯、偏氟乙烯-六氟丙烯的共聚物、聚酰胺、聚丙烯腈、聚丙烯酸酯、聚丙烯酸、聚丙烯酸盐、聚乙烯呲咯烷酮、聚乙烯烷氧、聚甲基丙烯酸甲酯、聚四氟乙烯和聚六氟丙烯中的至少一种。The inorganic layer includes inorganic particles and a binder. The inorganic particles are selected from aluminum oxide, silicon oxide, magnesium oxide, titanium oxide, hafnium dioxide, tin oxide, ceria, nickel oxide, zinc oxide, calcium oxide, zirconium oxide, At least one of yttrium oxide, silicon carbide, boehmite, aluminum hydroxide, magnesium hydroxide, calcium hydroxide and barium sulfate. The binder is selected from polyvinylidene fluoride, vinylidene fluoride-hexafluoropropylene copolymer, polyamide, polyacrylonitrile, polyacrylate, polyacrylic acid, polyacrylate, polyvinylpyrrolidone, polyethylene alkoxy , at least one of polymethylmethacrylate, polytetrafluoroethylene and polyhexafluoropropylene.
聚合物层中包含聚合物,聚合物的材料选自聚酰胺、聚丙烯腈、丙烯酸酯聚合物、聚丙烯酸、聚丙烯酸盐、聚乙烯呲咯烷酮、聚乙烯烷氧、聚偏氟乙烯、聚(偏氟乙烯-六氟丙烯)中的至少一种。The polymer layer contains a polymer, and the material of the polymer is selected from polyamide, polyacrylonitrile, acrylate polymer, polyacrylic acid, polyacrylate, polyvinylpyrrolidone, polyethylene alkoxy, polyvinylidene fluoride, At least one of poly(vinylidene fluoride-hexafluoropropylene).
电子装置electronic device
本申请进一步提供了一种电子装置,其包括本申请第二方面的电化学装置。The present application further provides an electronic device, which includes the electrochemical device of the second aspect of the present application.
本申请的电子设备或装置没有特别限定。在一些实施例中,本申请的电子设备包括但不限于,笔记本电脑、笔输入型计算机、移动电脑、电子书播放器、便携式电话、便携式传真机、便携式复印机、便携式打印机、头戴式立体声耳机、录像机、液晶电视、手提式清洁器、便携CD机、迷你光盘、收发机、电子记事本、计算器、存储卡、便携式录音机、收音机、备用电源、无人机、电机、汽车、摩托车、助力自行车、自行车、照明器具、玩具、游戏机、钟表、电动工具、闪光灯、照相机、家庭用大型蓄电池和锂离子电容器等。The electronic equipment or device of the present application is not particularly limited. In some embodiments, electronic devices of the present application include, but are not limited to, notebook computers, pen-input computers, mobile computers, e-book players, portable telephones, portable fax machines, portable copiers, portable printers, and stereo headsets. , VCR, LCD TV, portable cleaner, portable CD player, mini disc, transceiver, electronic notepad, calculator, memory card, portable recorder, radio, backup power supply, drone, motor, car, motorcycle, Power bicycles, bicycles, lighting equipment, toys, game consoles, clocks, power tools, flashlights, cameras, large household batteries and lithium-ion capacitors, etc.
下面结合实施例,进一步阐述本申请。应理解,这些实施例仅用于说明本申请而不用于限制本申请的范围。The present application will be further described below in conjunction with examples. It should be understood that these examples are only used to illustrate the present application and are not intended to limit the scope of the present application.
实施例和对比例Examples and Comparative Examples
测试方法Test Methods
直流内阻测试:以0.2C将锂离子电池充至50%SOC,静置30min,然后以0.1C放电1s,再以1C放电1s,计算两次放点末端的电压差与电流差的比值,得到直流内阻。DC internal resistance test: Charge the lithium-ion battery to 50% SOC at 0.2C, let it sit for 30 minutes, then discharge it at 0.1C for 1s, and then discharge it at 1C for 1s. Calculate the ratio of the voltage difference to the current difference at the end of the two discharge points. Get the DC internal resistance.
倍率放电测试:以0.2C恒压充电至4.4V,再恒压充电至0.02C,静置30min后,0.2C放电至3.0V,得到锂离子电池实际容量,然后以相同方式满充,静置30min后,3C放电至3.0V,得到锂离子电池容量,并与实际容量对比,计算容量保持率。Rate discharge test: charge to 4.4V at a constant voltage of 0.2C, then charge to a constant voltage of 0.02C, let it sit for 30 minutes, discharge it to 3.0V at 0.2C to get the actual capacity of the lithium-ion battery, and then fully charge it in the same way and let it stand. After 30 minutes, 3C was discharged to 3.0V to obtain the lithium-ion battery capacity, and compared with the actual capacity, the capacity retention rate was calculated.
极片粘结力测量方法Pole piece bonding force measurement method
将极片裁成20mm×10cm大小的矩形小片,采用20mm宽的双面胶黏在洁净的宽度为20mm的钢板上,手动剥离20mm后,采用拉力机分别固定钢板和极片剥离部分,使剥离面与试验机力线保持一致,测试极片180°的剥离力,拉力机拉伸速度为50mm/min,得到的剥离力曲线,取平稳段的均值作为剥离力F 0,则被测试负极片的粘结力为:F=F 0/0.02 =50F 0Cut the pole piece into a rectangular piece of size 20mm×10cm. Use a 20mm wide double-sided tape to stick it on a clean steel plate with a width of 20mm. After manually peeling off 20mm, use a tensile machine to fix the peeled part of the steel plate and pole piece respectively to make the peeling easier. Keep the surface consistent with the force line of the testing machine, test the peeling force of the electrode piece at 180°, and the tensile machine stretching speed is 50mm/min. From the peeling force curve obtained, take the average value of the plateau section as the peeling force F 0 , then the negative electrode piece is tested The bonding force is: F=F 0 /0.02 =50F 0 .
实施例1-1Example 1-1
正极的制备:采用12μm铝箔作为正极的集流体,将正极活性材料钴酸锂、导电剂导电炭黑、聚偏氟乙烯按重量比97.5∶1.5∶1.0的比例混合,采用静电喷涂将粉料喷涂到铝集流体上,然后经过冷压和裁切后得到所需要厚度和尺寸的正极极片。Preparation of the positive electrode: Use 12 μm aluminum foil as the current collector of the positive electrode, mix the positive active material lithium cobalt oxide, conductive agent conductive carbon black, and polyvinylidene fluoride in a weight ratio of 97.5:1.5:1.0, and use electrostatic spraying to spray the powder onto the aluminum current collector, and then undergo cold pressing and cutting to obtain the positive electrode piece with the required thickness and size.
底涂层:将导电碳∶PVDF=97∶3的比例在水中混合,通过转移涂布涂敷在6μm Cu集流体上,底涂层厚度为1μm。Undercoating: Mix conductive carbon:PVDF=97:3 in water and apply it on the 6μm Cu current collector by transfer coating. The thickness of the undercoat is 1μm.
非阵列负极的制备:将Dv50为15μm的石墨、羧甲基纤维素钠(CMC)和粘结剂丁苯橡胶按重量比97.7∶1.3∶1混合,得到第一粉料,采用静电喷涂方式将第一粉料喷涂到厚度为6μm的铜集流体上,制备第一区域;然后Dv50为30μm的石墨、羧甲基纤维素钠(CMC)和粘结剂丁苯橡胶按重量比97.7∶1.3∶1混合,得到第二粉料,采用静电喷涂将第二粉料喷涂到铜集流体上对应的第二区域。然后经过冷压和裁切得到负极极片。Preparation of non-array negative electrode: Mix graphite with a Dv50 of 15 μm, sodium carboxymethyl cellulose (CMC) and binder styrene-butadiene rubber in a weight ratio of 97.7:1.3:1 to obtain the first powder, which is then electrostatically sprayed. The first powder is sprayed onto a copper current collector with a thickness of 6 μm to prepare the first area; then graphite with a Dv50 of 30 μm, sodium carboxymethylcellulose (CMC) and binder styrene-butadiene rubber are used in a weight ratio of 97.7:1.3: 1 is mixed to obtain a second powder, and electrostatic spraying is used to spray the second powder onto the corresponding second area on the copper current collector. Then, the negative electrode piece is obtained through cold pressing and cutting.
隔离膜的制备:隔离膜基材为8μm厚的聚乙烯(PE),在隔离膜基材的两侧各涂覆2μm氧化铝陶瓷层,最后在涂布了陶瓷层的两侧各涂覆2.5mg/cm 2的粘结剂聚偏氟乙烯(PVDF),烘干。 Preparation of isolation film: The base material of the isolation film is 8 μm thick polyethylene (PE). A 2 μm alumina ceramic layer is coated on both sides of the isolation film base material. Finally, 2.5 μm alumina ceramic layer is coated on both sides of the ceramic layer. mg/cm 2 binder polyvinylidene fluoride (PVDF), dried.
电解液的制备:在含水量小于10ppm的环境下,将LiPF 6加入非水有机溶剂(碳酸乙烯酯(EC)∶碳酸丙烯酯(PC)∶碳酸二乙酯(DEC)和碳酸二甲酯(DMC)=1∶1∶1∶1,重量比),LiPF 6的浓度为1mol/L,混合均匀,得到电解液。 Preparation of electrolyte: In an environment with a water content of less than 10 ppm, add LiPF 6 to a non-aqueous organic solvent (ethylene carbonate (EC): propylene carbonate (PC): diethyl carbonate (DEC) and dimethyl carbonate ( DMC) = 1:1:1:1, weight ratio), the concentration of LiPF 6 is 1 mol/L, mix evenly to obtain an electrolyte.
锂离子电池的制备:将正极极片、隔离膜、负极极片按顺序依次叠好,使隔离膜处于正极极片和负极极片中间起到隔离的作用,并卷绕得到电极组件。将电极组件置于外包装铝塑膜中,在80℃下脱去水分后,注入上述电解液并封装,经过化成,脱气,切边等工艺流程得到锂离子电池。Preparation of lithium-ion battery: Stack the positive electrode sheet, isolation film, and negative electrode sheet in order, so that the isolation film is between the positive electrode sheet and the negative electrode sheet for isolation, and wind it to obtain the electrode assembly. The electrode assembly is placed in the outer packaging aluminum plastic film, and after the moisture is removed at 80°C, the above-mentioned electrolyte is injected and packaged. After formation, degassing, trimming and other processes, a lithium-ion battery is obtained.
实施例1-1至实施例1-11、对比例1-3和对比例1-4都是采用极片宽度方向条纹形貌(如图3所示),区别之处参见表1。对比例1-1仅采用Dv50为15μm的石墨,即仅具有第一区域。对比例1-2中采用5∶1混合Dv50为155μm与Dv50为305μm的石墨,即不具有第一区域和第二区域。Examples 1-1 to 1-11, Comparative Examples 1-3 and 1-4 all adopt the stripe morphology in the width direction of the pole piece (as shown in Figure 3). See Table 1 for the differences. Comparative Example 1-1 only uses graphite with a Dv50 of 15 μm, that is, it only has the first region. In Comparative Example 1-2, a 5:1 mixture of graphite with Dv50 of 155 μm and Dv50 of 305 μm was used, that is, it did not have the first region and the second region.
从表1的实施例1-1至实施例1-11、对比例1-3和对比例1-4可以看出:负极活性材 料层中,第一区域与第二区域的适当分布,具体地,第一区域与第二区域的厚度比值、宽度比值、面积占比、颗粒粒径以及孔隙率在本申请范围内,锂离子电池的直流内阻显著降低,从而实现大倍率放电的情况下较高的容量保持率。对比例1-1和对比例1-2均不具有本申请的第一区域和第二区域,对比例1-1中仅具有小颗粒石墨,对比例1-2中两种颗粒石墨的混合会导致大颗粒间空隙被小颗粒填充,离子扩散路径变长或受阻,导致锂离子电池的直流内阻增加,无法实现大倍率放电的情况下较高的容量保持率。It can be seen from Example 1-1 to Example 1-11, Comparative Example 1-3 and Comparative Example 1-4 in Table 1: the appropriate distribution of the first region and the second region in the negative active material layer, specifically , the thickness ratio, width ratio, area ratio, particle size and porosity of the first region and the second region are within the scope of the present application. The DC internal resistance of the lithium-ion battery is significantly reduced, thereby achieving a relatively high rate of discharge at a high rate. High capacity retention rate. Neither Comparative Example 1-1 nor Comparative Example 1-2 has the first region and the second region of the present application. Comparative Example 1-1 only has small particles of graphite. The mixture of two kinds of graphite particles in Comparative Example 1-2 will cause As a result, the gaps between large particles are filled with small particles, and the ion diffusion path becomes longer or blocked, causing the DC internal resistance of the lithium-ion battery to increase, making it impossible to achieve a higher capacity retention rate under high-rate discharge.
实施例2-1至实施例2-8都是采用极片长度方向条纹形貌(如图4所示),具体如下表2。Examples 2-1 to 2-8 all adopt the stripe morphology in the length direction of the pole piece (as shown in Figure 4), as detailed in Table 2 below.
通过表2的实施例可以看出:对于极片长度方向条纹形貌,第一区域与第二区域的厚度比值、宽度比值、面积占比、颗粒粒径以及孔隙率在本申请范围内,均有利于提高电解液扩散效率,锂离子电池的直流内阻显著降低,从而实现大倍率放电的情况下较高的容量保持率,有利于提升电化学装置的动力学性能。It can be seen from the examples in Table 2 that for the stripe morphology in the length direction of the pole piece, the thickness ratio, width ratio, area ratio, particle size and porosity of the first region and the second region are all within the scope of the present application. It is beneficial to improve the electrolyte diffusion efficiency, and the DC internal resistance of the lithium-ion battery is significantly reduced, thereby achieving a higher capacity retention rate under high-rate discharge, which is beneficial to improving the dynamic performance of the electrochemical device.
实施例3-1至实施例3-7都是采用岛状分布形貌(如图5所示),具体如下表3。Examples 3-1 to 3-7 all adopt island-like distribution morphology (as shown in Figure 5), as detailed in Table 3 below.
通过表3的实施例可以看出:对于岛状分布形貌,第一区域与第二区域的厚度比值、宽度比值、面积占比、颗粒粒径以及孔隙率在本申请范围内,均有利于提高电解液扩散效率,锂离子电池的直流内阻显著降低,从而实现大倍率放电的情况下较高的容量保持率,有利于提升电化学装置的动力学性能。It can be seen from the examples in Table 3 that for the island-like distribution morphology, the thickness ratio, width ratio, area ratio, particle size and porosity of the first region and the second region are within the scope of this application, which is beneficial to By improving the electrolyte diffusion efficiency, the DC internal resistance of the lithium-ion battery is significantly reduced, thereby achieving a higher capacity retention rate under high-rate discharge, which is beneficial to improving the kinetic performance of the electrochemical device.
此外,表1至表3的实施例中,第一区域和第二区域的活性材料颗粒为非阵列排布,根据实施例1-1至1-8、实施例2-1至2-8以及实施例3-1至3-8的比较发现,沿极片宽度方向贯穿设置的第二区域的技术方案中,电化学装置的直流内阻及放电容量保持率优于第二区域沿长度方向贯通设置或岛状设置的情形,这可能是由于电极组件沿长度方向卷绕时,电解液能够由卷绕式电极组件的两端浸润,沿极片宽度方向贯通设置的第二区域有助于电解液的区域扩散,从而改善电化学装置的直流内阻,在较高倍率的放电中能够维持更优的容量保持率。对于岛状分布形貌,第二区域的比例较少,因此直流内阻偏大,3C放电倍率容量保持率偏低,但第一区域的比例增加能够使得能量密度提升。In addition, in the embodiments of Tables 1 to 3, the active material particles in the first region and the second region are arranged in a non-array, according to Embodiments 1-1 to 1-8, Embodiments 2-1 to 2-8 and Comparison of Examples 3-1 to 3-8 found that in the technical solution in which the second region is provided along the width direction of the pole piece, the DC internal resistance and discharge capacity retention rate of the electrochemical device are better than that in which the second region is provided along the length direction. This may be due to the fact that when the electrode assembly is wound along the length direction, the electrolyte can be infiltrated from both ends of the wound electrode assembly, and the second area arranged through the width direction of the pole piece is helpful for electrolysis. The regional diffusion of the liquid improves the DC internal resistance of the electrochemical device and maintains a better capacity retention rate in higher rate discharges. For the island-like distribution morphology, the proportion of the second region is small, so the DC internal resistance is relatively large, and the 3C discharge rate capacity retention rate is low, but the increased proportion of the first region can increase the energy density.
Figure PCTCN2022084118-appb-000001
Figure PCTCN2022084118-appb-000001
Figure PCTCN2022084118-appb-000002
Figure PCTCN2022084118-appb-000002
实施例4-1Example 4-1
正极极片、隔离膜、电解液、锂离子电池的制备方法与实施例1相同;The preparation methods of the positive electrode sheet, separator, electrolyte, and lithium-ion battery are the same as in Example 1;
底涂层:将导电碳∶PVDF=97∶3的比例在水中混合,通过转移涂布涂敷在6μm Cu集流体上,底涂层厚度为2.5μm。Undercoating: Mix conductive carbon:PVDF=97:3 in water and apply it on the 6μm Cu current collector by transfer coating. The thickness of the undercoat is 2.5μm.
阵列负极的制备:将小颗粒度石墨、羧甲基纤维素钠(CMC)和粘结剂丁苯橡胶按重量比97.7∶1.3∶1的比例溶于去离子水中,形成小颗粒负极浆料,固含量70%;大颗粒负极浆料制备与小颗粒相同;利用3D打印技术将小颗粒负极浆料垂直于集流体挤出到6μm Cu集流体上,同时利用热光源使水挥发,将打印出的浆料短时间固化,形成需要的形貌;然后利用3D打印将大颗粒浆料打印到相应位置上,然后冷压和裁切得到阵列负极极片,其中,活性材料颗粒原料的长径比为2至5。Preparation of array negative electrode: Dissolve small particle size graphite, sodium carboxymethylcellulose (CMC) and binder styrene-butadiene rubber in deionized water at a weight ratio of 97.7:1.3:1 to form a small particle negative electrode slurry. The solid content is 70%; the preparation of large-particle anode slurry is the same as that of small particles; 3D printing technology is used to extrude the small-particle anode slurry perpendicularly to the current collector onto a 6μm Cu current collector, and a thermal light source is used to volatilize water at the same time, and the printed The slurry is cured in a short time to form the required morphology; then 3D printing is used to print the large particle slurry to the corresponding position, and then cold pressed and cut to obtain the array negative electrode piece, in which the aspect ratio of the active material particle raw material is 2 to 5.
实施例4-1至实施例4-8、对比例4-3和对比例4-4都是采用极片宽度方向条纹形貌,区别之处具体如下表4。对比例4-1仅采用Dv50为15μm的石墨,即仅具有第一区域。对比例4-2中采用5∶1混合Dv50为155μm与Dv50为305μm的石墨,即不具有第一区域和第二区域。Examples 4-1 to 4-8, Comparative Examples 4-3 and 4-4 all adopt the stripe morphology in the width direction of the pole piece. The differences are detailed in Table 4 below. Comparative Example 4-1 only uses graphite with a Dv50 of 15 μm, that is, it only has the first region. In Comparative Example 4-2, a 5:1 mixture of graphite with Dv50 of 155 μm and Dv50 of 305 μm was used, that is, it did not have the first region and the second region.
通过表4的实施例和对比例可以看出:负极活性材料层中,第一区域与第二区域的适当分布,具体地,第一区域与第二区域的厚度比值、宽度比值、面积占比、颗粒粒径以及孔隙率在本申请范围内,锂离子电池的直流内阻显著降低,从而实现大倍率放电的情况下较高的容量保持率。It can be seen from the examples and comparative examples in Table 4: the appropriate distribution of the first region and the second region in the negative active material layer, specifically, the thickness ratio, width ratio, and area ratio of the first region and the second region. , particle size and porosity within the scope of this application, the DC internal resistance of the lithium-ion battery is significantly reduced, thereby achieving a higher capacity retention rate under high-rate discharge.
通过表1和表4的实施例的比较,例如通过实施例1-7与实施例4-1或通过实施例1-8与实施例4-5的比较可以看出:由于负极采用阵列排布,电化学装置的动力学性能可以进一步提升,因此极片的厚度可以进一步提升,阵列排布石墨的厚度采用120μm可以达到非阵列排布石墨100μm的动力学水平。By comparing the examples in Table 1 and Table 4, for example, by comparing Examples 1-7 with Example 4-1 or by comparing Examples 1-8 with Examples 4-5, it can be seen that since the negative electrode adopts an array arrangement , the kinetic performance of the electrochemical device can be further improved, so the thickness of the pole piece can be further increased. The thickness of array-arranged graphite can be 120 μm to reach the kinetic level of 100 μm for non-array-arranged graphite.
实施例5-1至实施例5-7都是采用极片长度方向条纹形貌,具体如下表5。Examples 5-1 to 5-7 all adopt the stripe morphology in the length direction of the pole piece, as detailed in Table 5 below.
通过表5的实施例可以看出,对于极片长度方向条纹形貌,第一区域与第二区域的厚度比值、宽度比值、面积占比、颗粒粒径以及孔隙率在本申请范围内,均有利于提高电解液扩散效率,锂离子电池的直流内阻显著降低,从而实现大倍率放电的情况下较高的容量保持率,有利于提升电化学装置的动力学性能。It can be seen from the examples in Table 5 that for the stripe morphology in the length direction of the pole piece, the thickness ratio, width ratio, area ratio, particle size and porosity of the first region and the second region are all within the scope of the present application. It is beneficial to improve the electrolyte diffusion efficiency, and the DC internal resistance of the lithium-ion battery is significantly reduced, thereby achieving a higher capacity retention rate under high-rate discharge, which is beneficial to improving the dynamic performance of the electrochemical device.
通过表2和表5的实施例的比较,例如通过实施例2-7与实施例5-1或通过实施例2-8与实施例5-5的比较可以看出:由于负极采用阵列排布,电化学装置的动力学性能可以进一步提升。By comparing the examples in Table 2 and Table 5, for example, by comparing Example 2-7 with Example 5-1 or by comparing Example 2-8 with Example 5-5, it can be seen that since the negative electrode adopts an array arrangement , the kinetic performance of the electrochemical device can be further improved.
实施例6-1至实施例6-7都是采用岛状形貌,具体如下表6。Examples 6-1 to 6-7 all adopt island morphology, as shown in Table 6 below.
通过表6的实施例可以看出,对于岛状形貌,第一区域与第二区域的厚度比值、宽度比值、面积占比、颗粒粒径以及孔隙率在本申请范围内,均有利于提高电解液扩散效率,锂离子电池的直流内阻显著降低,从而实现大倍率放电的情况下较高的容量保持率,有利于提升电化学装置的动力学性能。。It can be seen from the examples in Table 6 that for the island-shaped morphology, the thickness ratio, width ratio, area ratio, particle size and porosity of the first region and the second region are within the scope of this application, which is beneficial to improving The electrolyte diffusion efficiency and the DC internal resistance of lithium-ion batteries are significantly reduced, thereby achieving a higher capacity retention rate under high-rate discharge, which is beneficial to improving the kinetic performance of the electrochemical device. .
通过表3和表6的实施例的比较,例如通过实施例3-7与实施例6-1的比较可以看出:由于负极采用阵列排布,电化学装置的动力学性能可以进一步提升。By comparing the examples in Table 3 and Table 6, for example, by comparing Example 3-7 with Example 6-1, it can be seen that since the negative electrode is arranged in an array, the kinetic performance of the electrochemical device can be further improved.
此外,通过表4至表6可以看出,阵列排布的条形形貌和岛状形貌的性能规律与非阵列排布相同,即沿极片宽度方向贯穿设置的第二区域相比于沿长度方向贯通设置或岛状设置,电化学装置的直流内阻及放电容量保持率更优。In addition, it can be seen from Table 4 to Table 6 that the performance rules of the strip morphology and island morphology of the array arrangement are the same as those of the non-array arrangement, that is, the second area arranged throughout the width direction of the pole piece is compared with If it is arranged through the length direction or in an island shape, the DC internal resistance and discharge capacity retention rate of the electrochemical device are better.
Figure PCTCN2022084118-appb-000003
Figure PCTCN2022084118-appb-000003
Figure PCTCN2022084118-appb-000004
Figure PCTCN2022084118-appb-000004
以上各实施例仅用以说明本申请的技术方案,而非对其限制;尽管参照前述各实施例对本申请进行了详细的说明,本领域的普通技术人员应当理解:其依然可以对前述各实施例所记载的技术方案进行修改,或者对其中部分或者全部技术特征进行等同替换;而这些修改或者替换,并不使相应技术方案的本质脱离本申请技术方案的范围。The above embodiments are only used to illustrate the technical solutions of the present application, but not to limit them. Although the present application has been described in detail with reference to the foregoing embodiments, those of ordinary skill in the art should understand that they can still implement the foregoing implementations. The technical solutions described in the examples are modified, or some or all of the technical features are equivalently replaced; and these modifications or substitutions do not cause the essence of the corresponding technical solutions to deviate from the scope of the technical solution of this application.

Claims (10)

  1. 一种负极极片,包括集流体和负极活性材料层,所述负极活性材料层包括第一区域和第二区域,其中所述第一区域的孔隙率小于所述第二区域的孔隙率,所述第一区域的活性材料颗粒Dv50与所述第二区域的活性材料颗粒Dv50的比值为0.3至0.9。A negative electrode plate includes a current collector and a negative active material layer. The negative active material layer includes a first region and a second region, wherein the porosity of the first region is smaller than the porosity of the second region, so The ratio of Dv50 of the active material particles in the first region to the Dv50 of the active material particles in the second region is 0.3 to 0.9.
  2. 根据权利要求1所述的负极极片,其中,满足以下条件中的至少一者:The negative electrode plate according to claim 1, wherein at least one of the following conditions is met:
    (a)所述第一区域的活性材料颗粒的Dv50为5μm至20μm,(a) The Dv50 of the active material particles in the first region is 5 μm to 20 μm,
    (b)所述第二区域的活性材料颗粒的Dv50为20μm至50μm,(b) the Dv50 of the active material particles in the second region is 20 μm to 50 μm,
    (c)所述第一区域的孔隙率为15%至30%,(c) the porosity of the first region is 15% to 30%,
    (d)所述第二区域的孔隙率为30%至45%。(d) The second region has a porosity of 30% to 45%.
  3. 根据权利要求1所述的负极极片,其中,所述第一区域和/或所述第二区域的活性材料颗粒为阵列排布,且活性材料颗粒的长径比为1.1至5。The negative electrode sheet according to claim 1, wherein the active material particles in the first region and/or the second region are arranged in an array, and the aspect ratio of the active material particles is 1.1 to 5.
  4. 根据权利要求1-3中任一项所述的负极极片,其中,所述第一区域和/或所述第二区域的活性材料颗粒沿长径方向与集流体之间的角度为45°至135°。The negative electrode sheet according to any one of claims 1 to 3, wherein an angle between the active material particles in the first region and/or the second region and the current collector along the long diameter direction is 45°. to 135°.
  5. 根据权利要求1-3中任一项所述的负极极片,其中,沿极片厚度方向,基于所述活性材料层的投影面积,所述第二区域的投影面积占比为5%至50%。The negative electrode piece according to any one of claims 1 to 3, wherein along the thickness direction of the electrode piece, based on the projected area of the active material layer, the projected area ratio of the second region is 5% to 50%. %.
  6. 根据权利要求1-3中任一项所述的负极极片,其中,满足以下条件中的至少一者:The negative electrode piece according to any one of claims 1-3, wherein at least one of the following conditions is met:
    (e)所述第二区域为条形分布或者岛状分布,(e) The second area is a strip distribution or an island distribution,
    (f)所述第二区域沿所述负极极片宽度方向贯通设置,(f) the second region is provided through the negative electrode piece in the width direction,
    (g)所述负极极片的粘结力为5N/m至15N/m。(g) The bonding force of the negative electrode piece is 5N/m to 15N/m.
  7. 根据权利要求1-3中任一项所述的负极极片,其中,所述第一区域的厚度与所述第二区域的厚度的比值为1至2;和/或所述第一区域的宽度与所述第二区域的宽度的比值为1至20。The negative electrode piece according to any one of claims 1 to 3, wherein the ratio of the thickness of the first region to the thickness of the second region is 1 to 2; and/or the thickness of the first region is The ratio of the width to the width of the second area is 1 to 20.
  8. 根据权利要求1-3中任一项所述的负极极片,其中,在所述集流体和所述负极活性材料层之间还设置有底涂层,所述底涂层的厚度为0.5μm至3.0μm。The negative electrode sheet according to any one of claims 1 to 3, wherein an undercoat layer is further provided between the current collector and the negative active material layer, and the thickness of the undercoat layer is 0.5 μm. to 3.0μm.
  9. 一种电化学装置,包括权利要求1-8中任一项所述的负极极片。An electrochemical device comprising the negative electrode piece according to any one of claims 1-8.
  10. 一种电子装置,包括权利要求9所述的电化学装置。An electronic device comprising the electrochemical device according to claim 9.
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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109301160A (en) * 2018-09-05 2019-02-01 上海奥威科技开发有限公司 A kind of electrode and preparation method thereof and lithium-ion capacitor battery
CN111261834A (en) * 2020-03-25 2020-06-09 宁德新能源科技有限公司 Negative electrode sheet, electrochemical device, and electronic device
CN113097431A (en) * 2021-03-30 2021-07-09 宁德新能源科技有限公司 Electrochemical device and electronic device
CN215600510U (en) * 2021-09-27 2022-01-21 宁德时代新能源科技股份有限公司 Pole piece structure, battery monomer and electric device

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109301160A (en) * 2018-09-05 2019-02-01 上海奥威科技开发有限公司 A kind of electrode and preparation method thereof and lithium-ion capacitor battery
CN111261834A (en) * 2020-03-25 2020-06-09 宁德新能源科技有限公司 Negative electrode sheet, electrochemical device, and electronic device
CN113097431A (en) * 2021-03-30 2021-07-09 宁德新能源科技有限公司 Electrochemical device and electronic device
CN215600510U (en) * 2021-09-27 2022-01-21 宁德时代新能源科技股份有限公司 Pole piece structure, battery monomer and electric device

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