WO2023082264A1 - 一种负极极片及包含其的电化学装置和电子设备 - Google Patents

一种负极极片及包含其的电化学装置和电子设备 Download PDF

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WO2023082264A1
WO2023082264A1 PCT/CN2021/130699 CN2021130699W WO2023082264A1 WO 2023082264 A1 WO2023082264 A1 WO 2023082264A1 CN 2021130699 W CN2021130699 W CN 2021130699W WO 2023082264 A1 WO2023082264 A1 WO 2023082264A1
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negative electrode
pole piece
active material
negative
material layer
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PCT/CN2021/130699
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English (en)
French (fr)
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朱珊
关婷
吴飞
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宁德新能源科技有限公司
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Priority to CN202180012765.5A priority Critical patent/CN115088095B/zh
Priority to PCT/CN2021/130699 priority patent/WO2023082264A1/zh
Publication of WO2023082264A1 publication Critical patent/WO2023082264A1/zh
Priority to US18/664,815 priority patent/US20240304809A1/en

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    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • H01M4/139—Processes of manufacture
    • H01M4/1395—Processes of manufacture of electrodes based on metals, Si or alloys
    • H—ELECTRICITY
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    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
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    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00—Secondary cells; Manufacture thereof
    • H01M10/05—Accumulators with non-aqueous electrolyte
    • H01M10/052—Li-accumulators
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    • H01M10/00—Secondary cells; Manufacture thereof
    • H01M10/05—Accumulators with non-aqueous electrolyte
    • H01M10/052—Li-accumulators
    • H01M10/0525—Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
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    • H01M4/0404—Methods of deposition of the material by coating on electrode collectors
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    • H01M4/04—Processes of manufacture in general
    • H01M4/0471—Processes of manufacture in general involving thermal treatment, e.g. firing, sintering, backing particulate active material, thermal decomposition, pyrolysis
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    • H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • H01M4/133—Electrodes based on carbonaceous material, e.g. graphite-intercalation compounds or CFx
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    • H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • H01M4/134—Electrodes based on metals, Si or alloys
    • H—ELECTRICITY
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    • H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • H01M4/139—Processes of manufacture
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    • H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
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    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/36—Selection of substances as active materials, active masses, active liquids
    • H01M4/38—Selection of substances as active materials, active masses, active liquids of elements or alloys
    • H01M4/386—Silicon or alloys based on silicon
    • H—ELECTRICITY
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    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/36—Selection of substances as active materials, active masses, active liquids
    • H01M4/58—Selection of substances as active materials, active masses, active liquids of inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFy; of polyanionic structures, e.g. phosphates, silicates or borates
    • H01M4/583—Carbonaceous material, e.g. graphite-intercalation compounds or CFx
    • H—ELECTRICITY
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    • H01M4/36—Selection of substances as active materials, active masses, active liquids
    • H01M4/58—Selection of substances as active materials, active masses, active liquids of inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFy; of polyanionic structures, e.g. phosphates, silicates or borates
    • H01M4/583—Carbonaceous material, e.g. graphite-intercalation compounds or CFx
    • H01M4/587—Carbonaceous material, e.g. graphite-intercalation compounds or CFx for inserting or intercalating light metals
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    • H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • H—ELECTRICITY
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    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • H01M4/621—Binders
    • H01M4/622—Binders being polymers
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • H01M4/621—Binders
    • H01M4/622—Binders being polymers
    • H01M4/623—Binders being polymers fluorinated polymers
    • H—ELECTRICITY
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    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • H01M4/624—Electric conductive fillers
    • H01M4/625—Carbon or graphite
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M2004/021—Physical characteristics, e.g. porosity, surface area
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M2004/026—Electrodes composed of, or comprising, active material characterised by the polarity
    • H01M2004/027—Negative electrodes
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10—Energy storage using batteries

Definitions

  • the present application relates to the field of electrochemical technology, in particular to a negative electrode sheet and an electrochemical device and electronic equipment including the same.
  • lithium-ion batteries As an efficient mobile energy source, lithium-ion batteries have been widely used in electronic products such as mobile phones, notebook computers, and digital cameras due to their advantages of high voltage, high specific energy, and long cycle life. Especially with the rapid popularization of smart phones in recent years, people have higher and higher requirements for the charging rate and energy density of lithium-ion batteries for energy storage.
  • the negative electrode material and negative electrode formula are usually adjusted to improve the negative electrode kinetics, but the adjustment of the negative electrode material and formula will bring certain processing problems, and the improvement of the kinetics is relatively limited. It is urgent to find a new way to solve the above problems.
  • the present application provides a negative electrode sheet, which has better kinetic performance, so that the electrochemical device to which it is applied has a faster charging rate.
  • the first aspect of the present application provides a negative pole piece, the temperature corresponding to the peak height of the first peak of the differential curve (DTG curve) of the thermogravimetric curve (TG curve) is greater than 350°C;
  • K is a correction parameter
  • K 15 ⁇ m/Dv50
  • Dv50 is the negative electrode
  • the median particle size of the active material is a correction parameter
  • the active specific surface area of the negative electrode active material layer of the present application refers to the ratio of the active surface area of the negative electrode active material layer to the mass of the negative electrode active material layer, which can be used to reflect the number of active sites when the negative electrode sheet is charged and discharged.
  • the inventors have found that the activity The larger the specific surface area, the higher the lithium separation window, and the faster the charging speed.
  • the inventor found in research that the active specific surface area of the negative electrode active material layer is related to the microstructure of the negative electrode active material layer and the average particle size of the negative electrode active material.
  • the value of the obtained activity specific surface area more objectively reflects the internal microstructure of the active material layer.
  • the negative electrode active material layer of the present application has a higher active specific surface area, indicating that the active material layer of the negative electrode sheet of the present application has a different microstructure from the existing negative electrode active material layer.
  • the inventors have found that the temperature corresponding to the peak height of the first peak of the DTG curve (differential curve of TG) is greater than 350° C., and the negative electrode active material layer has more Due to the high active specific surface area, the inventors found that the negative electrode sheet has better kinetic performance, and the electrochemical device using the negative electrode sheet has a faster charging rate and better electrochemical performance.
  • the "peak height” mentioned in this application can be understood as the maximum value of the first peak.
  • Dv50 means the particle diameter at which the particle cumulative distribution is 50%, also called the median particle diameter, that is, the volume content of particles smaller than this particle diameter accounts for 50% of all particles.
  • min minutes
  • the differential curve of the thermogravimetric curve described in the present application can be obtained by conventional methods in the art, for example, can be obtained by the following method: the negative electrode sheet is cut into small discs with a diameter of 14 mm, and The thermogravimetric analysis test is carried out under the following conditions, the test temperature is raised from 25°C to 600°C, and the heating rate is 10°C/min, the thermogravimetric curve is obtained, and the thermogravimetric curve is differentiated to obtain the differential curve of the thermogravimetric curve.
  • the average particle diameter Dv50 of the negative electrode active material satisfies: 100nm ⁇ Dv50 ⁇ 30 ⁇ m.
  • the application does not limit the type of negative electrode active material.
  • various components existing as lithium ion battery negative electrode active materials can be used, such as graphite-based negative electrode materials containing graphite, including at least one of silicon carbon and silicon oxide.
  • the silicon material is used as the negative electrode material, or hard carbon-based negative electrode materials such as resin carbon, organic polymer pyrolytic carbon, carbon black, etc., and composite negative electrode materials mixed with different types of negative electrode materials in a certain proportion.
  • the inventors have found that different negative electrode materials have different particle size ranges.
  • the Dv50 of silicon-based negative electrode materials is usually 100 nm to 20 ⁇ m; the Dv50 of graphite-based negative electrode materials is usually 10 ⁇ m to 30 ⁇ m; , compared with the negative electrode sheet obtained by the existing method, the negative electrode active material layer has a larger active specific surface area.
  • the negative electrode active material layer further includes long-range fibers.
  • Long-range fibers in this application include some long-range conductive carbon or long-range ceramic fibers or long-range polymer fibers, etc.
  • the long-range conductive carbon refers to a conductive carbon material with a one-dimensional structure, such as at least one of carbon nanotubes and carbon nanofibers.
  • the inventors found that the long-distance fiber has a fibrous structure, which increases the contact with the negative electrode active material particles, can significantly improve the cohesion of the pole piece, and has a good effect on the expansion of the pole piece during the cycle process of the lithium-ion battery. Inhibition, to avoid the loss of volumetric energy density of lithium-ion batteries during cycle use.
  • the inventors also found that although the introduction of long-range fibers can improve the expansion of lithium-ion batteries, it has caused the deterioration of the kinetic performance of the battery cell, such as the decrease of the lithium separation window; After the method of the present application is heat-treated, the obtained negative electrode sheet can realize the modification of the cycle expansion performance of the battery cell under the premise of ensuring the dynamic performance of the lithium-ion battery, taking into account reliability and fast charging performance.
  • the length of the long-range fiber is greater than 1 ⁇ m, preferably, the length of the long-range fiber is 1 ⁇ m to 1 mm; preferably 1 ⁇ m to 50 ⁇ m; the inventors have found that further increasing the length of the long-range fiber does not bring about Additional advantage.
  • the present application does not limit the diameter of the long-distance fiber, for example, it may be 1 to 200 nm.
  • the mass content of the long-distance fibers is 0.2% to 1.5%.
  • the inventors have found that when the content of long-range fibers is too low (for example, less than 0.2%), it cannot play a role in alleviating the expansion of the negative electrode; when the content of long-range conductive carbon is too high (for example, higher than 1.5%) , not only will reduce the relative content of the active material in the negative electrode sheet, affect the energy density of the lithium-ion battery, but also have a greater impact on the kinetic performance of the negative electrode sheet.
  • the inventor also found that the negative electrode sheet of the present application, the increase in the active specific surface area of its negative electrode active material layer does not bring the problem of SEI (Solid Electrolyte Interphase, solid electrolyte interface) film thickening, more The important thing is that the electrochemical reaction energy barrier of the negative electrode active material layer of the present application is reduced, so that the negative electrode sheet has lower activation energy.
  • the electrochemical reaction activation energy Ea of the negative electrode sheet satisfies: 25kJ/mol ⁇ Ea ⁇ 55kJ/mol.
  • the inventors found that when the negative electrode active material does not contain silicon, the negative electrode sheet has lower electrochemical reaction activation energy, and its Ea satisfies: 25kJ/mol ⁇ Ea ⁇ 37kJ/mol, the negative electrode sheet of the present application Compared with the existing negative electrode sheet, the activation energy is lower, which is more conducive to the improvement of the kinetic performance of the lithium-ion battery.
  • the negative electrode active material layer also includes a conductive agent, and the application does not limit the type of the conductive agent, for example, it may include conductive carbon black, conductive graphite, graphene and acetylene black. At least one; the conductivity of the negative electrode can be improved by adding a conductive agent.
  • the present application has no special limitation on the content of the conductive agent in the negative electrode active material layer, as long as the purpose of the application can be achieved, for example, the conductive agent accounts for 0% to 1% of the total mass of the negative electrode active material layer.
  • the negative electrode active material layer further includes a binder, and the application does not limit the type of the binder, for example, the binder may include polyvinylidene fluoride, vinylidene fluoride -at least one of copolymers of fluorinated olefins, polyvinylpyrrolidone, polyacrylonitrile, polymethylacrylate, polytetrafluoroethylene, styrene-butadiene rubber, polyurethane, fluorinated rubber and polyvinyl alcohol; the addition of binders
  • the viscosity of the negative electrode active material layer can be improved, the possibility of falling off of the negative electrode active material and the conductive agent in the negative electrode active material layer can be reduced, and the possibility of falling off of the negative electrode active material layer from the current collector can also be reduced.
  • the present application has no special limitation on the content of the binder in the negative electrode active material layer, as long as the purpose of the application can be achieved, for example, the binder accounts for
  • the negative electrode sheet of the present application can be made by arranging the negative electrode active material layer on the negative electrode current collector. Collectors, etc.
  • the thickness of the negative electrode current collector and the negative electrode active material layer is not particularly limited, as long as the purpose of the present application can be achieved.
  • the thickness of the negative electrode current collector is 6 ⁇ m to 10 ⁇ m
  • the thickness of the negative electrode active material layer is 30 ⁇ m to 120 ⁇ m.
  • the second aspect of the present application provides the preparation method of the negative electrode sheet of the first aspect of the present application, which includes:
  • the modification treatment includes at least one of plasma treatment, heat treatment and laser treatment.
  • the plasma treatment may be: the initial pole piece is treated with plasma in a vacuum environment, the power range of the plasma treatment is 0.5k to 5kW, and the gas source includes At least one of nitrogen, argon and carbon tetrafluoride, the gas flow range is 200mL/min to 3000mL/min, the temperature range is 20°C to 60°C, and the processing time is 1min to 60min;
  • the heat treatment may be: placing the initial pole piece in a vacuum or an inert gas environment, and heat treatment for 1 minute to 60 minutes at a temperature ranging from 200°C to 350°C;
  • the heating method is not limited, as long as the purpose of the application can be achieved, for example, blast heating, infrared heating, microwave heating, electromagnetic induction heating, etc. can be used;
  • the laser treatment may be: treating the initial pole piece for 1s to 600s under the condition of a vacuum or an inert gas environment and a laser intensity of 30W to 100W; specifically, In a vacuum or an inert gas environment, the initial pole piece is placed within the working range of the laser transmitter, the laser intensity is 30W to 100W, the distance between the laser source and the initial pole piece is 3cm to 10cm, and the treatment is 1s to 600s.
  • the preparation of the initial pole piece can adopt the conventional method in the field, and the above-mentioned description of the negative pole piece can be used for the composition and content of the negative electrode active material layer. After the neutralization treatment, the negative electrode sheet described in this application can be obtained.
  • the third aspect of the present application provides an electrochemical device, which includes the negative electrode sheet described in the first aspect of the application; and other components, including the positive electrode sheet, diaphragm and electrolyte, are not particularly limited, as long as It is enough to realize the purpose of this application.
  • a positive electrode sheet generally includes a positive electrode current collector and a positive electrode active material layer.
  • the positive electrode current collector is not particularly limited, and may be a positive electrode current collector known in the art, such as copper foil, aluminum foil, aluminum alloy foil, and a composite current collector.
  • the positive electrode active material layer includes a positive electrode active material, the positive electrode active material is not particularly limited, and can be a positive electrode active material known in the art, for example, including nickel cobalt lithium manganate (811, 622, 523, 111), nickel cobalt lithium aluminate, At least one of lithium iron phosphate, lithium-rich manganese-based materials, lithium cobaltate, lithium manganate, lithium iron manganese phosphate or lithium titanate.
  • the thicknesses of the positive electrode current collector and the positive electrode active material layer are not particularly limited, as long as the purpose of the present application can be achieved.
  • the thickness of the positive electrode current collector is 8 ⁇ m to 12 ⁇ m
  • the thickness of the positive electrode active material layer is 30 ⁇ m to 120 ⁇ m.
  • the positive electrode sheet may further include a conductive layer, and the conductive layer is located between the positive electrode current collector and the positive electrode active material layer.
  • the composition of the conductive layer is not particularly limited, and may be a commonly used conductive layer in the field.
  • the conductive layer includes a conductive agent and a binder.
  • the conductive agent is not particularly limited, and may be any conductive agent known to those skilled in the art or a combination thereof, for example, at least one of a zero-dimensional conductive agent, a one-dimensional conductive agent and a two-dimensional conductive agent may be used.
  • the conductive agent may include at least one of carbon black, conductive graphite, carbon fiber, carbon nanotube, VGCF (vapour-grown carbon nanofiber) or graphene.
  • the amount of the conductive agent is not particularly limited, and can be selected according to common knowledge in the art. One of the above-mentioned conductive agents may be used alone, or two or more of them may be used in combination in an arbitrary ratio.
  • the binder in the conductive layer is not particularly limited, and may be any binder known to those skilled in the art or a combination thereof, such as polyacrylate, polyimide, polyamide, polyamideimide, polyamideimide, At least one of polyvinylidene fluoride, styrene-butadiene rubber, sodium alginate, polyvinyl alcohol, polytetrafluoroethylene, polyacrylonitrile, sodium carboxymethyl cellulose, lithium carboxymethyl cellulose, and the like. These binders may be used alone or in combination of two or more in any ratio.
  • the electrochemical device of the present application also includes a separator, which is used to separate the positive electrode and the negative electrode, prevent the internal short circuit of the electrochemical device, allow electrolyte ions to pass through freely, and complete the electrochemical charging and discharging process.
  • the separator is not particularly limited, as long as the purpose of the present application can be achieved.
  • polyethylene PE
  • polypropylene PP
  • PO polyolefin
  • polyester film such as polyethylene terephthalate (PET) film
  • cellulose film polyamide Imine film (PI)
  • PI polyamide film
  • PA polyamide film
  • aramid film woven film, non-woven film (non-woven fabric), microporous film, composite film, separator paper, rolled film, spun film, etc.
  • a separator may include a substrate layer and a surface treatment layer.
  • the substrate layer can be a non-woven fabric, a film or a composite film with a porous structure, and the material of the substrate layer can include at least one of polyethylene, polypropylene, polyethylene terephthalate and polyimide, etc. kind.
  • a polypropylene porous film, a polyethylene porous film, a polypropylene non-woven fabric, a polyethylene non-woven fabric, or a polypropylene-polyethylene-polypropylene porous composite film may be used.
  • at least one surface of the substrate layer is provided with a surface treatment layer, and the surface treatment layer may be a polymer layer or an inorganic layer, or a layer formed by mixing a polymer and an inorganic material.
  • the inorganic layer includes inorganic particles and a binder
  • the inorganic particles are not particularly limited, for example, can be selected from aluminum oxide, silicon oxide, magnesium oxide, titanium oxide, hafnium oxide, tin oxide, cerium oxide, nickel oxide, At least one of zinc oxide, calcium oxide, zirconia, yttrium oxide, silicon carbide, boehmite, aluminum hydroxide, magnesium hydroxide, calcium hydroxide and barium sulfate.
  • the binder is not particularly limited, for example, it can be selected from polyvinylidene fluoride, copolymer of vinylidene fluoride-hexafluoropropylene, polyamide, polyacrylonitrile, polyacrylate, polyacrylic acid, polyacrylate, polyvinylpyrrolidine One or a combination of ketone, polyvinyl ether, polymethyl methacrylate, polytetrafluoroethylene and polyhexafluoropropylene.
  • the polymer layer comprises a polymer, and the polymer material includes polyamide, polyacrylonitrile, acrylate polymer, polyacrylic acid, polyacrylate, polyvinylpyrrolidone, polyvinyl ether, polyvinylidene fluoride or poly( at least one of vinylidene fluoride-hexafluoropropylene) and the like.
  • the electrochemical device of the present application also includes an electrolyte, which may be one or more of a gel electrolyte, a solid electrolyte, and an electrolyte, and the electrolyte includes a lithium salt and a non-aqueous solvent.
  • an electrolyte which may be one or more of a gel electrolyte, a solid electrolyte, and an electrolyte, and the electrolyte includes a lithium salt and a non-aqueous solvent.
  • the lithium salt is selected from lithium hexafluorophosphate (LiPF 6 ), lithium tetrafluoroborate (LiBF 4 ), lithium hexafluoroarsenate (LiAsF 6 ), lithium perchlorate (LiClO 4 ), Lithium tetraphenylborate (LiB(C 6 H 5 ) 4 ), lithium methanesulfonate (LiCH 3 SO 3 ), lithium trifluoromethanesulfonate (LiCF 3 SO 3 ), lithium bistrifluoromethanesulfonylimide ( One of LiN(SO 2 CF 3 ) 2 ), LiC(SO 2 CF 3 ) 3 , lithium hexafluorosilicate (LiSiF 6 ), lithium bisoxalate borate (LiBOB) and lithium difluoroborate (LiF 2 OB) or more.
  • LiPF 6 may be selected from lithium hexafluorophosphate (L
  • the non-aqueous solvent can be carbonate compound, carboxylate compound, ether compound, other organic solvent or their combination.
  • the above-mentioned carbonate compound can be a chain carbonate compound, a cyclic carbonate compound, a fluorocarbonate compound or a combination thereof.
  • Examples of the aforementioned chain carbonate compounds are dimethyl carbonate (DMC), diethyl carbonate (DEC), dipropyl carbonate (DPC), methylpropyl carbonate (MPC), ethylpropyl carbonate (EPC), carbonic acid Ethyl methyl ester (EMC) and combinations thereof.
  • Examples of cyclic carbonate compounds are ethylene carbonate (EC), propylene carbonate (PC), butylene carbonate (BC), vinylethylene carbonate (VEC), and combinations thereof.
  • fluorocarbonate compounds are fluoroethylene carbonate (FEC), 1,2-difluoroethylene carbonate, 1,1-difluoroethylene carbonate, 1,1,2-trifluoroethylene carbonate Ethyl carbonate, 1,1,2,2-tetrafluoroethylene carbonate, 1-fluoro-2-methylethylene carbonate, 1-fluoro-1-methylethylene carbonate, 1,2-dicarbonate Fluoro-1-methylethylene carbonate, 1,1,2-trifluoro-2-methylethylene carbonate, trifluoromethylethylene carbonate, and combinations thereof.
  • FEC fluoroethylene carbonate
  • 1,2-difluoroethylene carbonate 1,1-difluoroethylene carbonate
  • 1,1,2-trifluoroethylene carbonate Ethyl carbonate 1,1,2,2-tetrafluoroethylene carbonate
  • 1-fluoro-2-methylethylene carbonate 1-fluoro-1-methylethylene carbonate
  • 1,2-dicarbonate Fluoro-1-methylethylene carbonate
  • Examples of the above carboxylate compounds are methyl formate, methyl acetate, ethyl acetate, n-propyl acetate, tert-butyl acetate, methyl propionate, ethyl propionate, propyl propionate, ⁇ -butyrolactone , decanolactone, valerolactone, mevalonolactone, caprolactone, and combinations thereof.
  • ether compounds examples include dibutyl ether, tetraglyme, diglyme, 1,2-dimethoxyethane, 1,2-diethoxyethane, ethoxymethyl Oxyethane, 2-methyltetrahydrofuran, tetrahydrofuran, and combinations thereof.
  • Examples of the aforementioned other organic solvents are dimethylsulfoxide, 1,2-dioxolane, sulfolane, methylsulfolane, 1,3-dimethyl-2-imidazolidinone, N-methyl-2-pyrrolidone, Formamide, dimethylformamide, acetonitrile, trimethyl phosphate, triethyl phosphate, trioctyl phosphate, and phosphate esters, and combinations thereof.
  • an electrochemical device can be manufactured through the following process: overlap the positive electrode and the negative electrode through the separator, and put them into the case after winding, folding, etc. as required, inject the electrolyte into the case and seal it.
  • anti-overcurrent elements, guide plates, etc. can also be placed in the casing as needed, so as to prevent pressure rise and overcharge and discharge inside the electrochemical device.
  • the fourth aspect of the present application provides an electronic device, which includes the electrochemical device provided by the third aspect of the present application.
  • electronic devices may include, but are not limited to, notebook computers, pen-based computers, mobile computers, e-book players, cellular phones, portable fax machines, portable copiers, portable printers, headsets, video recorders , LCD TVs, portable cleaners, portable CD players, mini discs, transceivers, electronic organizers, calculators, memory cards, portable tape recorders, radios, backup power supplies, motors, cars, motorcycles, power-assisted bicycles, bicycles, lighting Appliances, toys, game consoles, clocks, electric tools, flashlights, cameras, large household storage batteries and lithium-ion capacitors, etc.
  • the temperature corresponding to the peak height of the first peak of the DTG curve of the negative electrode sheet is greater than 350°C; and the active specific surface area of the negative electrode active material layer is greater than or equal to K ⁇ 25cm 2 /g, the electrochemical device using the negative electrode sheet of the present application has better kinetic performance, the lithium analysis window is enlarged, and the charging rate is faster.
  • FIG. 1 is the TG curve and DTG curve of the negative electrode sheet of Example 1.
  • FIG. 2 is a TG curve and a DTG curve of the negative electrode sheet of Example 7.
  • FIG. 2 is a TG curve and a DTG curve of the negative electrode sheet of Example 7.
  • FIG. 3 is the TG curve and DTG curve of the negative electrode sheet of Comparative Example 2.
  • a lithium-ion battery is used as an example of an electrochemical device to explain the present application, but the electrochemical device of the present application is not limited to the lithium-ion battery.
  • the negative pole pieces of each example and comparative example were cut into discs with a diameter of 1.4 cm by a punching machine in a dry environment, and the mass was recorded as m.
  • a metal lithium sheet is used as a counter electrode
  • a ceglard composite membrane is selected as a separator
  • an electrolyte is added to assemble a button battery; wherein, the electrolyte contains an electrochemical redox probe molecule ferrocene with a concentration of c.
  • a series of cyclic voltammetry curves are obtained by using an electrochemical workstation to test at different scan rates v, and the peak current Ip is obtained from the cyclic voltammetry curves; the obtained series of peak current Ip and the square root of the scan rate v are plotted to obtain Slope K; according to the Randles-Sevick equation, the active surface area of the pole piece Among them, n represents the electron transfer number of the electrode reaction, which is 1 in this test system; c represents the concentration of probe molecules; D represents the diffusion coefficient of probe molecules.
  • the diffusion coefficient of ferrocene is 2.1 ⁇ 10 -6 cm 2 /s; the ratio of the active surface area A of the pole piece to the mass of the active material layer of the pole piece (m-the mass of the current collector) is the active specific surface area of the active material layer.
  • the negative pole pieces and the same positive pole pieces of each embodiment and comparative example were assembled into a lithium-ion battery respectively, installed on a charging and discharging device for charging and discharging, and monitoring the voltage and current of the lithium-ion battery to obtain the direct current of the lithium-ion battery. Impedance value. Specifically, the lithium-ion battery is charged at a constant current to a full charge voltage with a current of 0.5C, and then charged at a constant voltage to 0.05C. Then discharge at 1C current for 30 minutes to make the lithium-ion battery in a state of 50% charge ratio, and let it stand for 60 minutes. Discharge at a current of 0.1C for 10s, and record the voltage V1. Then discharge with a current of 1C for 1s, and record the voltage V2.
  • the polarization resistance 1s DCR of the lithium-ion battery is calculated according to the following formula:
  • the negative pole pieces of each example and comparative example were assembled into a lithium-ion battery, left to stand for 30 minutes at 25°C, charged at a constant current rate of 0.5C to the rated voltage, and then charged at a constant voltage until the charge-discharge rate reached 0.05 C stop charging.
  • the time between the time when charging starts and the time when charging stops is the full charge time.
  • the negative pole pieces prepared in each example and comparative example were assembled into a full battery.
  • the test temperature was 45°C, charged to the rated voltage with a constant current of 0.5C, charged to 0.025C at a constant voltage, and discharged to 0.5C after standing for 5 minutes. 3.0V.
  • the capacity obtained in this step is the initial capacity, and 0.5C charge/0.5C discharge is carried out for cycle test, and the capacity of each step is compared with the initial capacity to obtain the capacity decay curve; the capacity of each embodiment and comparative example after 300 cycles
  • the retention rate is shown in Table 1.
  • a PPG soft pack battery thickness gauge control a specific pressure, such as 400 grams to test the thickness of the lithium-ion battery when it is initially half-charged (half of the capacity when the battery is fully charged). At 45°C, when the charge-discharge cycle reaches 300 times, the lithium-ion battery is fully charged, and then the thickness of the lithium-ion battery is tested with a PPG soft pack battery thickness gauge, and compared with the thickness of the lithium-ion battery at the initial half charge , the expansion rate of the fully charged lithium-ion battery at this time can be obtained.
  • the base material of the isolation film is polyethylene (PE) with a thickness of 8 ⁇ m, and a 2 ⁇ m alumina ceramic layer is coated on both sides of the isolation film base material, and then 2.5 mg of adhesive is coated on both sides coated with the ceramic layer Polyvinylidene fluoride (PVDF), oven dry.
  • PE polyethylene
  • PVDF Polyvinylidene fluoride
  • LiPF 6 lithium hexafluorophosphate
  • PC propylene carbonate
  • PP polypropylene
  • DEC diethyl carbonate
  • the positive electrode sheet, the separator, and the negative electrode sheets prepared in each example and comparative example were stacked in order, so that the separator was placed between the positive and negative electrodes to play the role of isolation, and the electrode assembly was obtained by winding.
  • the electrode assembly is placed in the aluminum-plastic film of the outer packaging, and after dehydration at 80°C, the above-mentioned electrolyte is injected and packaged, and the lithium-ion battery is obtained through processes such as formation, degassing, and edge trimming.
  • Dissolve artificial graphite (Dv50 15 ⁇ m) as the negative active material, lithium carboxymethyl cellulose as the dispersant, and styrene-butadiene rubber as the binder in deionized water at a weight ratio of 98:1:1 to form a negative electrode slurry with a solid content of 70%. material.
  • Copper foil with a thickness of 10 ⁇ m is used as the negative electrode current collector, and the negative electrode slurry is coated on the negative electrode current collector with a coating thickness of 80 ⁇ m, and dried to obtain a negative electrode sheet coated on one side; after that, on the other side of the negative electrode sheet Repeat the above steps on one surface to obtain a negative electrode sheet coated with negative active materials on both sides.
  • the pole piece was cold pressed first, and then heated at 300° C. for 1 hour under nitrogen (N 2 ) atmosphere to obtain the treated negative pole piece.
  • Example 1 Except that the nitrogen atmosphere was adjusted to a vacuum atmosphere, and the vacuum degree was 5000 Pa, the rest was the same as that of Example 1.
  • the pole piece was placed in vacuum and treated with plasma, the plasma power was 2.5kW, the gas source was carbon tetrafluoride, the gas flow rate was 2000mL/min, the temperature was 30°C, and the treatment time was 30min.
  • the treated negative electrode sheet was obtained, and the rest were the same as in Example 1.
  • the pole piece was placed in vacuum and treated with plasma, the plasma power was 0.5kW, the gas source was argon, the gas flow rate was 200mL/min, the temperature was 20°C, and the treatment time was 60min.
  • the rest of the negative electrode sheet is the same as that of Example 1.
  • the pole piece was placed in vacuum and treated with plasma, the plasma power was 5kW, the gas source was nitrogen, the gas flow rate was 2000mL/min, the temperature was 60°C, and the treatment time was 5min.
  • the plasma power was 5kW
  • the gas source was nitrogen
  • the gas flow rate was 2000mL/min
  • the temperature was 60°C
  • the treatment time was 5min.
  • Negative pole piece, all the other are identical with embodiment 1.
  • the pole piece was placed within the working range of the laser transmitter in an N2 atmosphere, the laser intensity was 40W, the distance between the laser source and the pole piece was 7cm, and the treatment was performed for 500s to obtain the processed negative pole piece. All the other are identical with embodiment 1.
  • the TG and DTG curves of the negative electrode sheet obtained in Example 1 are shown in Figure 1, and the TG and DTG curves of the negative electrode sheet obtained in Example 7 are shown in Figure 2, and the peak heights of the first peaks of both are only around 400 °C Appear.
  • the TG and DTG curves of the negative electrode sheet obtained in Comparative Example 2 are shown in Figure 3, the peak height of the first peak appears in the range of 250°C to 350°C, and the peak height of the second peak is around 400°C.
  • Examples 1-12 and Comparative Examples 1-8 that after the specific modification treatment of the negative electrode sheet, its kinetic and electrochemical performances are significantly improved.
  • Examples 1-3, 6-12 Compared with Comparative Example 1, the active specific surface area of the negative electrode active material layer is increased by about 27%, the activation energy of the pole piece is reduced by about 27%, the polarization resistance is reduced by about 20%, the lithium separation window is increased by about 1C (multiplier), and the charging rate is improved. About 10%, the 300-cycle cycle capacity retention rate has no significant change with no heat treatment, indicating that the kinetic performance of the electrochemical device comprising the negative electrode sheet of the present application has been significantly improved, and the cycle performance has no obvious impact. It can also be seen from Examples 1-3 and 6-12 that the negative electrode sheet of the present application can be obtained by using different heating methods of the present application.
  • the active specific surface area of the negative electrode active material layer obtained is all lower than the negative electrode active material layer of the present application, so that its negative electrode
  • the kinetics and electrochemical properties of the sheet are lower than the negative electrode sheet of the present application.
  • Comparative Example 3 was heated in an air atmosphere, and Comparative Example 4 was heated in a nitrogen atmosphere at 400°C. After heating, the negative electrode sheet was seriously powdered, which could not meet the processing performance and could not be used to prepare lithium-ion batteries. , so it does not have the so-called "active specific surface area".
  • composition (weight ratio) of the negative electrode slurry in addition to adjusting the composition (weight ratio) of the negative electrode slurry to be 97.5% artificial graphite+1% carboxymethyl cellulose lithium+1% styrene-butadiene rubber+0.5% carbon nanotube (CNT, length 4 ⁇ m, pipe diameter 5nm) , all the other are identical with embodiment 1.
  • composition (weight ratio) of the negative electrode slurry In addition to adjusting the composition (weight ratio) of the negative electrode slurry to be 96.5% artificial graphite+1% carboxymethyl cellulose lithium+1% styrene-butadiene rubber+1.5% carbon nanotube (CNT, length 4 ⁇ m, pipe diameter 5 nm) , and the rest are identical with embodiment 18.
  • composition (weight ratio) of the negative electrode slurry In addition to adjusting the composition (weight ratio) of the negative electrode slurry to be 97% artificial graphite+1% carboxymethyl cellulose lithium+1% styrene-butadiene rubber+0.5% carbon nanotube (CNT, length 4 ⁇ m, pipe diameter 5nm) +0.5% carbon nanofibers (VGCF, about 10 ⁇ m in length and 10 nm in diameter), and the rest are the same as in Example 18.

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Abstract

一种负极极片及包含其的电化学装置和电子设备，其中，负极极片的DTG曲线首个峰的峰高对应的温度大于350℃；负极极片包括负极活性材料层，负极活性材料层包括负极活性材料，负极极片的活性比表面积大于或等于K·25cm 2/g，其中K为校正参数，K＝15μm/Dv50，其中Dv50为负极活性材料的中值粒径。

Description

一种负极极片及包含其的电化学装置和电子设备 技术领域
本申请涉及电化学技术领域，具体涉及一种负极极片及包含其的电化学装置和电子设备。
背景技术
锂离子电池作为一种高效移动式能源凭借其高电压、高比能量、长循环寿命的优势已经广泛应用于手机、笔记本电脑、数码相机等电子产品中。尤其随着近年来智能手机的快速普及，人们对于储能的锂离子电池的充电速率和能量密度要求越来越高。为了解决充电速率问题，通常对负极材料和负极配方进行调控来提升负极动力学，但是在对负极材料和配方进行调控时会带来一定的加工问题，而且对动力学的改善也比较有限。亟需寻找一种新的途径解决上述问题。
发明内容
本申请提供了一种负极极片，具有更好的动力学性能，以使应用其的电化学装置具有更快的充电速率。
本申请第一方面提供了一种负极极片，其热失重曲线(TG曲线)的微分曲线(DTG曲线)首个峰的峰高对应的温度大于350℃；所述负极极片包括负极活性材料层，所述负极活性材料层包括负极活性材料，所述负极活性材料层的活性比表面积大于或等于K·25cm 2/g，其中K为校正参数，K＝15μm/Dv50，Dv50为所述负极活性材料的中值粒径。
本申请的负极活性材料层的活性比表面积是指负极活性材料层的活性表面积与负极活性材料层的质量之比，可用于反映负极极片充放电时活性位点的多少，发明人发现，活性比表面积越大，析锂窗口越高，其充电的速度也越快。发明人在研究中发现，负极活性材料层的活性比表面积与负极活性材料层的微观结构以及负极活性材料的平均粒径相关，本申请的发明人通过校正参数，排除不同粒径对活性比表面积的影响，所得活性比表面积的数值更客观地反映了活性材料层的内部微观结构。本申请的负极活性材料层，具有更高的活性比表面积，说明本申请的负极极片的活性材料层具有与现有的负极活性材料层不同的微观结构。
发明人发现，本申请的负极极片通过热失重法(TG)分析，DTG曲线(TG的微分曲线)首个峰的峰高对应的温度大于350℃，此外，所述负极活性材料层具有更高的活性比表面积，发明人发现，所述负极极片具有更好的动力学性能，应用所述负极极片的电化学装 置具有更快的充电速率和更好的电化学性能。本申请中所说的“峰高”可以理解为首个峰的最大值。
本申请中，术语“Dv50”表示颗粒累积分布为50％的粒径，也叫中值粒径，即小于此粒径的颗粒体积含量占全部颗粒的50％。
本申请中，min代表分钟。
本申请中所述热失重曲线的微分曲线可以通过本领域的常规方法获得，示例性地，可以通过如下方法获得：将所述负极极片裁切为直径为14mm的小圆片，在氮气氛围下进行热失重分析测试，测试温度从25℃升温到600℃，升温速率为10℃/min，得到热失重曲线，对热失重曲线微分，得到热失重曲线的微分曲线。
在本申请的一些实施方式中，负极活性材料的平均粒径Dv50满足：100nm≤Dv50≤30μm。
本申请对负极活性材料的种类不做限定，例如可以采用现有作为锂离子电池负极活性材料的各种成分，例如包含石墨的石墨系负极材料，包含硅碳、硅氧化物中的至少一种的硅材料作为负极材料，或者采用例如树脂碳、有机聚合物热解碳、炭黑等硬碳系负极材料，以及不同上述类型的负极材料通过一定比例混合后的复合负极材料。发明人发现，不同负极材料的粒径范围不同，例如，硅系负极材料的Dv50通常为100nm至20μm；石墨系负极材料的Dv50通常为10μm至30μm；但是发明人发现，当采用不同负极活性材料时，经过本申请特定方法(下文中将详述)处理后获得的负极极片，相比于现有方法获得的负极极片，其负极活性材料层均具有更大的活性比表面积。
在本申请的一些实施方式中，所述负极活性材料层还包含长程纤维。本申请中的长程纤维包括一些长程导电碳或长程陶瓷纤维或长程聚合物纤维等。其中长程导电碳是指具有一维结构的导电碳材料，例如碳纳米管和纳米碳纤维中的至少一种。发明人发现，所述长程纤维因为具有纤维状结构，增大了与负极活性材料颗粒的接触，能够显著提升极片的内聚力，对于制成锂离子电池在循环过程中的极片膨胀具有良好的抑制作用，避免锂离子电池在循环使用过程中的体积能量密度的损失。更出人意料的是，发明人还发现长程纤维的引入虽然能够改善锂离子电池膨胀，但是却造成了电芯动力学性能的恶化，例如析锂窗口下降；而当将加入长程纤维的负极极片采用本申请的方法进行热处理后，获得的负极极片可以在保证锂离子电池动力学性能的前提下，实现电芯的循环膨胀性能改性，兼顾了可靠性和快充性能。
在本申请的一些实施方式中，所述长程纤维的长度大于1μm，优选地，长程纤维的长 度为1μm至1mm；优选1μm至50μm；发明人发现，进一步增加长程纤维的长度并不会带来额外的优势。另外，本申请对长程纤维的直径不做限定，例如可以是1至200nm。
在本申请的一些实施方式中，基于所述负极活性材料层的总质量，所述长程纤维的质量含量为0.2％至1.5％。不限于任何理论，发明人发现，当长程纤维的含量过低时(例如低于0.2％)，不能起到缓解负极膨胀的作用；当长程导电碳的含量过高时(例如高于1.5％)，不仅会使负极极片中活性材料的相对含量降低，影响锂离子电池的能量密度，而且对于负极极片的动力学性能存在较大的影响。
更出人意料的是，发明人还发现，本申请的负极极片，其负极活性材料层的活性比表面积增大并不会带来SEI(Solid Electrolyte Interphase，固体电解质界面)膜增厚的问题，更重要的是，本申请的负极活性材料层的电化学反应能垒降低，使负极极片具有更低的活化能。在本申请的一些实施方式中，所述负极极片的电化学反应活化能Ea满足：25kJ/mol≤Ea≤55kJ/mol。发明人发现，当所述负极活性材料不含硅时，所述负极极片具有更低的电化学反应活化能，其Ea满足：25kJ/mol≤Ea≤37kJ/mol，本申请的负极极片相比于现有的负极极片活化能更低，从而更有利于锂离子电池动力学性能的提升。
在本申请的一些实施方式中，所述负极活性材料层还包括导电剂，本申请对所述导电剂的种类不做限定，例如可以包括导电炭黑、导电石墨、石墨烯和乙炔黑中的至少一种；通过导电剂的加入，能够提升负极的导电性能。本申请对负极活性材料层中导电剂的含量没有特别限制，只要能够实现本申请目的即可，例如导电剂占负极活性材料层总质量的0％至1％。
在本申请的一些实施方式中，所述负极活性材料层还包括粘结剂，本申请对粘结剂的种类不做限定，例如所述粘结剂可以包括聚偏二氟乙烯、偏氟乙烯-氟化烯烃的共聚物、聚乙烯吡咯烷酮、聚丙烯腈、聚丙烯酸甲酯、聚四氟乙烯、丁苯橡胶、聚胺酯、氟化橡胶和聚乙烯醇中的至少一种；粘结剂的加入能够提高负极活性材料层的粘性，减少负极活性材料层中的负极活性材料、导电剂脱落的可能性，也可以降低负极活性材料层从集流体上脱落的可能性。本申请对负极活性材料层中粘结剂的含量没有特别限制，只要能够实现本申请目的即可，例如粘结剂占负极活性材料层总质量的0.5％至10％。
本申请的负极极片可以是通过将负极活性材料层设置于负极集流体上制成，集流体没有特别限制，可以使用本领域公知的负极集流体，例如铜箔、铝箔、铝合金箔以及复合集流体等。在本申请中，负极集流体和负极活性材料层的厚度没有特别限制，只要能够实现本申请目的即可。例如，负极集流体的厚度为6μm至10μm，负极活性材料层的厚度为30μm 至120μm。
本申请第二方面提供了本申请第一方面的负极极片的制备方法，其包括：
将负极活性材料层的浆料涂布于负极集流体的至少一个表面，烘干，形成初始极片；
将所述初始极片进行改性处理，获得所述负极极片；
其中，所述改性处理包括等离子体处理、加热处理和激光处理的至少一种。
具体地，在本申请的一些实施方式中，所述的等离子体处理可以为：所述初始极片在真空环境下采用等离子体处理，等离子体处理的功率范围为0.5k至5kW，气源包括氮气、氩气和四氟化碳中的至少一种，气体流量范围为200mL/min至3000mL/min，温度范围为20℃至60℃，处理时间1min至60min；
在本申请的一些实施方式中，所述的加热处理可以为：将所述初始极片置于真空或惰性气体环境下，200℃至350℃的温度范围内，加热处理1min至60min；本申请对加热方式不做限定，只要能够实现本申请的目的即可，例如可以采用鼓风加热、红外加热、微波加热、电磁感应加热等；
在本申请的一些实施方式中，所述的激光处理可以为：将所述初始极片在真空或惰性气体环境下，激光强度在30W至100W的条件下，处理1s至600s；具体地，可以在真空或惰性气体环境下，将所述初始极片置于激光发射器工作范围内，激光强度30W至100W，激光源与初始极片间距3cm至10cm，处理1s至600s。
本申请中，初始极片的制备可采用本领域的常规方法，对于负极活性材料层的成分和含量可以采用上述对负极极片的说明，发明人发现，将初始极片经过特定条件下的改性处理后，即可获得本申请所述的负极极片。
本申请第三方面提供了一种电化学装置，其包括本申请第一方面所述的负极极片；而其它的组成部分，包括正极极片、隔膜及电解液等，没有特别的限制，只要能够实现本申请目的即可。
例如，正极极片通常包含正极集流体和正极活性材料层。其中，正极集流体没有特别限制，可以为本领域公知的正极集流体，例如铜箔、铝箔、铝合金箔以及复合集流体等。正极活性材料层包括正极活性材料，正极活性材料没有特别限制，可以为本领域公知的正极活性材料，例如，包括镍钴锰酸锂(811、622、523、111)、镍钴铝酸锂、磷酸铁锂、富锂锰基材料、钴酸锂、锰酸锂、磷酸锰铁锂或钛酸锂中的至少一种。在本申请中，正极集流体和正极活性材料层的厚度没有特别限制，只要能够实现本申请目的即可。例如，正极集流体的厚度为8μm至12μm，正极活性材料层的厚度为30μm至120μm。
任选地，正极极片还可以包含导电层，该导电层位于正极集流体和正极活性材料层之间。导电层的组成没有特别限制，可以是本领域常用的导电层。该导电层包括导电剂和粘结剂。所述导电剂没有特别限制，可以是本领域技术人员公知的任何导电剂或其组合，例如，可以采用零维导电剂、一维导电剂及二维导电剂中的至少一种。优选地，导电剂可以包括炭黑、导电石墨、碳纤维、碳纳米管、VGCF(气相法生长纳米碳纤维)或石墨烯中的至少一种。导电剂的用量没有特别限制，可以根据本领域公知常识进行选择。上述导电剂可以单独使用一种，也可以将两种以上以任意比例组合使用。
所述导电层中的粘结剂没有特别限制，可以是本领域技术人员公知的任何粘结剂或其组合，例如可以使用聚丙烯酸酯、聚酰亚胺、聚酰胺、聚酰胺酰亚胺、聚偏氟乙烯、丁苯橡胶、海藻酸钠、聚乙烯醇、聚四氟乙烯、聚丙烯腈、羧甲基纤维素钠、羧甲基纤维素锂等的至少一种。这些粘结剂可以单独使用一种，也可以将两种以上以任意比例组合使用。
本申请的电化学装置还包括隔离膜，用以分隔正极和负极，防止电化学装置内部短路，允许电解质离子自由通过，完成电化学充放电过程的作用。在本申请中，隔离膜没有特别限制，只要能够实现本申请目的即可。
例如，聚乙烯(PE)、聚丙烯(PP)为主的聚烯烃(PO)类隔离膜，聚酯膜(例如聚对苯二甲酸二乙酯(PET)膜)、纤维素膜、聚酰亚胺膜(PI)、聚酰胺膜(PA)，氨纶或芳纶膜、织造膜、非织造膜(无纺布)、微孔膜、复合膜、隔膜纸、碾压膜、纺丝膜等中的至少一种。
例如，隔离膜可以包括基材层和表面处理层。基材层可以为具有多孔结构的无纺布、膜或复合膜，基材层的材料可以包括聚乙烯、聚丙烯、聚对苯二甲酸乙二醇酯和聚酰亚胺等中的至少一种。任选地，可以使用聚丙烯多孔膜、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。任选地，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。
例如，无机物层包括无机颗粒和粘结剂，该无机颗粒没有特别限制，例如可以选自氧化铝、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、氢氧化钙和硫酸钡等中的至少一种。粘结剂没有特别限制，例如可以选自聚偏氟乙烯、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、聚乙烯醚、聚甲基丙烯酸甲酯、聚四氟乙烯和聚六氟丙烯中的一种或几种的组合。聚合物层中包含聚 合物，聚合物的材料包括聚酰胺、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、聚乙烯醚、聚偏氟乙烯或聚(偏氟乙烯-六氟丙烯)等中的至少一种。
本申请的电化学装置还包括电解质，电解质可以是凝胶电解质、固态电解质和电解液中的一种或多种，电解液包括锂盐和非水溶剂。
在本申请第一方面的一些实施方式中，锂盐选自六氟磷酸锂(LiPF 6)、四氟硼酸锂(LiBF 4)、六氟砷酸锂(LiAsF 6)、高氯酸锂(LiClO 4)、四苯硼锂(LiB(C 6H 5) 4)、甲基磺酸锂(LiCH 3SO 3)、三氟甲磺酸锂(LiCF 3SO 3)、双三氟甲烷磺酰亚胺锂(LiN(SO 2CF 3) 2)、LiC(SO 2CF 3) 3、六氟硅酸锂(LiSiF 6)、双草酸硼酸锂(LiBOB)和二氟硼酸锂(LiF 2OB)中的一种或多种。举例来说，锂盐可以选用LiPF 6，因为它具有高的离子导电率并改善循环特性。
非水溶剂可为碳酸酯化合物、羧酸酯化合物、醚化合物、其它有机溶剂或它们的组合。
上述碳酸酯化合物可为链状碳酸酯化合物、环状碳酸酯化合物、氟代碳酸酯化合物或其组合。
上述链状碳酸酯化合物的实例为碳酸二甲酯(DMC)、碳酸二乙酯(DEC)、碳酸二丙酯(DPC)、碳酸甲丙酯(MPC)、碳酸乙丙酯(EPC)、碳酸甲乙酯(EMC)及其组合。环状碳酸酯化合物的实例为碳酸亚乙酯(EC)、碳酸亚丙酯(PC)、碳酸亚丁酯(BC)、碳酸乙烯基亚乙酯(VEC)及其组合。氟代碳酸酯化合物的实例为碳酸氟代亚乙酯(FEC)、碳酸1,2-二氟亚乙酯、碳酸1,1-二氟亚乙酯、碳酸1,1,2-三氟亚乙酯、碳酸1,1,2,2-四氟亚乙酯、碳酸1-氟-2-甲基亚乙酯、碳酸1-氟-1-甲基亚乙酯、碳酸1,2-二氟-1-甲基亚乙酯、碳酸1,1,2-三氟-2-甲基亚乙酯、碳酸三氟甲基亚乙酯及其组合。
上述羧酸酯化合物的实例为甲酸甲酯、乙酸甲酯、乙酸乙酯、乙酸正丙酯、乙酸叔丁酯、丙酸甲酯、丙酸乙酯、丙酸丙酯、γ-丁内酯、癸内酯、戊内酯、甲瓦龙酸内酯、己内酯及其组合。
上述醚化合物的实例为二丁醚、四甘醇二甲醚、二甘醇二甲醚、1,2-二甲氧基乙烷、1,2-二乙氧基乙烷、乙氧基甲氧基乙烷、2-甲基四氢呋喃、四氢呋喃及其组合。
上述其它有机溶剂的实例为二甲亚砜、1,2-二氧戊环、环丁砜、甲基环丁砜、1,3-二甲基-2-咪唑烷酮、N-甲基-2-吡咯烷酮、甲酰胺、二甲基甲酰胺、乙腈、磷酸三甲酯、磷酸三乙酯、磷酸三辛酯、和磷酸酯及其组合。
电化学装置的制备过程为本领域技术人员所熟知的，本申请没有特别的限制。例如电化学装置可以通过以下过程制造：将正极和负极经由隔离膜重叠，并根据需要将其卷绕、 折叠等操作后放入壳体内，将电解液注入壳体并封口。此外，也可以根据需要将防过电流元件、导板等置于壳体中，从而防止电化学装置内部的压力上升、过充放电。
本申请第四方面提供了一种电子设备，其包含本申请第三方面所提供的电化学装置。
本申请的电子设备没有特别限定，其可以是用于现有技术中已知的任何电子设备。在一些实施例中，电子设备可以包括但不限于，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、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。
本申请提供的电化学装置及电子设备，其中的负极极片的DTG曲线首个峰的峰高对应的温度大于350℃；且所述负极活性材料层的活性比表面积大于或等于K·25cm 2/g，应用本申请负极极片的电化学装置具有更好地动力学性能，析锂窗口增大，充电速率更快。
附图说明
为了更清楚地说明本发明实施例和现有技术的技术方案，下面对实施例和现有技术中所需要使用的附图作简单地介绍，显而易见地，下面描述中的附图仅仅是本申请的一种实施方式，对于本领域普通技术人员来讲，还可以根据这些附图获得其他的实施方式。
图1为实施例1的负极极片的TG曲线和DTG曲线。
图2为实施例7的负极极片的TG曲线和DTG曲线。
图3为对比例2的负极极片的TG曲线和DTG曲线。
具体实施方式
为使本申请的目的、技术方案、及优点更加清楚明白，以下参照附图和实施例，对本申请进一步详细说明。显然，所描述的实施例仅仅是本申请一部分实施例，而不是全部的实施例。基于本申请中的实施例，本领域普通技术人员所获得的所有其他技术方案，都属于本申请保护的范围。
需要说明的是，本申请的具体实施方式中，以锂离子电池作为电化学装置的例子来解释本申请，但是本申请的电化学装置并不仅限于锂离子电池。
测试方法：
TG测试：
取各实施例和对比例的负极极片，裁切为直径D＝14mm的小圆片，在氮气氛围下进行TG测试，测试温度从25℃升温到600℃，温升速率为10℃/min。得到的TG曲线，进行TG曲线的微分，得到DTG曲线，可以明确负极极片的失重峰值温度及失重速率。
活性比表面积测试：
将各实施例和对比例的负极极片在干燥环境中用冲压机切成直径为1.4cm的圆片，并记录质量为m。在手套箱中以金属锂片作为对电极，隔离膜选择ceglard复合膜，加入电解液组装成扣式电池；其中，电解液中含有浓度为c的电化学氧化还原探针分子二茂铁。
利用电化学工作站在不同扫速v下进行测试得到一系列循环伏安曲线，并从循环伏安曲线中得到峰电流Ip；将得到的一系列峰电流Ip和扫速v的平方根做图，得到斜率K；根据Randles-Sevick方程，极片的活性表面积
Figure PCTCN2021130699-appb-000001
其中n表示电极反应的电子转移数，本测试体系中为1；c表示探针分子的浓度；D表示探针分子的扩散系数，本体系中，二茂铁扩散系数为2.1×10 -6cm 2/s；极片的活性表面积A与极片活性材料层的质量(m-集流体的质量)的比值即为活性材料层的活性比表面积。
活化能测试：
取各实施例和对比例制备的负极极片各两片，在中间加入隔离膜，密封后注入电解液，得到对称电池。在不同的温度下测试对称电池的电化学阻抗谱(EIS)，得到电池的Rct(电化学反应阻抗)，根据Arrhenius公式计算活化能。
极化阻抗测试：
将各实施例和对比例的负极极片和相同的正极极片分别组装成锂离子电池，安装于充放电设备上进行充放电，并监测锂离子电池的电压与电流，得到锂离子电池的直流阻抗值。具体地，以0.5C的电流将锂离子电池恒流充电至满充电压，再恒压充电至0.05C。再以1C电流放电30min使锂离子电池处于50％的荷电比状态，静置60min。以0.1C的电流放电10s，并记录电压V1。再以1C的电流放电1s，并记录电压V2。按如下公式计算得出锂离子电池的极化阻抗1s DCR：
1s DCR＝(V1-V2)/(1C-0.1C)
充电速率测试：
将各实施例和对比例的负极极片分别组装成锂离子电池，在25℃环境中静置30分钟，以0.5C倍率恒流充电至额定电压，随后以恒压充电直到充放电倍率达到0.05C时停止充电。计时开始充电的时刻到停止充电的时刻之间的时间为满充时间。
析锂窗口测试：
先把电化学装置放电至满放状态，然后设定特定温度(例如，25℃)，根据电化学装置设计以不同的倍率，如1C、1.1C、1.2C…进行常规充电(恒流+恒压)，即特定倍率下充电至电池额定电压，之后恒压充电至0.05C停止充电，充电后0.2C满放，对上述充放电流程循环10个周期。最后对电化学装置满充后进行拆解，观察负极极片是否析锂，在不析锂(负极极片表面不存在白斑)的情况下的最大电流定义为该电池的最大不析锂倍率，也就是析锂窗口。
循环性能测试：
将各实施例和对比例制备的负极极片组装为全电池，测试温度为45℃，以0.5C恒流充电到额定电压，恒压充电到0.025C，静置5分钟后以0.5C放电到3.0V。以此步骤得到的容量为初始容量，进行0.5C充电/0.5C放电进行循环测试，以每一步的容量与初始容量做比值，得到容量衰减曲线；各实施例和对比例循环300次后的容量保持率如表1所示。
满充膨胀率测试：
用PPG软包电池测厚仪(控制特定压力，如400克)测试初始半充(充电至电池满充状态时容量的一半)时锂离子电池的厚度。45℃下，充放电循环至300次时，锂离子电池于满充状态下，再用PPG软包电池测厚仪测试此时锂离子电池的厚度，与初始半充时锂离子电池的厚度对比，即可得此时满充锂离子电池的膨胀率。
全电池制备：
正极极片制备：
将正极活性材料钴酸锂、导电剂导电炭黑、粘结剂聚偏氟乙烯(PVDF)按重量比97.6︰1.1︰1.3的比例溶于N-甲基吡咯烷酮(NMP)溶液中，调配成固含量为75％的正极浆料；采用10μm厚的铝箔作为正极集流体，将正极浆料涂覆于正极集流体上，涂布厚度为50μm，经过干燥得到单面涂布的正极极片；之后，在该正极极片的另一个表面上重复以上步骤，即得到双面涂布正极活性材料的正极极片。
隔离膜制备：
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，然后在涂布了陶瓷层的两侧各涂覆2.5mg的粘结剂聚偏氟乙烯(PVDF)，烘干。
电解液制备：
在含水量小于10ppm的环境下，将六氟磷酸锂(LiPF 6)与非水有机溶剂按照碳酸乙烯酯(EC)︰碳酸丙烯酯(PC)︰聚丙烯(PP)︰二乙基碳酸酯(DEC)＝1︰1︰1︰1的重量比配制成电解液，其中，LiPF 6的浓度为1.15mol/L。
全电池组装：
将正极极片、隔离膜、各实施例和对比例制备的负极极片按顺序叠好，使隔离膜处于正负极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。
负极极片的制备：
实施例1
将负极活性材料人造石墨(Dv50＝15μm)、分散剂羧甲基纤维素锂和粘结剂丁苯橡胶按照重量比98︰1︰1溶于去离子水中，形成固含量为70％的负极浆料。采用10μm厚度的铜箔作为负极集流体，将负极浆料涂覆于负极集流体上，涂布厚度为80μm，干燥，得到单面涂布的负极极片；之后，在该负极极片的另一个表面上重复以上步骤，即得到双面涂布负极活性材料的负极极片。极片先通过冷压，随后在氮气(N 2)氛围下，300℃加热1h后得到处理后的负极极片。
实施例2
除了加热温度调整为200℃，其余与实施例1相同。
实施例3
除了加热温度调整为350℃，其余与实施例1相同。
实施例4
除了人造石墨Dv50为20μm，其余与实施例1相同。
实施例5
除了人造石墨Dv50为25μm，其余与实施例1相同。
实施例6
除了将氮气氛围调整为真空氛围，真空度为5000Pa，其余与实施例1相同。
实施例7
除了极片冷压后，将所述极片置于真空中，采用等离子体处理，等离子体功率2.5kW，气源为四氟化碳，气体流量2000mL/min，温度30℃，处理时间30min，得到处理后的负极极片，其余与实施例1相同。
实施例8
除了极片冷压后，将所述极片置于真空中，采用等离子体处理，等离子体功率0.5kW，气源为氩气，气体流量200mL/min，温度20℃，处理时间60min，得到处理后的负极极片， 其余与实施例1相同。
实施例9
除了极片冷压后，将所述极片置于真空中，采用等离子体处理，等离子体功率5kW，气源为氮气，气体流量2000mL/min，温度60℃，处理时间5min，得到处理后的负极极片，其余与实施例1相同。
实施例10
除了极片冷压后，在N 2氛围中，将所述极片置于激光发射器工作范围内，激光强度40W，激光源与极片间距7cm，处理500s，得到处理后的负极极片，其余与实施例1相同。
实施例11
除了调整激光强度80W，处理100s，其余与实施例10相同。
实施例12
除了调整激光强度100W，处理20s，其余与实施例10相同。
实施例13
除负极活性材料(人造石墨)的Dv50由15μm调整为10μm，其余与实施例1相同。
实施例14
除负极活性材料(人造石墨)的Dv50由15μm调整为30μm，其余与实施例1相同。
实施例15
除调整负极浆料的组成(重量比)为88％的硅氧(Dv50＝10μm，G1S-C450)+2％的羧甲基纤维素锂+10％的丁苯橡胶，其余与实施例1相同。
实施例16
除负极活性材料由人造石墨调整为硬碳(Dv50＝10μm，MS-BHC-400)，其余与实施例1相同。
实施例17
除调整负极浆料的组成(重量比)为89.4％的硅碳材料(Dv50＝10μm，SN-SC2)+1％的羧甲基纤维素锂+9.6％的丁苯橡胶，其余与实施例1相同。
对比例1
除负极极片冷压后不经过加热处理，直接得到负极极片，其余与实施例1相同。
对比例2
除负极极片加热温度调整为150℃，其余与实施例1相同。
对比例3
除将氮气氛围替换为空气氛围，其余与实施例1相同。
对比例4
除负极极片加热温度调整为400℃，其余与实施例1相同。
对比例5
除负极极片冷压后不经过加热处理，直接得到负极极片，其余与实施例13相同。
对比例6
除负极极片冷压后不经过加热处理，直接得到负极极片，其余与实施例15相同。
对比例7
除负极极片冷压后不经过加热处理，直接得到负极极片，其余与实施例16相同。
对比例8
除负极极片冷压后不经过加热处理，直接得到负极极片，其余与实施例17相同。
实施例1所得负极极片的TG和DTG曲线如图1所示，实施例7所得负极极片的TG和DTG曲线如图2所示，两者首个峰的峰高均只在400℃左右出现。对比例2所得负极极片的TG和DTG曲线如图3所示，其首个峰的峰高在250℃至350℃范围内出现，且其第二个峰的峰高在400℃左右。
Figure PCTCN2021130699-appb-000002
Figure PCTCN2021130699-appb-000003
Figure PCTCN2021130699-appb-000004
通过实施例1-12与对比例1-8相比可以看出，负极极片经过特定改性处理后，其动力学及电化学性能均显著提高，其中，实施例1-3、6-12与对比例1相比，负极活性材料层的活性比表面积提高约27％，极片活化能降低约27％，极化阻抗降低约20％，析锂窗口提升约1C(倍率)，充电速率提升约10％，300圈循环容量保持率与不经热处理没有明显变化，说明包含本申请的负极极片的电化学装置动力学性能得到明显提高，对循环性能没有明显影响。从实施例1-3、6-12中还可以看出，采用本申请的不同加热方法，均能够获得本申请的负极极片。
而不进行改性处理，或改性处理条件与本申请不同(例如对比例1-8)，获得的负极活性材料层的活性比表面积均低于本申请的负极活性材料层，以致其负极极片的动力学和电化学性能均低于本申请的负极极片。由此说明，当采用本申请的方法对负极极片进行改性处理后，负极极片的动力学和电化学性能得到显著提升，不限于任何理论，发明人认为这可能是由于极片热处理后，其活性材料层的活性比表面积增大，露出了更多的活性位点。
发明人还发现，对比例3在空气氛围中加热，对比例4在氮气氛围中，400℃下加热，加热后得到的负极极片掉粉严重，无法满足加工性能，不能用于制备锂离子电池，因此其也不具备所说的“活性比表面积”。
实施例13-17与对比例5-8比较可以看出，采用本申请的方法处理具有不同粒径的、相同或不同种类的负极活性材料制备的负极极片，其活性材料层均能够获得具有更高活性比表面积，且得到的负极极片的动力学性能和电化学性能更好。对于不同的负极活性材料而言，相比不进行改性处理的负极极片，改性处理后，负极极片的动力学及电化学性能获得显著提高。
实施例18
除调整负极浆料的组成(重量比)为97.5％的人造石墨+1％的羧甲基纤维素锂+1％的丁苯橡胶+0.5％碳纳米管(CNT，长度4μm，管径5nm)，其余与实施例1相同。
实施例19
材料将CNT替换为纳米碳纤维(VGCF，长度约10μm，直径10nm)，其余与实施例18相同。
实施例20
除调整负极浆料的组成(重量比)为96.5％的人造石墨+1％的羧甲基纤维素锂+1％的丁苯橡胶+1.5％碳纳米管(CNT，长度4μm，管径5nm)，其余与实施例18相同。
实施例21
除调整负极浆料的组成(重量比)为97％的人造石墨+1％的羧甲基纤维素锂+1％的丁苯橡胶+0.5％碳纳米管(CNT，长度4μm，管径5nm)+0.5％纳米碳纤维(VGCF，长度约10μm，直径10nm)，其余与实施例18相同。
实施例22
材料将CNT替换为长程陶瓷纤维(长度约20μm，直径10nm)，其余与实施例18相同。
实施例23
材料将CNT替换为长程芳纶纤维(长度约30μm，直径10nm)，其余与实施例18相同。
对比例9
除负极极片冷压后不经过加热处理，直接得到负极极片，其余与实施例18相同。
对比例10
除负极极片冷压后不经过加热处理，直接得到负极极片，其余与实施例19相同。
对比例11
除负极极片冷压后不经过加热处理，直接得到负极极片，其余与实施例20相同。
对比例12
除负极极片冷压后不经过加热处理，直接得到负极极片，其余与实施例21相同。
对比例13
除负极极片冷压后不经过加热处理，直接得到负极极片，其余与实施例22相同。
对比例14
除负极极片冷压后不经过加热处理，直接得到负极极片，其余与实施例23相同。
Figure PCTCN2021130699-appb-000005
Figure PCTCN2021130699-appb-000006
实施例1、18-23中可以看出，加入长程纤维后，其膨胀性能得到改善，根据与对比例9-14的比较可以看出，加之以热处理，可使负极极片获得更高的动力学性能，从而实现了缓解膨胀和提高动力学性能的双重改性。
另外，发明人发现，不同活性材料的种类对锂离子电池的动力学及电化学性能会产生不同影响，本申请在讨论动力学及电化学性能时，均采用相同材料进行比较。
以上所述仅为本发明的较佳实施例而已，并不用以限制本发明，凡在本发明的精神和原则之内，所做的任何修改、等同替换、改进等，均应包含在本发明保护的范围之内。

Claims (17)

  1. 一种负极极片，其热失重曲线的微分曲线首个峰的峰高对应的温度大于350℃；所述负极极片包括负极活性材料层，所述负极活性材料层包括负极活性材料，所述负极活性材料层的活性比表面积大于或等于K·25cm 2/g，其中K为校正参数，K＝15μm/Dv50，其中Dv50为所述负极活性材料的中值粒径。
  2. 根据权利要求1所述的负极极片，其中，所述热失重曲线的微分曲线通过如下方法获得：将所述负极极片裁切为直径为14mm的小圆片，在氮气氛围下进行热失重分析测试，测试温度从25℃升温到600℃，升温速率为10℃/min，得到热失重曲线，对热失重曲线微分，得到热失重曲线的微分曲线。
  3. 根据权利要求1所述的负极极片，其中，100nm≤Dv50≤30μm。
  4. 根据权利要求1所述的负极极片，其中，所述负极活性材料包括石墨、硬碳、或者硅材料中的至少一种。
  5. 根据权利要求1所述的负极极片，其中，所述负极活性材料层还包含长程纤维，所述长程纤维包括长程陶瓷纤维、长程聚合物纤维或者长程导电碳中的一种。
  6. 根据权利要求5所述的负极极片，其中，所述长程导电碳包括碳纳米管和纳米碳纤维中的至少一种。
  7. 根据权利要求5所述的负极极片，其中，所述长程纤维的长度为1μm至1mm。
  8. 根据权利要求5所述的负极极片，其中，基于所述负极活性材料层的总质量，所述长程纤维的质量百分含量为0.2％至1.5％。
  9. 根据权利要求1所述的负极极片，其中，所述负极活性材料层还包括导电剂，所述导电剂包括导电炭黑、导电石墨、石墨烯和乙炔黑中的至少一种。
  10. 根据权利要求1所述的负极极片，其中，所述负极活性材料层还包含粘结剂，所述粘结剂包括聚偏二氟乙烯、偏氟乙烯-氟化烯烃的共聚物、聚乙烯吡咯烷酮、聚丙烯腈、聚丙烯酸甲酯、聚四氟乙烯、丁苯橡胶、聚胺酯、氟化橡胶和聚乙烯醇中的至少一种。
  11. 根据权利要求1所述的负极极片，其中，所述负极极片的电化学反应活化能Ea满足：kJ/mol 25≤Ea≤55 kJ/mol。
  12. 一种电化学装置，其包括权利要求1-11中任一项所述的负极极片。
  13. 一种电子设备，其包括权利要求12所述的电化学装置。
  14. 一种负极极片的制备方法，其包括：
    将负极活性材料层的浆料涂布于负极集流体的至少一个表面，干燥，冷压，形成初始极片；
    将所述初始极片进行改性处理，获得所述负极极片；
    所述改性处理包括等离子体处理、加热处理和激光处理中的至少一种。
  15. 根据权利要求14所述的一种负极极片的制备方法，其中，所述等离子体处理为：将所述初始极片在真空环境下采用等离子体处理，等离子体处理的功率范围为0.5kW至5kW，气源包括氮气、氩气和四氟化碳中的至少一种，气体流量的范围为200mL/min至3000mL/min，温度范围为20℃至60℃，处理时间的范围为1min至60min。
  16. 根据权利要求14所述的一种负极极片的制备方法，其中，所述加热处理为将所述初始极片置于真空或惰性气体环境下，在200℃至350℃的温度范围内加热处理1min至60min。
  17. 根据权利要求14所述的一种负极极片的制备方法，其特征在于，所述激光处理为将所述初始极片在真空或惰性气体环境下，激光强度在30W至100W的条件下，处理1s至600s。
PCT/CN2021/130699 2021-11-15 2021-11-15 一种负极极片及包含其的电化学装置和电子设备 WO2023082264A1 (zh)

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