WO2023004633A1 - 一种电池、电池模块、电池包和用电装置 - Google Patents

一种电池、电池模块、电池包和用电装置 Download PDF

Info

Publication number
WO2023004633A1
WO2023004633A1 PCT/CN2021/108971 CN2021108971W WO2023004633A1 WO 2023004633 A1 WO2023004633 A1 WO 2023004633A1 CN 2021108971 W CN2021108971 W CN 2021108971W WO 2023004633 A1 WO2023004633 A1 WO 2023004633A1
Authority
WO
WIPO (PCT)
Prior art keywords
coating
negative electrode
polar substance
positive electrode
battery
Prior art date
Application number
PCT/CN2021/108971
Other languages
English (en)
French (fr)
Inventor
黄玉平
林明峰
马云建
喻鸿钢
李彦辉
张建平
代宇
沈仡东
Original Assignee
宁德时代新能源科技股份有限公司
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 宁德时代新能源科技股份有限公司 filed Critical 宁德时代新能源科技股份有限公司
Priority to PCT/CN2021/108971 priority Critical patent/WO2023004633A1/zh
Priority to CN202180071500.2A priority patent/CN116349077A/zh
Priority to KR1020227029101A priority patent/KR20230019406A/ko
Priority to EP21927065.9A priority patent/EP4148891A4/en
Priority to JP2022550822A priority patent/JP7432753B2/ja
Priority to US17/937,768 priority patent/US20230117614A1/en
Publication of WO2023004633A1 publication Critical patent/WO2023004633A1/zh

Links

Images

Classifications

    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/46—Separators, membranes or diaphragms characterised by their combination with electrodes
    • H01M50/461—Separators, membranes or diaphragms characterised by their combination with electrodes with adhesive layers between electrodes and separators
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/409—Separators, membranes or diaphragms characterised by the material
    • H01M50/411—Organic material
    • H01M50/414—Synthetic resins, e.g. thermoplastics or thermosetting resins
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00—Secondary cells; Manufacture thereof
    • H01M10/05—Accumulators with non-aqueous electrolyte
    • H01M10/052—Li-accumulators
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00—Secondary cells; Manufacture thereof
    • H01M10/05—Accumulators with non-aqueous electrolyte
    • H01M10/052—Li-accumulators
    • H01M10/0525—Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00—Secondary cells; Manufacture thereof
    • H01M10/05—Accumulators with non-aqueous electrolyte
    • H01M10/058—Construction or manufacture
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00—Secondary cells; Manufacture thereof
    • H01M10/05—Accumulators with non-aqueous electrolyte
    • H01M10/058—Construction or manufacture
    • H01M10/0585—Construction or manufacture of accumulators having only flat construction elements, i.e. flat positive electrodes, flat negative electrodes and flat separators
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/04—Processes of manufacture in general
    • H01M4/0402—Methods of deposition of the material
    • H01M4/0404—Methods of deposition of the material by coating on electrode collectors
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • 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
    • H01M4/133—Electrodes based on carbonaceous material, e.g. graphite-intercalation compounds or CFx
    • 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
    • H01M4/134—Electrodes based on metals, Si or alloys
    • 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
    • H01M4/36—Selection of substances as active materials, active masses, active liquids
    • H01M4/362—Composites
    • H01M4/364—Composites as mixtures
    • 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
    • H01M4/36—Selection of substances as active materials, active masses, active liquids
    • H01M4/362—Composites
    • H01M4/366—Composites as layered products
    • 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
    • H01M4/36—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
    • 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
    • H01M4/36—Selection of substances as active materials, active masses, active liquids
    • H01M4/48—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
    • H01M4/50—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of manganese
    • H01M4/505—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of manganese of mixed oxides or hydroxides containing manganese for inserting or intercalating light metals, e.g. LiMn2O4 or LiMn2OxFy
    • 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
    • H01M4/36—Selection of substances as active materials, active masses, active liquids
    • H01M4/48—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
    • H01M4/52—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of nickel, cobalt or iron
    • H01M4/525—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of nickel, cobalt or iron of mixed oxides or hydroxides containing iron, cobalt or nickel for inserting or intercalating light metals, e.g. LiNiO2, LiCoO2 or LiCoOxFy
    • 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
    • H01M4/36—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
    • 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
    • H01M4/36—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
    • 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
    • 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
    • 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
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/20—Mountings; Secondary casings or frames; Racks, modules or packs; Suspension devices; Shock absorbers; Transport or carrying devices; Holders
    • H01M50/204—Racks, modules or packs for multiple batteries or multiple cells
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/403—Manufacturing processes of separators, membranes or diaphragms
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/409—Separators, membranes or diaphragms characterised by the material
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/409—Separators, membranes or diaphragms characterised by the material
    • H01M50/411—Organic material
    • H01M50/414—Synthetic resins, e.g. thermoplastics or thermosetting resins
    • H01M50/417—Polyolefins
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/409—Separators, membranes or diaphragms characterised by the material
    • H01M50/411—Organic material
    • H01M50/414—Synthetic resins, e.g. thermoplastics or thermosetting resins
    • H01M50/42—Acrylic resins
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/409—Separators, membranes or diaphragms characterised by the material
    • H01M50/411—Organic material
    • H01M50/414—Synthetic resins, e.g. thermoplastics or thermosetting resins
    • H01M50/423—Polyamide resins
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/409—Separators, membranes or diaphragms characterised by the material
    • H01M50/446—Composite material consisting of a mixture of organic and inorganic materials
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/409—Separators, membranes or diaphragms characterised by the material
    • H01M50/449—Separators, membranes or diaphragms characterised by the material having a layered structure
    • H01M50/457—Separators, membranes or diaphragms characterised by the material having a layered structure comprising three or more layers
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/489—Separators, membranes, diaphragms or spacing elements inside the cells, characterised by their physical properties, e.g. swelling degree, hydrophilicity or shut down properties
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M2220/00—Batteries for particular applications
    • H01M2220/20—Batteries in motive systems, e.g. vehicle, ship, plane
    • 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 technical field of lithium batteries, in particular to a battery, a battery module, a battery pack and an electrical device.
  • lithium-ion batteries have been widely used in energy storage power systems such as hydropower, thermal power, wind power and solar power stations, as well as power tools, electric bicycles, electric motorcycles, electric vehicles, Military equipment, aerospace and other fields. Due to the great development of lithium-ion batteries, higher requirements have been put forward for their energy density, group margin, cycle/rate performance and safety performance.
  • the separator is one of the components of the battery, and the separator can effectively prevent the contact between the positive and negative electrodes and cause internal short circuit.
  • the separator is only in physical contact with the positive or negative electrode, which easily leads to the expansion of the bare cell, which is not conducive to cell shaping. Therefore, existing batteries still need to be improved.
  • the present application was made in view of the above-mentioned problems, and an object thereof is to provide a battery to further improve the overall performance of the battery (high-rate discharge performance, cycle performance).
  • the present application provides a battery, a battery module, a battery pack and an electric device.
  • the first aspect of the present application provides a battery, which includes a positive electrode, a separator, and a negative electrode, and the separator includes a base film, a first coating on the first surface of the base film, and a first coating on the first surface of the base film.
  • the second coating on the second surface of the base film wherein the first coating includes a first polar substance, and the first polar substance includes polyolefin amides, polyolefin imines, polyoxyalkylene One or more of class, polyurethane, polyurea substances, there is a hydrogen bond between the first polar substance and the positive electrode binder of the positive electrode; the second coating includes the second Polar substances, the second polar substances include one or more of polyolefin amides, polyolefin imines, polyoxyalkylenes, polyurethanes, and polyureas, and the second polar substances There is a hydrogen bond with the binder for the negative electrode of the negative electrode and/or the active component of the negative electrode.
  • the hydrogen bond can be represented by X-H-Y, wherein X and Y can be independently selected from one of N, O and F. It is easy to form a hydrogen bond between the positive electrode binder (containing-X) and the first polar substance (containing-YH); similarly, the negative electrode binder and/or negative active component (containing-HX) and the second Hydrogen bonds are also easily formed between polar substances (including -YH). Therefore, the present application strengthens the bonding force between the separator and the positive electrode and the negative electrode through hydrogen bonds, thereby reducing the expansion of the bare cell during processing, and the cycle expansion rate after several cycles, and improving the high-rate discharge capacity of the battery. Shorten the lithium ion transmission path and improve the cycle performance of the battery.
  • the peeling force between the first coating and the positive electrode is not lower than 0.075N, optionally 0.075N-0.125N; the peeling force between the second coating and the negative electrode is not lower than 0.075N, optional 0.075N ⁇ 0.15N.
  • the peel force can characterize the size of the adhesive force between the separator and the positive and negative electrodes. The peeling force is within a reasonable range, the bare cells are not easy to expand during processing and cycling, the separator is in close contact with the positive and negative electrodes, and the battery has a strong high-rate discharge capability.
  • the ratio of the mass content w1 of the first polar substance in the first coating to the mass content m1 of the positive electrode binder in the film layer of the positive electrode It is (80 ⁇ 100): 1; the mass content w2 of the second polar substance in the second coating layer and the mass content m2 of the negative electrode binder in the film layer of the negative electrode ratio of It is (32 ⁇ 50):1.
  • the value is within a reasonable range, which can take into account the optimal ratio of battery performance and cost, and improve the high-rate discharge capacity and cycle performance of the battery.
  • the ratio of the mass content w1 of the first polar substance in the first coating to the mass content w2 of the second polar substance in the second coating It is 1: (1 ⁇ 1.3).
  • the mass content w1 of the first polar substance in the first coating is 80% to 90%, and the mass content of the positive electrode binder in the film layer of the positive electrode is The content m 1 is 0.9% to 1.2%.
  • the mass content w2 of the second polar substance in the second coating is 80% to 90%, and the mass content m2 of the negative electrode binder in the film layer of the negative electrode is 2 %. ⁇ 3%. Therefore, by limiting the above-mentioned parameters within a reasonable range, the battery can have both good high-rate discharge performance and cycle performance.
  • the first polar substance includes polyethylene oxide and polyacrylamide; wherein, the mass ratio C1 of polyethylene oxide to polyacrylamide is (2-6):1.
  • the second polar substance includes polyethyleneimine and polyethylene oxide; wherein, the mass ratio C2 of polyethyleneimine to polyethylene oxide is (2-6):1. Therefore, in the first polar substance, mixing a small amount of polyacrylamide long-chain molecules in polyethylene oxide can improve the cycle stability of the battery. In the second polar substance, a small amount of low-cost polyethylene oxide is added to the highly polar polyethyleneimine, and the two will also form hydrogen bonds to further enhance the bonding force between the second polar substance, thereby Further improve the high-rate discharge performance and cycle performance of the battery.
  • the first coating includes a first reinforcing agent, and the mass content w1 of the first polar substance in the first coating is the same as that of the first reinforcing agent in the first coating.
  • the ratio of the mass content k in a layer to the mass of 1 is (5 ⁇ 9): 1;
  • the second coating includes a second reinforcing agent, and the mass content w of the second polar substance in the second coating is equal to that of the second reinforcing agent in the first
  • the mass ratio of the mass content k in the second coating to 2 It is (5 ⁇ 9):1.
  • the ratio of the first polar substance to the first enhancer on the separator and the ratio of the second polar substance to the second enhancer within a reasonable range, the ratio of the first enhancer to the first polar substance Hydrogen bonds can be formed between the second enhancer and the second polar substance, so that the bare cell can be compacted more tightly during processing, and the cycle expansion rate of the bare cell after multiple cycles of charging and discharging is low, improving the battery life High rate discharge performance and cycle performance.
  • the mass content k 1 of the first reinforcing agent in the first coating is not higher than the mass content k 2 of the second reinforcing agent in the second coating.
  • the ratio of the mass content k of the first reinforcing agent in the first coating to the mass content k of the second reinforcing agent in the second coating It is (0.8 ⁇ 1):1. Therefore, by limiting the ratio of the mass content of the reinforcing agent in the first coating to the second coating within a reasonable range, the stability of the separator can be improved while the kinetics of lithium ion transport during charge and discharge is less affected, improving The cycle performance and high rate discharge performance of the battery.
  • the first enhancer or the second enhancer includes one or more of polyvinylidene fluoride and sodium alginate.
  • the binder for the positive electrode includes polyvinylidene fluoride
  • the binder for the negative electrode includes at least one of styrene-butadiene rubber and sodium alginate.
  • the negative electrode active component includes a silicon-carbon mixture, and in the silicon-carbon mixture, the particle size of silicon is 0.1-0.5 microns, and the carbon is a mixed carbon of artificial graphite and natural graphite, and the silicon-carbon mixture
  • the content in the negative electrode film layer is 95%-97%. Therefore, by limiting the particle size of silicon within a reasonable range, the cycle performance of the battery can be better, and by limiting the content of the silicon-carbon mixture in the negative electrode film layer within a reasonable range, high-rate charging of the battery can be achieved. discharge performance.
  • the mass ratio of the first coating layer to the second coating layer is 1:(1 ⁇ 1.5). Therefore, by limiting the coating amounts of the first coating and the second coating within a reasonable range, the tension of the separator can be made consistent, so as to prevent the risk of short circuit due to inconsistent tension, and improve the cycle performance of the battery.
  • the first coating is prepared from a first coating slurry, and the first coating slurry includes the first polar substance, the first reinforcing agent and a first solvent; Wherein, the viscosity of the first coating slurry is 8000mpa.s ⁇ 12000mpa.s.
  • the second coating is prepared from a second coating slurry, and the second coating slurry includes the second polar substance, the second reinforcing agent and a second solvent; wherein, the second The viscosity of the coating slurry is 5000mpa.s-20000mpa.s.
  • the coating process of the first coating slurry or the second coating slurry on the base film can be optimized , improve the coating effect, and ensure good consistency of the battery cells, which can improve the cycle performance and high-rate discharge performance of the battery.
  • the separator of the present application is particularly effective in improving the cyclic expansion rate of bare cells containing high-nickel positive electrode materials.
  • a second aspect of the present application provides a battery module including the battery of the first aspect of the present application.
  • a third aspect of the present application provides a battery pack, including the battery module of the second aspect of the present application.
  • a fourth aspect of the present application provides an electric device, including at least one selected from the battery of the first aspect of the present application, the battery module of the second aspect of the present application, or the battery pack of the third aspect of the present application.
  • the present invention has the following beneficial effects:
  • this application can improve the expansion of the bare cell during processing and reduce the cycle expansion rate of the bare cell during the cycle, which is beneficial to the shaping of the bare cell, making the bare cell more compact, and improving the high-rate discharge of the battery performance and cycle performance.
  • Figure 1 is a schematic diagram of the reaction principle of hydrogen bond formation between polar substances on the separator and the positive and negative electrodes.
  • Fig. 2 is a schematic diagram of infrared characterization of Examples 1-4 and Comparative Examples 1-3 of the present application.
  • FIG. 3 is a schematic diagram of a secondary battery according to an embodiment of the present application.
  • FIG. 4 is an exploded view of the secondary battery according to one embodiment of the present application shown in FIG. 3 .
  • FIG. 5 is a schematic diagram of a battery module according to an embodiment of the present application.
  • FIG. 6 is a schematic diagram of a battery pack according to an embodiment of the present application.
  • FIG. 7 is an exploded view of the battery pack according to one embodiment of the present application shown in FIG. 6 .
  • FIG. 8 is a schematic diagram of an electrical device in which a secondary battery is used as a power source according to an embodiment of the present application.
  • ranges disclosed herein are defined in terms of lower and upper limits, and a given range is defined by selecting a lower limit and an upper limit that define the boundaries of the particular range. Ranges defined in this manner may be inclusive or exclusive and may be combined in any combination, ie any lower limit may be combined with any upper limit to form a range. For example, if ranges of 60-120 and 80-110 are listed for a particular parameter, it is understood that ranges of 60-110 and 80-120 are contemplated. Additionally, if the minimum range values 1 and 2 are listed, and if the maximum range values 3, 4, and 5 are listed, the following ranges are all expected: 1-3, 1-4, 1-5, 2- 3, 2-4 and 2-5.
  • the numerical range "a-b” represents an abbreviated representation of any combination of real numbers between a and b, where a and b are both real numbers.
  • the numerical range "0-5" indicates that all real numbers between "0-5" have been listed in this article, and "0-5" is only an abbreviated representation of the combination of these values.
  • a certain parameter is an integer ⁇ 2
  • the method includes steps (a) and (b), which means that the method may include steps (a) and (b) performed in sequence, and may also include steps (b) and (a) performed in sequence.
  • steps (c) means that step (c) may be added to the method in any order, for example, the method may include steps (a), (b) and (c) , may also include steps (a), (c) and (b), may also include steps (c), (a) and (b) and so on.
  • the “comprising” and “comprising” mentioned in this application mean open or closed.
  • the “comprising” and “comprising” may mean that other components not listed may be included or included, or only listed components may be included or included.
  • the term "or” is inclusive unless otherwise stated.
  • the phrase "A or B” means “A, B, or both A and B.” More specifically, the condition "A or B” is satisfied by either of the following: A is true (or exists) and B is false (or does not exist); A is false (or does not exist) and B is true (or exists) ; or both A and B are true (or exist).
  • the inventors of the present application found that: on the one hand, during the processing process, the positive electrode, separator, and negative electrode are wound and compacted into bare cells. Compaction, but after a period of time, the bare cell itself will have a tendency to rebound, which will cause the bare cell to expand. On the other hand, during the cycle, the negative electrode active material itself, such as the graphite lattice becomes larger, and the interlayer distance between the graphite sheets becomes larger, which will cause the thickness of the bare cell to become thicker, thereby causing the bare cell to expand.
  • a polar substance can be coated on the surface of the base film of the separator, and through the polarity A hydrogen bond is formed between the substance and the binder for the positive electrode, the binder for the negative electrode, or the active material of the negative electrode, thereby increasing the binding force between the separator and the positive electrode and the negative electrode.
  • some reinforcing agents can be mixed into the polar substances to improve the adhesion of the separator.
  • the inventors proceeded from the synergistic effects of the two aspects, and through the comprehensive modification of the separator, fully synergistically utilized the effects of the above two aspects, and designed a battery that can significantly improve the adhesion between the separator and the positive and negative electrodes, and reduce the The expansion of bare cells during processing and the cycle expansion rate during cycle use greatly improve the high-rate discharge performance and cycle performance of the battery.
  • the present application proposes a battery.
  • the battery includes a positive electrode, a separator, a negative electrode, and an electrolyte.
  • the separator includes a base film, a first coating on the first surface of the base film, and a second coating on the second surface of the base film. layer, where
  • the first coating layer includes a first polar substance, and the first polar substance includes one of polyolefin amides, polyolefin imines, polyoxyalkylenes, polyurethanes, and polyureas, or A plurality of kinds, there is a hydrogen bond between the first polar substance and the positive electrode binder of the positive electrode;
  • the second coating layer includes a second polar substance, and the second polar substance includes one or more of polyolefin amides, polyolefin imines, polyoxyalkylenes, polyurethanes, and polyureas. Multiple, there is a hydrogen bond between the second polar substance and the negative electrode binder and/or negative electrode active component of the negative electrode.
  • the first coating on the separator of the present application is a structure with a predetermined thickness including the first polar substance.
  • the first coating can be firmly bonded to the positive electrode by the first polar substance, thereby preventing bare Expansion during cell processing and cycle expansion rate during cycle use.
  • the first polar substances such as polyolefin amides, polyolefin imines, polyoxyalkylenes, polyurethanes, polyureas, etc. include polar functional groups, on the one hand, they can be used with the positive electrode through the polar group functional group Hydrogen bonds are formed between the binders to improve the bonding force between the first coating and the positive electrode; on the other hand, the first polar substance itself is a binder, which can also improve the bonding force between the first coating and the positive electrode cohesion. Therefore, through the functions of the polar functional groups in the first polar substance and the first polar substance itself as a binder, the first coating is more firmly bonded to the positive electrode.
  • the first polar substance of the present application has a YH group, and Y is selected from one of N, O, and F.
  • the positive electrode binder has an X group, and X is selected from one of N, O, and F.
  • the positive electrode binder with the X group can form a hydrogen bond X-H-Y with the YH group in the first polar substance of the present application, so that the first coating of the present application is bonded to the positive electrode of the present application.
  • the knot is stronger. More specifically, as shown in FIG. 1 , it is illustrated by taking the positive electrode binder containing F as an example. Since the positive electrode binder contains F, the positive electrode binder and the first polar substance (-OH) are likely to form hydrogen bonds.
  • the second coating layer of the separator of the present application is a structure with a predetermined thickness comprising a second polar substance, and the second coating layer can firmly adhere to the negative electrode binder and/or negative electrode active material through the second polar substance. Junction, thereby preventing the expansion of bare cells during processing and the cyclic expansion rate during cycle use.
  • the second polar substances such as polyolefin amides, polyolefin imines, polyoxyalkylenes, polyurethanes, polyureas, etc. all include polar functional groups.
  • a hydrogen bond is formed between the binder and/or the negative electrode active material to improve the binding force between the first coating and the negative electrode; The adhesion between the layer and the negative electrode. Therefore, through the functions of the polar functional groups in the second polar substance and the second polar substance itself as a binder, the second coating layer is more firmly bonded to the negative electrode.
  • the second polar substance of the present application has a YH group, and Y is selected from one of N, O, and F.
  • the binder for the negative electrode and/or the active component of the negative electrode has a -HX group, and X is selected from one of N, O, and F; the binder for the negative electrode and/or the active component of the negative electrode with the X group here
  • the component can form a hydrogen bond XHY with the YH group in the second polar substance of the present application, so that the second coating of the present application and the negative electrode of the present application can be bonded more firmly.
  • the negative electrode contains -OH/-COOH, more for example contains -OH in the negative electrode active material, and -COOH in the negative electrode binder, so the negative electrode active material or negative electrode binder and the second polar material (Containing -NH 2 ) is also easy to form hydrogen bonds.
  • the adhesion between the separator and the positive electrode and the negative electrode can be enhanced through hydrogen bonds, thereby reducing the expansion and cycle of the bare cell during processing.
  • the cyclic expansion rate during use is conducive to the shaping of the bare cell, making the bare cell more compact, thereby shortening the transmission path of lithium ions, allowing lithium ions to be transmitted faster, and thus improving the high rate discharge performance of the battery and cycle performance is better.
  • the peeling force between the first coating and the positive electrode is not less than 0.075N, and may be 0.075N ⁇ 0.125N.
  • the peeling force between the second coating and the negative electrode is not less than 0.075N, and may be 0.075N ⁇ 0.15N.
  • Peeling force usually refers to the maximum force required to peel off the unit width of the bonded materials from the contact surface.
  • the peel force can reflect the bond strength of the material.
  • the detailed test method of peel force can be found in the test method section of the examples. Specifically in this application, the magnitude of the peeling force can be used to reflect the existence and strength of hydrogen bonds between the separator and the positive and negative electrodes from a macroscopic perspective, and further reflect the strength of the bonding force between the separator and the positive and negative electrodes.
  • the separation film if the first coating does not contain the first polar substance
  • the peeling force between it and the positive electrode is usually less than 0.035N.
  • the adhesion between them is small, and there is no or very little hydrogen bond.
  • the peeling force between the first coating and the positive electrode is not less than 0.075N, therefore, it can be further proved that there is a hydrogen bond between the first polar substance and the binder for the positive electrode.
  • the peeling force between the separator (if the second coating does not contain the second polar substance) and the negative electrode is usually less than 0.035N.
  • the cohesive force is small, and there is no or very little hydrogen bond.
  • the peeling force between the negative electrode surface and the separator coating it is unexpectedly found that by adding a second polar substance in the second coating, the peeling force between the second coating and the negative electrode is not less than 0.075N, which can It is further proved that there is a hydrogen bond between the second polar substance and the negative electrode binder or the negative electrode active component.
  • the bare cell when the peeling force between the first coating and the positive electrode or the peeling force between the second coating and the negative electrode is not less than 0.075N, the bare cell can be made It is not easy to expand, and the separator is in closer contact with the positive and negative electrodes, which shortens the transmission path of lithium ions, so that lithium ions can be transmitted faster, so that the high-rate discharge performance and cycle performance of the battery are better.
  • the ratio of the mass content w1 of the first polar substance in the first coating to the mass content m1 of the positive electrode binder in the film layer of the positive electrode can be (80-100):1.
  • the binder used in the positive electrode is usually an inert insulator, which has poor electrical conductivity and large polarization, which affects the cycle performance and high-rate discharge performance of the battery. .
  • the value is within a reasonable range, the expansion of bare cells during processing and recycling can be reduced, and the high-rate discharge performance and cycle performance of the battery can be improved.
  • the ratio of the mass content w of the second polar substance in the second coating to the mass content m of the negative electrode binder in the film layer of the negative electrode can be (32-50):1.
  • the It reflects the relative content relationship between the second polar substance in the separator and the binder in the negative electrode.
  • the binder used in the negative electrode is usually an inert insulator, which has poor electrical conductivity and large polarization, which affects the cycle performance and high rate discharge performance of the battery. .
  • the value is within a reasonable range, it can reduce the expansion of the bare cell during the processing and cycling of the bare cell, and improve the high-rate discharge performance and cycle performance of the battery.
  • the ratio of the mass content w2 of the second polar substance in the second coating to the mass content m2 of the negative electrode binder in the film layer of the negative electrode It can be 32:1, 36:1, 40:1, 45:1, or 50:1, etc. It can be any point value above or a range value formed between any point values.
  • the ratio of the mass content w1 of the first polar substance in the first coating to the mass content w2 of the second polar substance in the second coating It can be 1: (1-1.3).
  • the It reflects the content of polar substances coated on both surfaces of the isolation film.
  • the tension of the separator can be made consistent and more stable. On the one hand, it can prevent the risk of short circuit due to inconsistent tension, and on the other hand, it can improve the cycle performance and high-rate discharge performance of the battery. if less than 1:1 or When it is greater than 1:1.3, the two surface tensions of the separator will be inconsistent, the separator will wrinkle, bubbles will appear on the surface, the electrolyte will not infiltrate well, lithium precipitation will easily occur, the cycle performance will deteriorate, and the cycle attenuation will become faster. Discharge performance deteriorates.
  • the difference between the coating amounts of the first polar substance and the second polar substance cannot be too large, and the coating amounts of the two can be selected to be substantially equal, that is, This can ensure that the bearing capacity of the two surfaces of the separator is basically the same, and the cycle performance and high-rate discharge performance of the battery are better.
  • the mass content w 1 of the first polar substance in the first coating may be 80%-90%.
  • w1 may be used to reflect the content of the first polar substance in the first coating.
  • the first polar substance occupies the main body in the first coating, which can increase the hydrogen bond between the first polar substance and the binder for the positive electrode, thereby making the first coating and the positive electrode have better adhesion .
  • the content of the first polar substance in the first coating is less than 80%, the hydrogen bond between the binder for the positive electrode will be less, the improvement of the adhesion between the separator and the positive electrode will be limited, and the processing of the bare cell will be limited.
  • the expansion improvement effect during the process and recycling process is not obvious; if the content of the first polar substance in the first coating is greater than 90%, it is easy to block the base film, thereby reducing the air permeability and affecting the dynamic performance of the isolation film.
  • the mass content w1 of the first polar substance in the first coating may be 80%, 85%, 90% and so on.
  • w 1 may be any point value above or a range value formed between any point values.
  • the mass content m 1 of the positive electrode binder in the positive electrode film layer may be 0.9% ⁇ 1.2%.
  • the content of the positive electrode binder in the positive electrode film layer can be reflected by m 1 .
  • m 1 within this range can make the positive electrode and the first coating have a strong bonding force, thereby reducing the expansion of the bare cell during processing or recycling, and improving the high-rate discharge performance and cycle performance of the battery.
  • the content of the binder for the positive electrode in the positive electrode sheet should not be too large.
  • m 1 is greater than 1.2%, the content of the binder for the positive electrode is too much, which will block the electron transmission channel.
  • the binder for the positive electrode is usually an inert insulator, conductive Poor performance and large polarization will affect the cycle performance and high rate discharge performance of the battery.
  • the content of the positive electrode binder in the positive electrode sheet should not be too small.
  • m 1 is less than 0.9%, it may be due to too little content of the positive electrode binder, which will lead to insufficient adhesion, and the adhesion between the positive electrode and the first coating will be small. .
  • the mass content m 1 of the positive electrode binder in the positive electrode film layer may be 0.9%, 1%, or 1.2%.
  • m 1 may be any point value above or a range value formed between any point values.
  • the kinetic performance and the adhesion between the first coating and the positive electrode can be taken into account, and the optimal ratio of the two can be obtained to improve the high-rate discharge of the battery. performance and cycle performance.
  • the mass content w 2 of the second polar substance in the second coating may be 80%-90%.
  • the content of the second polar substance in the second coating can be reflected by w 2 .
  • the second polar substance occupies the main body in the second coating, which can increase the hydrogen bond between the second polar substance and the binder for the negative electrode, thereby making the second coating and the negative electrode have better adhesion .
  • the content of the second polar substance in the second coating is lower than 80%, there will be less hydrogen bonding with the binder for the negative electrode, and the improvement of the adhesion between the separator and the negative electrode will be limited, and the bare cell will The expansion improvement effect during processing and recycling is not obvious; if the content of the second polar substance in the second coating is greater than 90%, it is easy to block the base film, thereby reducing the air permeability and affecting the kinetics of the isolation film performance.
  • the mass content w2 of the second polar substance in the second coating may be 80%, 85%, or 90%, etc.
  • w 2 may be any point value above or a range value formed between any point values.
  • the mass content m 2 of the negative electrode binder in the negative electrode film layer may be 2%-3%.
  • the content of the positive electrode binder in the negative electrode film layer can be reflected by m 2 .
  • m2 within this range can make the negative electrode and the second coating have firm adhesion, thereby reducing the expansion of the bare cell during processing or recycling, improving the high-rate discharge performance of the battery and cycle performance.
  • the content of the negative electrode binder in the negative electrode sheet should not be too large.
  • m 1 is greater than 3%, the content of the negative electrode binder is too much, which will block the electron transmission channel.
  • the negative electrode binder is usually an inert insulator, conductive Poor performance and large polarization will affect the cycle performance and high rate discharge performance of the battery.
  • the content of the negative electrode binder in the negative electrode sheet should not be too small.
  • m 1 is less than 2%, it may be due to too little content of the negative electrode binder, which will lead to insufficient adhesion, and the adhesion between the negative electrode and the second coating will be small. .
  • the mass content m2 of the negative electrode binder in the negative electrode film layer can be 2 %, 2.6%, 3% or the like.
  • m 2 may be any point value above or a range value formed between any point values.
  • both the kinetic performance and the adhesion between the second coating and the negative electrode can be taken into account, the optimal ratio of the two can be obtained, and the high-rate discharge of the battery can be improved. performance and cycle performance.
  • the first polar substance includes polyethylene oxide and polyacrylamide.
  • the mass ratio C1 of polyethylene oxide to polyacrylamide may be (2-6):1.
  • polyethylene oxide is a lithium ion conductor, which has the characteristics of high conductivity, low activation energy and the most negative electrode potential, which can speed up the conduction of lithium ions. occupy the main body.
  • polyacrylamide has a long chain, a large molecular weight, and good thermal stability, and the side that is usually connected to the positive electrode has been oxidized by high pressure, so if it is in polyethylene oxide Mixing a small amount of long-chain molecules such as polyacrylamide, especially within the scope defined in this application, can improve the cycle stability and high-rate discharge performance of the battery.
  • the mass ratio C1 of polyethylene oxide to polyacrylamide is less than 2:1, since polyacrylamide is not a lithium ion conductor, the lithium ion conduction rate will be slow, affecting the cycle performance and high rate discharge performance of the battery. However, if the mass ratio C1 of polyethylene oxide to polyacrylamide is greater than 6:1, too little polyacrylamide content will result in poor thermal stability.
  • the mass ratio C1 of polyethylene oxide to polyacrylamide may be 2:1, 3:1, 4.5:1, 5:1, or 6:1.
  • C1 may be any point value above or a range value formed between any point values.
  • the second polar substance includes polyethyleneimine and polyethylene oxide.
  • the mass ratio C2 of polyethyleneimine to polyethylene oxide may be (2-6):1.
  • both polyethyleneimine and polyethylene oxide are lithium ion conductors, which have the characteristics of high electrical conductivity, low activation energy and the most negative electrode potential, which can accelerate the conduction of lithium ions.
  • the second active material is located on the side connected to the negative electrode. Since the negative active material such as graphite is easy to expand, it is necessary to select a binder with a stronger polarity such as polyethyleneimine (PEI).
  • polyethylene oxide is relatively Polyethyleneimine is cheap, considering the cost factor, a small amount of polyethylene oxide can be added to polyethyleneimine, especially within the scope of this application, while reducing costs, the two will also form hydrogen bonds with each other, further strengthening Adhesive force, reduce the expansion of bare cells during processing and recycling, and improve the cycle performance and high-rate discharge performance of the battery.
  • the mass ratio C2 of the polyethyleneimine to polyethylene oxide is less than 2:1, due to the strong polarity of the polyethyleneimine, if the content is too small, the second polar substance and the negative electrode binder or negative electrode activity will be caused. The formation of hydrogen bonds between substances is less, the binding force between the second coating and the negative electrode is reduced, and the bare cell expansion during the processing and recycling of the bare cell is reduced, which affects the cycle performance and high-rate discharge performance of the battery.
  • the mass ratio C2 of polyethyleneimine to polyethylene oxide is greater than 6:1, the cost will increase.
  • the mass ratio C2 of polyethyleneimine to polyethylene oxide can be 2:1, 3:1, 4.5:1, 5:1, or 6:1, etc.
  • C2 can be any point value above or a range value formed between any point values.
  • the polyamides may be one or more of polyacrylamide (PAM), nylon-66, nylon-6, etc. combination of species.
  • PAM polyacrylamide
  • the weight average molecular weight of polyamides can be 20,000 to 80,000; it can be 20,000, 30,000, 40,000, 50,000, 60,000, 70,000, or 80,000, etc.
  • the weight average molecular weight of polyamides can be Any point value above or a range value formed between any point values.
  • the polyolefinimines may be, for example, one or more of polyethyleneimine (PEI), polyethylene polyamine, and the like.
  • PEI polyethyleneimine
  • the weight-average molecular weight of the polyimines can be 70,000 to 100,000; it can be 70,000, 80,000, 90,000, or 100,000, etc.
  • the weight-average molecular weight of the polyolefinimines can be any of the above-mentioned values Or a range of values between any point values.
  • the polyoxyalkylene in the first polar substance or the second polar substance, can be, for example, polyethylene oxide (PEO) or the like.
  • the weight-average molecular weight of the polyoxyalkylenes can be 100,000 to 200,000; it can be 100,000, 120,000, 140,000, 160,000, 180,000, or 200,000, etc.
  • the weight-average molecular weight of the polyoxyalkylenes can be It is any point value above or a range value formed between any point values.
  • polyurethanes can be, for example, a type of polymer containing -NHCOO- in the general formula, more for example, polyurethanes can be composed of polyisocyanate, toluene Diisocyanate (TDI), diphenylmethane-4,4'-diisocyanate (MDI), polyphenyl polymethylene polyisocyanate (PAPI) formed by polymerization of at least one monomer, or copolymerization of two or more monomers Formation, polymerization methods include random copolymerization, block copolymerization, etc.
  • TDI toluene Diisocyanate
  • MDI diphenylmethane-4,4'-diisocyanate
  • PAPI polyphenyl polymethylene polyisocyanate
  • the weight-average molecular weight of the polyurethanes can be 0.1-10,000; it can be 0.1, 5,000, or 10,000, etc.
  • the weight-average molecular weight of the polyurethanes can be any of the above-mentioned values or a composition between any points. range of values.
  • the polyurea can be, for example, a type of polymer containing -NHCONH- in the general formula, more for example, it can be polyurea, urea-formaldehyde resin, etc. one or more of.
  • the weight-average molecular weight of the polyurea material can be 50,000 to 50,000; it can be 5,000, 10,000, 20,000, 30,000, 40,000, or 50,000, etc.
  • the weight-average molecular weight of the polyurea can be Any point value above or a range value formed between any point values.
  • the first coating layer includes a first reinforcing agent, and the mass content w of the first polar substance in the first coating layer is equal to that of the first reinforcing agent in the first coating layer.
  • the ratio of the mass content k in the coating to the mass of 1 It can be (5-9):1.
  • the adhesion of the first polar substance to the base film can be enhanced by the first enhancer. Only when the ratio of the first polar substance on the separator to the first enhancer is within a reasonable range can the expansion of the bare cell during processing and the cycle expansion rate during cycle use be reduced, and the cycle performance and high-rate discharge of the battery can be improved. performance. when When it is greater than 9:1, the content of the first polar substance is too much. First, it is easy to block the basement membrane, thereby reducing the air permeability and affecting the dynamic performance of the isolation membrane. The film falls off, resulting in poor cycle performance and high-rate discharge performance.
  • the content of the first polar substance in the first coating is too small, resulting in less hydrogen bond formation between the first polar substance and the positive electrode binder, plus the first polar substance
  • the adhesive force itself is not enough, and then the adhesive force between the first coating and the binder for the positive electrode cannot be firm, so that the problem of expansion during the processing and recycling of the bare cell cannot be well solved.
  • the first enhancer containing F
  • the first polar substance -YH
  • the first An enhancer can stabilize the first polar substance on the separation membrane. Therefore, the expansion of the bare cell during processing and the cycle expansion rate during cycle use can be reduced, and the cycle performance and high-rate discharge performance of the battery can be improved.
  • the mass ratio of the mass content w 1 of the first polar substance in the first coating to the mass content k 1 of the first reinforcing agent in the first coating It can be 5:1, 5.3:1, 6:1, 8:1, 9:1, etc. It can be any point value above or a range value formed between any point values.
  • the second coating includes a second reinforcing agent, and the mass content w of the second polar substance in the second coating is equal to that of the second reinforcing agent in the second coating.
  • the mass ratio of the mass content k in 2 It can be (5-9):1.
  • the adhesion of the second polar substance on the base film can be enhanced by the second enhancer. Only when the ratio of the second polar substance on the separator to the second enhancer is within a reasonable range can the expansion of the bare cell during processing and the cycle expansion rate during cycle use be reduced, and the cycle performance and high-rate discharge of the battery can be improved. performance. when When the content is greater than 9:1, the content of the second polar substance is relatively too much, and it will easily fall off in the middle and late stages of the cycle, resulting in poor cycle performance and high-rate discharge performance.
  • the second enhancer can stabilize the second polar substance on the separator, thereby reducing the expansion of the bare cell during processing and the cycle expansion rate during cycle use, and improving the cycle performance and high-rate discharge performance of the battery.
  • the mass ratio of the mass content w2 of the second polar substance in the second coating to the mass content k2 of the second reinforcing agent in the second coating It can be 5:1, 5.3:1, 6:1, 8:1, 9:1, etc. It can be any point value above or a range value formed between any point values.
  • the mass content k 1 of the first reinforcing agent in the first coating is not higher than the mass content k 2 of the second reinforcing agent in the second coating.
  • k 1 and k 2 can be used to reflect the coating enhancer content on both surfaces of the isolation film, wherein the difference between k 1 and k 2 should not be too large.
  • the tension of the separator can be kept consistent and more stable. On the one hand, it can prevent the risk of short circuit due to inconsistent tension, and on the other hand, it can improve the cycle performance and high-rate discharge performance of the battery. If the content of k1 and k2 is too different, the two surface tensions of the separator will be inconsistent, the separator will wrinkle, bubbles will appear on the surface, the electrolyte will not infiltrate well, lithium precipitation will easily occur, the cycle performance will deteriorate, and the cycle attenuation will occur. Faster, the performance of high-rate discharge becomes worse.
  • the ratio of the mass content k of the first reinforcing agent in the first coating to the mass content k of the second reinforcing agent in the second coating It can be (0.8 ⁇ 1):1.
  • the content on both surfaces of the isolation film is basically the same, which can reduce the difference between the two surfaces of the isolation film.
  • the ratio of the mass content k1 of the first reinforcing agent in the first coating to the mass content k2 of the second reinforcing agent in the second coating It can be 0.80:1, 0.9:1, 0.95:1, or 1:1, etc. It can be any point value above or a range value formed between any point values.
  • the mass content k 1 of the first reinforcing agent in the first coating layer may be 10%-20%.
  • the mass percentage k 2 of the second reinforcing agent in the second coating may be 10%-20%.
  • the content of the first reinforcing agent in the first coating can be reflected by k 1 .
  • the content of the second reinforcing agent in the second coating can be reflected by k2.
  • the difference between the content of the first reinforcing agent in the first coating and the content of the second reinforcing agent in the second coating should not be too large, if the difference between the contents of k1 and k2 is too large, it will cause two If the surface tension is not consistent, the separator will wrinkle, bubbles will appear on the surface, the electrolyte will not infiltrate well, lithium precipitation will easily occur, the cycle performance will deteriorate, the cycle attenuation will become faster, and the high rate discharge performance will deteriorate.
  • the stability of the separator can be improved while having little impact on the kinetics of lithium ion transport, and both kinetics and viscosity can be taken into account to achieve an optimal ratio, which can improve the cycle performance and high performance of the battery. Rate discharge performance.
  • the content on both sides of the separator is basically the same, which can reduce the difference between the two sides of the separator, and the tension of the separator is consistent to prevent wrinkling.
  • the mass content k 1 of the first reinforcing agent in the first coating layer may be 14%, 16.6%, 18%, 19%, or 20%.
  • k 1 may be any point value above or a range value formed between any point values.
  • the mass percentage k 2 of the second reinforcing agent in the second coating may be 10%, 11%, 14%, 15.8%, 16.6%, 17%, or 20%.
  • k 2 may be any point value above or a range value formed between any point values.
  • the first enhancer or the second enhancer includes one or more of polyvinylidene fluoride and sodium alginate, wherein, due to the low cost of polyvinylidene fluoride, polyvinylidene fluoride can be preferably used Vinylidene fluoride.
  • the positive electrode binder includes polyvinylidene fluoride.
  • the negative electrode binder includes more than one of styrene-butadiene rubber and sodium alginate.
  • the weight average molecular weight of the first enhancer or the second enhancer is 0.05 million to 600,000; 10,000, or 600,000, etc., the weight-average molecular weight of the first enhancer or the second enhancer can be at any point above or within the range formed between any point.
  • the weight average molecular weight of the polyvinylidene fluoride can be 100,000-600,000; it can be 100,000, 200,000, 300,000, 400,000, 500,000, or 600,000.
  • the weight-average molecular weight may be any point value above or a range value formed between any point values.
  • the weight average molecular weight of sodium alginate can be 0.05 to 50,000; it can be 0.05 million, 10,000, 20,000, 30,000, 40,000, or 50,000, etc.
  • the weight average molecular weight of sodium alginate can be the above-mentioned Any point value or a range of values between any point values.
  • the aforementioned polyvinylidene fluoride and sodium alginate can be used in the first reinforcing agent, the second reinforcing agent, the binder for the positive electrode or the binder for the negative electrode.
  • the mass ratio of the first coating layer to the second coating layer may be 1: (1 ⁇ 1.5).
  • the content of coating substances on both sides of the isolation film can be reflected by the first coating and the second coating, and the difference between the two cannot be too large; thus, by limiting the coating of the first coating and the second coating The amount is within a reasonable range, which can make the tension of the separator consistent and more stable. On the one hand, it can prevent the risk of short circuit due to inconsistent tension. On the other hand, the cycle performance and high rate discharge performance of the battery can be improved. If the content difference between the first coating and the second coating is too large, the two surface tensions of the separator will be inconsistent, the separator will wrinkle, bubbles will appear on the surface, the electrolyte will not infiltrate well, lithium precipitation will easily occur, and the cycle performance will deteriorate. Poor, the cycle attenuation becomes faster, and the high rate discharge performance becomes worse.
  • the mass ratio of the first coating to the second coating may be 1:1, 1:2, 1:3, 1:4, 1:5 and so on.
  • the mass ratio of the first coating layer to the second coating layer may be any point value above or a range value formed between any point values.
  • the first coating or the second coating may also include fillers, such as alumina, which can improve the heat resistance and stability of the coating and be used in conjunction with the first polar substance , can reduce the expansion of the bare cell during processing and recycling, and improve the cycle performance and high-rate discharge performance of the battery.
  • the content of the filler is not particularly limited, for example, the mass ratio of the filler in the first coating or the second coating may be greater than 0 and less than or equal to 25%. If the content of the filler in the first coating or the second coating is greater than 25%, the pores of the base film will be blocked, resulting in a slow ion transmission rate and affecting the cycle performance and high-rate discharge performance of the battery.
  • the mass percentage of the filler in the first coating or the second coating may be 3.2%, 8%, 10%, 15%, 18.9%, 20%, or 25%.
  • the mass ratio of the filler in the first coating layer or the second coating layer may be any point value above or a range value formed between any point values.
  • the first coating is prepared from a first coating slurry.
  • the first coating slurry includes the first polar substance, the first reinforcing agent and the first solvent; wherein, the viscosity of the first coating slurry may be 8000mpa.s ⁇ 12000mpa.s.
  • the preparation method of the first coating slurry may adopt a known method in the art.
  • the first polar substance and the first reinforcing agent can be mixed in the first solvent to form a uniform slurry, which is the first coating slurry.
  • the first polar substance, the first reinforcing agent, and the filler can also be mixed and then dissolved in the first solvent for the preparation process.
  • the dosage of each substance can be set with reference to the mass ratio of each component in the first coating mentioned above in this application.
  • the viscosity of the first coating slurry has a great influence on the coating and the electrochemical performance of the battery. If the viscosity of the first coating slurry is too high, it is easy to form a gel, and the coating is uneven, resulting in poor consistency of the battery. The cycle performance and high rate discharge performance of the battery will be reduced. However, if the viscosity of the first coating slurry is too low, the first coating slurry cannot be well coated on the base film. Thus, by limiting the first coating slurry to an appropriate viscosity range, the first coating slurry can be better coated on the base film, and the consistency of the cell can be ensured to improve the cycle performance of the battery and high rate discharge performance.
  • the viscosity of the first coating slurry may be 8000mpa.s, 9000mpa.s, 10000mpa.s, 11000mpa.s, or 12000mpa.s.
  • the weight-average molecular weight of the first coating slurry may be any point above or a range formed between any points.
  • the first solvent is generally not limited, and more specifically, when the first enhancer is selected from sodium alginate, the choice of the first solvent is not limited. And when the first reinforcing agent is selected from polyvinylidene fluoride, the first solvent is selected from organic solvents, such as N,N-dimethylpyrrolidone, acetone and the like.
  • the second coating is prepared from a second coating slurry, and the preparation method of the second coating can be a method known in the art.
  • the second coating slurry includes the second polar substance, the second reinforcing agent and a second solvent; wherein, the viscosity of the second coating slurry is 5000mpa.s ⁇ 20000mpa.s.
  • the preparation method of the second coating slurry may adopt a known method in the art.
  • the second polar substance and the second reinforcing agent can be mixed in the second solvent to form a uniform slurry, which is the second coating slurry.
  • the second polar substance, the second reinforcing agent, and the filler can also be mixed and then dissolved in the second solvent for the preparation process.
  • the dosage of each substance can be set with reference to the mass ratio of each component in the second coating mentioned above in this application.
  • the viscosity of the second coating slurry has a great influence on the coating and the electrochemical performance of the battery. If the viscosity of the second coating slurry is too high, it is easy to form a gel, and the coating is uneven, resulting in poor consistency of the battery. The cycle performance and high rate discharge performance of the battery will be reduced. However, if the viscosity of the second coating slurry is too low, the second coating slurry cannot be well coated on the base film. Therefore, by limiting the second coating slurry to an appropriate viscosity range, the second coating slurry can be better coated on the base film, and the consistency of the cell can be ensured to improve the cycle performance of the battery and high rate discharge performance.
  • the viscosity of the second coating slurry may be 5000mpa.s, 8000mpa.s, 10000mpa.s, 13000mpa.s, 15000mpa.s, 18000mpa.s, or 20000mpa.s.
  • the weight-average molecular weight of the second coating slurry may be any point above or a range formed between any point.
  • the second solvent is generally not limited, and more specifically, when the second enhancer is selected from sodium alginate, the choice of the second solvent is not limited. And when the second reinforcing agent is selected from polyvinylidene fluoride, the second solvent is selected from organic solvents, such as N,N-dimethylpyrrolidone, acetone and the like.
  • the present application has no particular limitation on the type of the base membrane, and any known porous structure base membrane with good chemical stability and mechanical stability can be selected.
  • the material of the base film can be selected from at least one of glass fiber, non-woven fabric, polyethylene, polypropylene and polyvinylidene fluoride.
  • the base film may be a single-layer film or a multi-layer composite film, without any particular limitation.
  • the materials of each layer may be the same or different, and there is no particular limitation.
  • the negative electrode includes a negative electrode collector and a negative electrode film layer arranged on at least one surface of the negative electrode collector, and the negative electrode film layer includes a negative electrode active component.
  • the negative electrode active component includes a silicon-carbon mixture, and in the silicon-carbon mixture, the particle size of silicon may be 0.1-0.5 microns.
  • the carbon is a mixed carbon of artificial graphite and natural graphite.
  • micro-silicon has a great influence on the electrochemical performance. Compared with nano-silicon, micro-silicon has a smaller specific surface area, fewer side reactions, better battery cycle performance, and better high-rate discharge performance. Therefore, micro-silicon is selected. .
  • the particle size of the silicon is 0.1 micron, 0.3 micron, 0.5 micron, etc.
  • the particle diameter of silicon may be any point value above or a range value formed between any point values.
  • C:Si in the silicon-carbon mixture may be 95-97:3-5, etc. More for example C:Si may be 95:5.
  • the content of the silicon-carbon mixture in the negative electrode film layer may be 95%-97%. Since the content of the silicon-carbon mixture affects the energy density of the cell, usually the content of the silicon-carbon mixture in the negative electrode film layer is greater than 95% to achieve high capacity of the battery, improve the cycle performance and high-rate discharge performance of the battery.
  • the content of the silicon-carbon mixture in the negative electrode film layer may be 95.9%, 96%, 96.7%, 96.8%, or 97%.
  • the content of the silicon-carbon mixture in the negative electrode film layer may be at any value above or in a range formed between any point values.
  • the negative electrode active component can be a negative electrode active material known in the art for batteries.
  • the negative electrode active component may include at least one of the following materials: artificial graphite, natural graphite, soft carbon, hard carbon, silicon-based material, tin-based material, lithium titanate, and the like.
  • the silicon-based material may be selected from at least one of elemental silicon, silicon-oxygen compounds, silicon-nitrogen compounds, and silicon alloys.
  • the tin-based material may be selected from at least one of simple tin, tin oxide compounds and tin alloys.
  • the present application is not limited to these materials, and other conventional materials that can be used as the active component of the negative electrode of the battery can also be used.
  • These negative electrode active components may be used alone or in combination of two or more.
  • the negative electrode current collector has two opposing surfaces in its own thickness direction, and the negative electrode film layer is disposed on any one or both of the two opposing surfaces of the negative electrode current collector.
  • the negative electrode current collector can use a metal foil or a composite current collector.
  • copper foil can be used as the metal foil.
  • the composite current collector may include a base layer of polymer material and a metal layer formed on at least one surface of the base material of polymer material.
  • Composite current collectors can be formed by metal materials (copper, copper alloys, nickel, nickel alloys, titanium, titanium alloys, silver and silver alloys, etc.) on polymer material substrates (such as polypropylene (PP), polyethylene terephthalic acid It is formed on substrates such as ethylene glycol ester (PET), polybutylene terephthalate (PBT), polystyrene (PS), polyethylene (PE), etc.).
  • the negative electrode film layer may also optionally include a negative electrode binder.
  • the binder for the negative electrode can be selected from styrene-butadiene rubber (SBR), polyacrylic acid (PAA), sodium polyacrylate (PAAS), polyacrylamide (PAM), polyvinyl alcohol (PVA), sodium alginate (SA) , at least one of polymethacrylic acid (PMAA) and carboxymethyl chitosan (CMCS).
  • the binder for the negative electrode is selected from styrene-butadiene rubber (SBR) and sodium alginate (SA).
  • the negative electrode film layer may also optionally include a conductive agent.
  • the conductive agent can be selected from at least one of superconducting carbon, acetylene black, carbon black, Ketjen black, carbon dots, carbon nanotubes, graphene and carbon nanofibers.
  • the negative electrode film layer also optionally includes other additives, such as thickeners (such as sodium carboxymethylcellulose (CMC-Na)) etc.
  • thickeners such as sodium carboxymethylcellulose (CMC-Na)
  • the negative electrode can be prepared in the following manner: the above-mentioned components used to prepare the negative electrode, such as negative active components, conductive agents, binders and any other components are dispersed in a solvent (such as deionized water) , to form negative electrode slurry; the negative electrode slurry can be coated on the negative electrode current collector, and after drying, cold pressing and other processes, the negative electrode can be obtained.
  • a solvent such as deionized water
  • the positive electrode includes a positive electrode collector and a positive electrode film layer arranged on at least one surface of the positive electrode collector, and the positive electrode film layer includes the positive electrode material according to the first aspect of the present application.
  • the nickel content of the positive electrode material is greater than 0.5.
  • the changes in the expansion of the bare cell are different.
  • the expansion rate improvement effect is remarkable.
  • the unit cell parameters of the positive electrode material change greatly, the volume change of the positive electrode material also changes greatly, and the final bare cell expansion changes greatly compared with the initial bare cell expansion.
  • the cyclic expansion rate of the obtained bare cell is relatively small, and within the aforementioned scope of the present application, the cyclic expansion rate of the bare cell is improved more significantly, and the cycle retention rate is better.
  • the nickel content is, for example, 0.8-0.9, although the unit cell parameters of the positive electrode material change little, the cyclic expansion rate of the final bare cell is also very small, so it is also within the scope required by this application.
  • the positive electrode material can be LiNi 0.4 Co 0.4 Mn 0.2 O 2 , LiNi 0.5 Co 0.2 Mn 0.3 O 2 , LiNi 0.6 Co 0.2 Mn 0.2 O 2 , LiNi 0.7 Co 0.2 Mn 0.1 O 2 , LiNi 0.8 Co 0.1 Mn 0.1 O 2 , LiNi 0.9 Co 0.05 Mn 0.05 O 2 etc.
  • positive electrode active materials known in the art for batteries can be used as the positive electrode active material.
  • the positive active material may include at least one of the following materials: olivine-structured lithium-containing phosphate, lithium transition metal oxide, and their respective modified compounds.
  • the present application is not limited to these materials, and other conventional materials that can be used as positive electrode active materials of batteries can also be used. These positive electrode active materials may be used alone or in combination of two or more.
  • lithium transition metal oxides may include, but are not limited to, lithium cobalt oxides (such as LiCoO 2 ), lithium nickel oxides (such as LiNiO 2 ), lithium manganese oxides (such as LiMnO 2 , LiMn 2 O 4 ), lithium Nickel cobalt oxide, lithium manganese cobalt oxide, lithium nickel manganese oxide, lithium nickel cobalt manganese oxide (such as LiNi 1/3 Co 1/3 Mn 1/3 O 2 (also referred to as NCM 333 ), LiNi 0.5 At least one of Co 0.25 Mn 0.25 O 2 (also abbreviated as NCM 211 ), lithium nickel cobalt aluminum oxide (such as LiNi 0.85 Co 0.15 Al 0.05 O 2 ) and its modified compounds, etc.
  • lithium cobalt oxides such as LiCoO 2
  • lithium nickel oxides such as LiNiO 2
  • lithium manganese oxides such as LiMnO 2 , LiMn 2 O 4
  • Nickel cobalt oxide lithium manganese cobalt oxide,
  • Lithium-containing olivine structure examples may include, but are not limited to, lithium iron phosphate (such as LiFePO 4 (also may be abbreviated as LFP)), a composite of lithium iron phosphate and carbon, lithium manganese phosphate (such as LiMnPO 4 ), a composite of lithium manganese phosphate and carbon material, at least one of lithium manganese iron phosphate, and a composite material of lithium manganese iron phosphate and carbon.
  • lithium iron phosphate such as LiFePO 4 (also may be abbreviated as LFP)
  • LiMnPO 4 lithium manganese phosphate
  • LiMnPO 4 lithium manganese phosphate and carbon material
  • the positive electrode current collector has two opposing surfaces in its own thickness direction, and the positive electrode film layer is disposed on any one or both of the two opposing surfaces of the positive electrode current collector.
  • the positive electrode current collector can be a metal foil or a composite current collector.
  • aluminum foil can be used as the metal foil.
  • the composite current collector may include a polymer material base and a metal layer formed on at least one surface of the polymer material base.
  • the composite current collector can be formed by forming metal materials (aluminum, aluminum alloy, nickel, nickel alloy, titanium, titanium alloy, silver and silver alloy, etc.) on a polymer material substrate (such as polypropylene (PP), polyethylene terephthalic acid It is formed on substrates such as ethylene glycol ester (PET), polybutylene terephthalate (PBT), polystyrene (PS), polyethylene (PE), etc.).
  • PP polypropylene
  • PET polyethylene glycol ester
  • PBT polybutylene terephthalate
  • PS polystyrene
  • PE polyethylene
  • the positive electrode film layer may further optionally include a binder for the negative electrode.
  • the binder for the negative electrode may include polyvinylidene fluoride (PVDF), polytetrafluoroethylene (PTFE), vinylidene fluoride-tetrafluoroethylene-propylene terpolymer, vinylidene fluoride-hexafluoropropylene- At least one of tetrafluoroethylene terpolymer, tetrafluoroethylene-hexafluoropropylene copolymer and fluorine-containing acrylate resin.
  • the binder for the negative electrode is selected from polyvinylidene fluoride (PVDF).
  • the positive electrode film layer may also optionally include a conductive agent.
  • the conductive agent may include at least one of superconducting carbon, acetylene black, carbon black, Ketjen black, carbon dots, carbon nanotubes, graphene, and carbon nanofibers.
  • the positive electrode can be prepared in the following manner: the above-mentioned components for preparing the positive electrode, such as positive electrode material, conductive agent, binder and any other components are dispersed in a solvent (such as N-methylpyrrolidone) In the process, the positive electrode slurry is formed; the positive electrode slurry is coated on the positive electrode current collector, and after drying, cold pressing and other processes, the positive electrode can be obtained.
  • a solvent such as N-methylpyrrolidone
  • electrolyte plays the role of conducting ions between the positive pole piece and the negative pole piece.
  • the application does not have specific restrictions on the type of electrolyte, which can be selected according to requirements.
  • electrolytes can be liquid, gel or all solid.
  • the electrolyte is an electrolytic solution.
  • the electrolyte solution includes an electrolyte salt and a solvent.
  • the electrolyte salt may be selected from lithium hexafluorophosphate, lithium tetrafluoroborate, lithium perchlorate, lithium hexafluoroarsenate, lithium bisfluorosulfonyl imide, lithium bistrifluoromethanesulfonyl imide, trifluoromethane At least one of lithium sulfonate, lithium difluorophosphate, lithium difluorooxalate borate, lithium difluorooxalate borate, lithium difluorodifluorooxalatephosphate and lithium tetrafluorooxalatephosphate.
  • the solvent may be selected from ethylene carbonate, propylene carbonate, ethyl methyl carbonate, diethyl carbonate, dimethyl carbonate, dipropyl carbonate, methyl propyl carbonate, ethyl propyl carbonate, Butylene carbonate, fluoroethylene carbonate, methyl formate, methyl acetate, ethyl acetate, propyl acetate, methyl propionate, ethyl propionate, propyl propionate, methyl butyrate, ethyl butyrate At least one of ester, 1,4-butyrolactone, sulfolane, dimethyl sulfone, methyl ethyl sulfone and diethyl sulfone.
  • the electrolyte may optionally include additives.
  • additives may include negative electrode film-forming additives, positive electrode film-forming additives, and additives that can improve certain performances of the battery, such as additives that improve battery overcharge performance, additives that improve high-temperature or low-temperature performance of batteries, and the like.
  • a secondary battery in one embodiment of the present application, includes a positive electrode, a negative electrode, an electrolyte, and a separator.
  • active ions are intercalated and extracted back and forth between the positive and negative electrodes.
  • the electrolyte plays a role of conducting ions between the positive electrode and the negative electrode.
  • the separator is arranged between the positive pole piece and the negative pole piece, which mainly plays a role in preventing the short circuit of the positive and negative poles, and at the same time allows ions to pass through.
  • the positive electrode, the negative electrode, and the separator can be fabricated into an electrode assembly through a winding process or a lamination process.
  • the secondary battery may include an outer package.
  • the outer package can be used to package the above-mentioned electrode assembly and electrolyte.
  • the outer packaging of the secondary battery may be a hard case, such as a hard plastic case, aluminum case, steel case, and the like.
  • the outer packaging of the secondary battery may also be a soft bag, such as a bag-type soft bag.
  • the material of the soft case may be plastic, and examples of the plastic include polypropylene, polybutylene terephthalate, polybutylene succinate, and the like.
  • FIG. 3 shows a square-shaped secondary battery 5 as an example.
  • the outer package may include a housing 51 and a cover 53 .
  • the housing 51 may include a bottom plate and a side plate connected to the bottom plate, and the bottom plate and the side plates enclose to form an accommodating cavity.
  • the housing 51 has an opening communicating with the accommodating cavity, and the cover plate 53 can cover the opening to close the accommodating cavity.
  • the positive pole piece, the negative pole piece and the separator can be formed into an electrode assembly 52 through a winding process or a lamination process.
  • the electrode assembly 52 is packaged in the accommodating chamber. Electrolyte is infiltrated in the electrode assembly 52 .
  • the number of electrode assemblies 52 contained in the secondary battery 5 can be one or more, and those skilled in the art can select according to specific actual needs.
  • the secondary battery can be assembled into a battery module, and the number of secondary batteries contained in the battery module can be one or more, and the specific number can be selected by those skilled in the art according to the application and capacity of the battery module.
  • FIG. 5 is a battery module 4 as an example.
  • a plurality of secondary batteries 5 may be arranged in sequence along the length direction of the battery module 4 .
  • the plurality of secondary batteries 5 may be fixed by fasteners.
  • the battery module 4 may also include a case having a housing space in which a plurality of secondary batteries 5 are accommodated.
  • the above-mentioned battery modules can also be assembled into a battery pack, and the number of battery modules contained in the battery pack can be one or more, and the specific number can be selected by those skilled in the art according to the application and capacity of the battery pack.
  • the battery pack 1 may include a battery box and a plurality of battery modules 4 disposed in the battery box.
  • the battery box includes an upper box body 2 and a lower box body 3 , the upper box body 2 can cover the lower box body 3 and form a closed space for accommodating the battery module 4 .
  • Multiple battery modules 4 can be arranged in the battery box in any manner.
  • the present application also provides an electric device, which includes at least one of the secondary battery, battery module, or battery pack provided in the present application.
  • the secondary battery, battery module, or battery pack can be used as a power source of the electric device, and can also be used as an energy storage unit of the electric device.
  • the electric devices may include mobile devices (such as mobile phones, notebook computers, etc.), electric vehicles (such as pure electric vehicles, hybrid electric vehicles, plug-in hybrid electric vehicles, electric bicycles, electric scooters, electric golf carts, etc.) , electric trucks, etc.), electric trains, ships and satellites, energy storage systems, etc., but not limited thereto.
  • a secondary battery, a battery module or a battery pack can be selected according to its usage requirements.
  • FIG. 8 is an example of an electrical device.
  • the electric device is a pure electric vehicle, a hybrid electric vehicle, or a plug-in hybrid electric vehicle.
  • a battery pack or a battery module may be used.
  • a device may be a cell phone, tablet, laptop, or the like.
  • the device is generally required to be light and thin, and a secondary battery can be used as a power source.
  • step 1) coating the first coating slurry and step 2) coating the second coating slurry at 60°C for 1 hour to form the first coating on both surfaces of the PE base film. layer and a second coating to prepare a barrier film.
  • the positive electrode active material LiNi 0.6 Co 0.2 Mn 0.2 O 2 , the positive electrode binder PVDF, and the conductive carbon in a mass ratio of 97:1.07:1.93, dissolve them in NMP, and stir for 6 hours to obtain the positive electrode slurry. Coating on aluminum foil, drying, and cold pressing to prepare positive electrode.
  • the ratio of the mass content w1 of the first polar substance in the first coating to the mass content m1 of the positive electrode binder in the film layer of the positive electrode It is 75:1.
  • the ratio of the mass content w of the second polar substance in the second coating to the mass content m of the negative electrode binder in the film layer of the negative electrode It is 30:1.
  • the positive electrode, the separator, and the negative electrode are stacked in order, wherein the first coating of the separator is in contact with the positive electrode, and the second coating of the separator is in contact with the negative electrode, and then wound to obtain a bare cell.
  • Embodiment 1-2
  • the preparation process of the lithium-ion battery refers to Example 1-1 as a whole.
  • the difference is that the mass ratio of the positive electrode active material LiNi 0.6 Co 0.2 Mn 0.2 O 2 , the positive electrode binder PVDF, and the conductive carbon is 97:1:2;
  • the mass ratio of the active material carbon-silicon mixture, the binder for the negative electrode, and the carbon nanotube is 97:2.5:0.5.
  • the ratio of the mass content w1 of the first polar substance in the first coating to the mass content m1 of the positive electrode binder in the film layer of the positive electrode It is 80:1.
  • the ratio of the mass content w of the second polar substance in the second coating to the mass content m of the negative electrode binder in the film layer of the negative electrode It is 32:1.
  • Embodiment 1-3
  • the preparation process of the lithium-ion battery refers to Example 1-1 as a whole.
  • the difference is that the mass ratio of the positive electrode active material LiNi 0.6 Co 0.2 Mn 0.2 O 2 , the positive electrode binder PVDF, and the conductive carbon is 97:0.91:2.09;
  • the mass ratio of the active material carbon-silicon mixture, the binder for the negative electrode, and the carbon nanotube is 97:2.2:0.8.
  • the ratio of the mass content w1 of the first polar substance in the first coating to the mass content m1 of the positive electrode binder in the film layer of the positive electrode It is 87:1.
  • the ratio of the mass content w of the second polar substance in the second coating to the mass content m of the negative electrode binder in the film layer of the negative electrode It is 36:1.
  • Embodiment 1-4
  • the preparation process of the lithium-ion battery refers to Example 1-1 as a whole.
  • the mass ratio of the positive electrode active material LiNi 0.6 Co 0.2 Mn 0.2 O 2 , the positive electrode binder PVDF, and the conductive carbon is 97:0.86:2.14; the negative electrode active material carbon
  • the mass ratio of the silicon mixture, the binder for the negative electrode, and the carbon nanotubes is 97:2:1.
  • the ratio of the mass content w1 of the first polar substance in the first coating to the mass content m1 of the positive electrode binder in the film layer of the positive electrode It is 93:1.
  • the ratio of the mass content w of the second polar substance in the second coating to the mass content m of the negative electrode binder in the film layer of the negative electrode It is 40:1.
  • Embodiment 1-5 are identical to Embodiment 1-5:
  • the preparation process of the lithium-ion battery refers to Example 1-1 as a whole, the difference is that the mass ratio of the positive electrode active material LiNi 0.6 Co 0.2 Mn 0.2 O 2 , the positive electrode binder PVDF, and the conductive carbon is 97:0.82:2.18; the negative electrode The mass ratio of the active material carbon-silicon mixture, the binder for the negative electrode, and the carbon nanotube is 97:1.77:1.23.
  • the ratio of the mass content w1 of the first polar substance in the first coating to the mass content m1 of the positive electrode binder in the film layer of the positive electrode It is 97:1.
  • the ratio of the mass content w of the second polar substance in the second coating to the mass content m of the negative electrode binder in the film layer of the negative electrode It is 45:1.
  • Embodiment 1-6
  • the preparation process of the lithium-ion battery refers to Example 1-1 as a whole, the difference is that the mass ratio of the positive electrode active material LiNi 0.6 Co 0.2 Mn 0.2 O 2 , the positive electrode binder PVDF, and the conductive carbon is 97:0.8:2.2; the negative electrode The mass ratio of the active material carbon-silicon mixture, the binder for the negative electrode, and the carbon nanotube is 97:1.6:1.4.
  • the ratio of the mass content w1 of the first polar substance in the first coating to the mass content m1 of the positive electrode binder in the film layer of the positive electrode It is 100:1.
  • the ratio of the mass content w of the second polar substance in the second coating to the mass content m of the negative electrode binder in the film layer of the negative electrode It is 50:1.
  • Embodiment 1-7 is a diagrammatic representation of Embodiment 1-7.
  • the preparation process of the lithium-ion battery refers to Example 1-1 as a whole, the difference is that the positive electrode active material LiNi 0.6 Co 0.2 Mn 0.2 O 2 , the positive electrode binder PVDF, and the conductive carbon are mixed according to the mass ratio of 97:0.76:2.24; The negative electrode active material carbon silicon mixture, the negative electrode binder, and the carbon nanotubes are mixed in a mass ratio of 97:1.5:1.5.
  • the ratio of the mass content w1 of the first polar substance in the first coating to the mass content m1 of the positive electrode binder in the film layer of the positive electrode It is 105:1.
  • the ratio of the mass content w of the second polar substance in the second coating to the mass content m of the negative electrode binder in the film layer of the negative electrode It is 53:1.
  • step 1) coating the first coating slurry and step 2) coating the second coating slurry at 60°C for 1 hour to form the first coating on both surfaces of the PE base film. layer and a second coating to prepare a barrier film.
  • the ratio of the mass content w 1 of the first polar substance in the first coating to the mass content w 2 of the second polar substance in the second coating It is 1:0.8.
  • the positive electrode active material LiNi 0.6 Co 0.2 Mn 0.2 O 2 , the positive electrode binder PVDF, and the conductive carbon were mixed according to the mass ratio of 97:1:2, and dissolved in NMP, stirred for 6 hours to obtain the positive electrode slurry, and the positive electrode slurry was Coating on aluminum foil, drying, and cold pressing to prepare positive electrode.
  • the positive electrode, separator, and negative electrode are stacked in order, wherein the first coating of the separator is in contact with the positive electrode, the second coating of the separator is in contact with the negative electrode, and then wound to obtain a bare cell. Put the bare cell into the aluminum shell, weld the top cover, and go through liquid injection, high temperature standing, formation, aging, and other processes to obtain a lithium-ion battery.
  • Example 2-1 It is basically the same as Example 2-1, except that the mass ratio of the first polar substance PAM to alumina is 85:15; the mass ratio of the second polar substance PEO to alumina is 85:15.
  • the ratio of the mass content w1 of the first polar substance in the first coating to the mass content w2 of the second polar substance in the second coating It is 1:1.
  • Embodiment 2-3 is a diagrammatic representation of Embodiment 2-3.
  • the preparation process of the lithium-ion battery refers to Example 2-1 as a whole, the difference is that the mass ratio of the first polar substance PAM to alumina is 71.1:28.9; the mass ratio of the second polar substance PEO to alumina is 92.5: 7.5.
  • the ratio of the mass content w1 of the first polar substance in the first coating to the mass content w2 of the second polar substance in the second coating It is 1:1.3.
  • Embodiment 2-4
  • the preparation process of the lithium-ion battery refers to Example 2-1 as a whole, the difference is that the mass ratio of the first polar substance PAM to alumina is 65:35; the mass ratio of the second polar substance PEO to alumina is 97.5: 2.5.
  • the ratio of the mass content w1 of the first polar substance in the first coating to the mass content w2 of the second polar substance in the second coating It is 1:1.5.
  • step 1) coating the first coating slurry and step 2) coating the second coating slurry at 60°C for 1 hour to form the first coating on both surfaces of the PE base film. layer and a second coating to prepare a barrier film.
  • the positive electrode active material LiNi 0.6 Co 0.2 Mn 0.2 O 2 , the positive electrode binder PVDF, and conductive carbon according to the mass ratio of 97:0.8:2.2, and dissolve them in NMP to obtain the positive electrode slurry, stir for 6 hours, and mix the positive electrode slurry
  • the material is coated on an aluminum foil, dried, and cold pressed to prepare a positive electrode.
  • the positive electrode, the separator, and the negative electrode are stacked in order, wherein the first coating of the separator is in contact with the positive electrode, and the second coating of the separator is in contact with the negative electrode, and then wound to obtain a bare cell.
  • the preparation process of the lithium-ion battery refers to Example 3-1 as a whole, the difference is that the mass ratio of the first polar substance polyurea in the first coating is 80%; the second polar substance PAM is in the second coating The mass proportion in is 80%.
  • the mass ratio of the positive electrode active material LiNi 0.6 Co 0.2 Mn 0.2 O 2 , the positive electrode binder PVDF, and the conductive carbon is 97:0.9:2.3.
  • the mass ratio of the negative electrode active material carbon-silicon mixture, the binder for the negative electrode, and the carbon nanotube is 97:2:1.
  • Embodiment 3-3 is a diagrammatic representation of Embodiment 3-3.
  • the preparation process of the lithium-ion battery refers to Example 3-1 as a whole, the difference is that the mass ratio of the first polar substance polyurea in the first coating is 85%; the second polar substance PAM is in the second coating The mass proportion in is 85%.
  • the mass ratio of the positive electrode active material LiNi 0.6 Co 0.2 Mn 0.2 O 2 , the positive electrode binder PVDF, and the conductive carbon is 97:1:2.
  • the mass ratio of the negative electrode active material carbon-silicon mixture, the binder for the negative electrode, and the carbon nanotube is 97:2.6:0.4.
  • Embodiment 3-4 is a diagrammatic representation of Embodiment 3-4.
  • the preparation process of the lithium-ion battery refers to Example 3-1 as a whole, the difference is that the mass ratio of the first polar substance polyurea in the first coating is 90%; the second polar substance PAM is in the second coating The mass proportion in is 90%.
  • the mass ratio of the positive electrode active material LiNi 0.6 Co 0.2 Mn 0.2 O 2 , the positive electrode binder PVDF, and the conductive carbon is 97:1.2:1.8.
  • the mass ratio of the negative electrode active material carbon-silicon mixture, the binder for the negative electrode, and the carbon nanotube is 97:3:0.
  • Embodiment 3-5
  • the preparation process of the lithium-ion battery refers to Example 3-1 as a whole, the difference is that the mass ratio of the first polar substance polyurea in the first coating is 92%; the second polar substance PAM is in the second coating The mass proportion in is 92%.
  • the mass ratio of the positive electrode active material LiNi 0.6 Co 0.2 Mn 0.2 O 2 , the positive electrode binder PVDF, and the conductive carbon is 97:1.5:0.5.
  • the mass ratio of the negative electrode active material carbon-silicon mixture, the binder for the negative electrode, and the carbon nanotube is 96.8:3.2:0.
  • step 1) coating the first coating slurry and step 2) coating the second coating slurry at 60°C for 1 hour to form the first coating on both surfaces of the PE base film. layer and a second coating to prepare a barrier film.
  • the ratio of the mass content k 1 of the first reinforcing agent in the first coating to the mass content k 2 of the second reinforcing agent in the second coating It is 0.7:1.
  • the positive electrode active material LiNi 0.6 Co 0.2 Mn 0.2 O 2 , the positive electrode binder PVDF, and the conductive carbon were mixed according to the mass ratio of 97:1:2, and dissolved in NMP, stirred for 6 hours to obtain the positive electrode slurry, and the positive electrode slurry was Coating on aluminum foil, drying, and cold pressing to prepare positive electrode.
  • the positive electrode, separator, and negative electrode are stacked in order, wherein the first coating of the separator is in contact with the positive electrode, the second coating of the separator is in contact with the negative electrode, and then wound to obtain a bare cell. Put the bare cell into the aluminum shell, weld the top cover, and go through liquid injection, high temperature standing, formation, aging, and other processes to obtain a lithium-ion battery.
  • the preparation process of the lithium-ion battery is generally referred to in Example 4-1, except that the mass ratio of the first polar substance PEO, the first enhancer PVDF, and alumina is 80:16.6:3.4.
  • the ratio of the mass content k 1 of the first reinforcing agent in the first coating to the mass content k 2 of the second reinforcing agent in the second coating It is 0.8:1.
  • Embodiment 4-3 is a diagrammatic representation of Embodiment 4-3.
  • the preparation process of the lithium-ion battery is generally referred to in Example 4-1, except that the mass ratio of the first polar substance PEO, the first enhancer PVDF, and alumina is 80:18:2.
  • the ratio of the mass content k 1 of the first reinforcing agent in the first coating to the mass content k 2 of the second reinforcing agent in the second coating It is 0.9:1.
  • Embodiment 4-4 is a diagrammatic representation of Embodiment 4-4:
  • the preparation process of the lithium-ion battery is generally referred to in Example 4-1, except that the mass ratio of the first polar substance PEO, the first enhancer PVDF, and alumina is 80:19:1.
  • the ratio of the mass content k 1 of the first reinforcing agent in the first coating to the mass content k 2 of the second reinforcing agent in the second coating It is 0.95:1.
  • Embodiment 4-5
  • the manufacturing process of the lithium-ion battery is generally referred to in Example 4-1, except that the mass ratio of the first polar substance PEO to the first enhancer PVDF is 80:20.
  • the ratio of the mass content k 1 of the first reinforcing agent in the first coating to the mass content k 2 of the second reinforcing agent in the second coating It is 1:1.
  • step 1) coating the first coating slurry and step 2) coating the second coating slurry at 60°C for 1 hour to form the first coating on both surfaces of the PE base film. layer and a second coating to prepare a barrier film.
  • the mass ratio of the mass content w 1 of the first polar substance in the first coating to the mass content k 1 of the first reinforcing agent in the first coating is 4.6:1;
  • the second coating includes a second reinforcing agent, the mass content of the second polar substance in the second coating w 2 and the mass content k 2 of the second reinforcing agent in the second coating Compare It is 4.9:1.
  • the positive electrode active material LiNi 0.6 Co 0.2 Mn 0.2 O 2 , the positive electrode binder PVDF, and the conductive carbon were mixed according to the mass ratio of 97:1:2, and dissolved in NMP, stirred for 6 hours to obtain the positive electrode slurry, and the positive electrode slurry was Coating on aluminum foil, drying, and cold pressing to prepare positive electrode.
  • the positive electrode, the separator, and the negative electrode are stacked in order, wherein the first coating of the separator is in contact with the positive electrode, and the second coating of the separator is in contact with the negative electrode, and then wound to obtain a bare cell.
  • the preparation process of the lithium-ion battery is generally referred to in Example 5-1, except that the mass ratio of the first polar substance PAM, the first enhancer PVDF, and alumina is 80:16:4.
  • the mass ratio of the second polar substance PEO to the second reinforcing agent PVDF is 83.4:16.6.
  • the mass ratio of the mass content w 1 of the first polar substance in the first coating to the mass content k 1 of the first reinforcing agent in the first coating is 5:1; the mass ratio of the mass content w2 of the second polar substance in the second coating to the mass content k2 of the second reinforcing agent in the second coating It is 5:1.
  • Embodiment 5-3 is a diagrammatic representation of Embodiment 5-3.
  • the preparation process of the lithium-ion battery is generally referred to in Example 5-1, except that the mass ratio of the first polar substance PAM, the first enhancer PVDF, and alumina is 80:15:5.
  • the mass ratio of the second polar substance PEO, the second reinforcing agent PVDF, and alumina is 84.2:15.8.
  • the mass ratio of the mass content w 1 of the first polar substance in the first coating to the mass content k 1 of the first reinforcing agent in the first coating is 5.3:1; the mass ratio of the mass content w 2 of the second polar substance in the second coating to the mass content k 2 of the second reinforcing agent in the second coating It is 5.3:1.
  • Embodiment 5-4 is a diagrammatic representation of Embodiment 5-4:
  • the preparation process of the lithium-ion battery is generally referred to in Example 5-1, except that the mass ratio of the first polar substance PAM, the first enhancer PVDF, and alumina is 80:13.3:6.7.
  • the mass ratio of the second polar substance PEO to the second reinforcing agent PVDF is 86:14.
  • the mass ratio of the mass content w 1 of the first polar substance in the first coating to the mass content k 1 of the first reinforcing agent in the first coating is 6:1; the mass ratio of the mass content w 2 of the second polar substance in the second coating to the mass content k 2 of the second reinforcing agent in the second coating It is 6:1.
  • Embodiment 5-5 is a diagrammatic representation of Embodiment 5-5:
  • the preparation process of the lithium-ion battery is generally referred to in Example 5-1, except that the mass ratio of the first polar substance PAM, the first enhancer PVDF, and alumina is 80:10:10.
  • the mass ratio of the second polar substance PEO to the second reinforcing agent PVDF is 89:11.
  • the mass ratio of the mass content w 1 of the first polar substance in the first coating to the mass content k 1 of the first reinforcing agent in the first coating is 8:1; the mass ratio of the mass content w 2 of the second polar substance in the second coating to the mass content k 2 of the second reinforcing agent in the second coating It is 8:1.
  • Embodiment 5-6 is a diagrammatic representation of Embodiment 5-6.
  • the preparation process of the lithium-ion battery is generally referred to in Example 5-1, except that the mass ratio of the first polar substance PAM, the first enhancer PVDF, and alumina is 80:8.9:11.1.
  • the mass ratio of the second polar substance PEO, the second reinforcing agent PVDF, and aluminum oxide is 90:10.
  • the mass ratio of the mass content w 1 of the first polar substance in the first coating to the mass content k 1 of the first reinforcing agent in the first coating is 9:1;
  • the second coating includes a second reinforcing agent, the mass content of the second polar substance in the second coating w 2 and the mass content k 2 of the second reinforcing agent in the second coating Compare It is 9:1.
  • Embodiment 5-7
  • the preparation process of the lithium-ion battery is generally referred to in Example 5-1, except that the mass ratio of the first polar substance PAM, the first enhancer PVDF, and alumina is 80:8.6:11.4.
  • the mass ratio of the second polar substance PEO to the second reinforcing agent PVDF is 90.3:9.7.
  • the mass ratio of the mass content w 1 of the first polar substance in the first coating to the mass content k 1 of the first reinforcing agent in the first coating is 9.3:1;
  • the second coating includes a second reinforcing agent, the mass content of the second polar substance in the second coating w 2 and the mass content k 2 of the second reinforcing agent in the second coating Compare It is 9.3:1.
  • step 1) coating the first coating slurry and step 2) coating the second coating slurry at 60°C for 1 hour to form the first coating on both surfaces of the PE base film. layer and a second coating to prepare a barrier film.
  • the positive electrode active material LiNi 0.6 Co 0.2 Mn 0.2 O 2 , the positive electrode binder PVDF, and the conductive carbon were mixed according to the mass ratio of 97:1:2, and dissolved in NMP, stirred for 6 hours to obtain the positive electrode slurry, and the positive electrode slurry was Coating on aluminum foil, drying, and cold pressing to prepare positive electrode.
  • the positive electrode, separator, and negative electrode are stacked in order, wherein the first coating of the separator is in contact with the positive electrode, the second coating of the separator is in contact with the negative electrode, and then wound to obtain a bare cell. Put the bare cell into the aluminum shell, weld the top cover, and go through liquid injection, high temperature standing, formation, aging, and other processes to obtain a lithium-ion battery.
  • Embodiment 6-2
  • the mass ratio of the tubes is 96.7:2.5:0.8.
  • Embodiment 6-3
  • Example 6-1 It is basically the same as Example 6-1, except that the mass ratio of negative electrode active material carbon-silicon mixture (Si particle size is 0.3 ⁇ m), negative electrode binder, and carbon nanotubes is 97:2.5:0.5.
  • Embodiment 6-4
  • the tubes are in a mass ratio of 96.8:2.5:0.7.
  • Embodiment 6-5 is a diagrammatic representation of Embodiment 6-5:
  • the preparation process of the lithium-ion battery refers to Example 6-1 as a whole.
  • the difference is that the negative electrode active material carbon-silicon mixture (the particle size of Si is 0.6 ⁇ m), the binder for the negative electrode, and the carbon nanotubes are in a mass ratio of 96:2.5 : 1.5.
  • step 1) coating the first coating slurry and step 2) coating the second coating slurry at 60°C for 1 hour to form the first coating on both surfaces of the PE base film. layer and a second coating to prepare a barrier film.
  • the positive electrode active material LiNi 0.4 Co 0.4 Mn 0.2 O 2 , the positive electrode binder PVDF, and the conductive carbon were mixed according to the mass ratio of 97:1:2, and dissolved in NMP, and stirred for 6 hours to obtain the positive electrode slurry. Coating on aluminum foil, drying, and cold pressing to prepare positive electrode.
  • the positive electrode, separator, and negative electrode are stacked in order, wherein the first coating of the separator is in contact with the positive electrode, the second coating of the separator is in contact with the negative electrode, and then wound to obtain a bare cell. Put the bare cell into the aluminum shell, weld the top cover, and go through liquid injection, high temperature standing, formation, aging, and other processes to obtain a lithium-ion battery.
  • Embodiment 7-2 is a diagrammatic representation of Embodiment 7-2.
  • the preparation process of the lithium-ion battery is generally referred to in Example 7-1, except that the positive electrode active material is LiNi 0.5 Co 0.2 Mn 0.3 O 2 .
  • Embodiment 7-3 is a diagrammatic representation of Embodiment 7-3.
  • the preparation process of the lithium-ion battery is generally referred to in Example 7-1, the difference is that the positive electrode active material is LiNi 0.6 Co 0.2 Mn 0.2 O 2 .
  • Embodiment 7-4 is a diagrammatic representation of Embodiment 7-4:
  • the preparation process of the lithium-ion battery is generally referred to in Example 7-1, except that the positive active material is LiNi 0.8 Co 0.1 Mn 0.1 O 2 .
  • Embodiment 7-5 is a diagrammatic representation of Embodiment 7-5:
  • the preparation process of the lithium-ion battery is generally referred to in Example 7-1, except that the positive active material is LiNi 0.9 Co 0.05 Mn 0.05 O 2 .
  • step 1) coating the first coating slurry and step 2) coating the second coating slurry at 60°C for 1 hour to form the first coating on both surfaces of the PE base film. layer and a second coating to prepare a barrier film.
  • the positive electrode active material LiNi 0.4 Co 0.4 Mn 0.4 O 2 , the positive electrode binder PVDF, and the conductive carbon were mixed according to the mass ratio of 97:1:2, and dissolved in NMP, stirred for 6 hours to obtain the positive electrode slurry, and the positive electrode slurry was Coating on aluminum foil, drying, and cold pressing to prepare positive electrode.
  • the positive electrode, separator, and negative electrode are stacked in order, wherein the first coating of the separator is in contact with the positive electrode, the second coating of the separator is in contact with the negative electrode, and then wound to obtain a bare cell. Put the bare cell into the aluminum shell, weld the top cover, and go through liquid injection, high temperature standing, formation, aging, and other processes to obtain a lithium-ion battery.
  • Example 8-1 The preparation process of the lithium-ion battery is generally referred to in Example 8-1, the difference is that the mass ratio of PEO and PAM in the first polar material is 2:1; the mass ratio of PEI and PEO in the first polar material is 2:1.
  • Embodiment 8-3 is a diagrammatic representation of Embodiment 8-3.
  • Example 8-1 The preparation process of the lithium-ion battery is generally referred to in Example 8-1, the difference is that the mass ratio of PEO and PAM in the first polar material is 3:1; the mass ratio of PEI and PEO in the first polar material is 3:1.
  • Embodiment 8-4 is a diagrammatic representation of Embodiment 8-4:
  • Example 8-1 The preparation process of the lithium ion battery is generally referred to in Example 8-1, the difference is that the mass ratio of PEO and PAM in the first polar material is 4.5:1; the mass ratio of PEI and PEO in the first polar material is 4.5:1.
  • Embodiment 8-5 is a diagrammatic representation of Embodiment 8-5:
  • Example 8-1 The preparation process of the lithium ion battery is generally referred to in Example 8-1, the difference is that the mass ratio of PEO and PAM in the first polar material is 5:1; the mass ratio of PEI and PEO in the first polar material is 5:1.
  • Embodiment 8-6 is a diagrammatic representation of Embodiment 8-6:
  • Example 8-1 The preparation process of the lithium-ion battery is generally referred to in Example 8-1, the difference is that the mass ratio of PEO and PAM in the first polar material is 6:1; the mass ratio of PEI and PEO in the first polar material is 6:1.
  • Embodiment 8-7
  • Example 8-1 The preparation process of the lithium-ion battery is generally referred to in Example 8-1, the difference is that the mass ratio of PEO and PAM in the first polar material is 6.3:1; the mass ratio of PEI and PEO in the first polar material is 6.3:1.
  • the preparation process of the lithium-ion battery is generally referred to in Example 1-2, except that the first polar substance PEO and the second polar substance PEI are not contained.
  • the preparation process of the lithium-ion battery is generally referred to in Example 1-2, the difference is that PEO in the first polar substance is not contained, and the proportion of PEI in the second polar substance in the second coating is 100%.
  • the preparation process of the lithium ion battery is generally referred to in Example 1-2, the difference is that PEI in the second polar substance is not contained, and the proportion of the first polar substance PEO in the first coating is 100%.
  • the separators of the embodiment and the comparative example were respectively cut into test samples with a length of 100 mm and a width of 10 mm. Take a stainless steel plate with a width of 25mm, paste it with double-sided adhesive tape (width 11mm), paste the test sample on the double-sided adhesive tape on the stainless steel plate, and use a 2000g pressure roller to roll back and forth on its surface three times (300mm/min).
  • the standard GB/T6040-2002 infrared spectroscopic analysis method an IS10 Fourier transform infrared spectrometer from Nicolet Company of the United States was used.
  • the positive electrode slurry obtained in the examples and comparative examples is suction-filtered to obtain the positive electrode powder; the first coating slurry obtained in the examples and comparative examples is coated on the PE base film, and after suction filtration, the PE base film is removed, The first coating powder is obtained.
  • the positive electrode powder and the first coating powder are mixed, and the mixed powder is obtained after further drying; the mixed powder is subjected to an infrared test.
  • the infrared test method between the second coating and the negative electrode is the same as above.
  • High-rate discharge capacity In an environment of 25°C, charge the batteries of all examples and comparative examples at a charging current of 1/3C with constant current and constant voltage until the upper limit voltage is 4.35V. Then, perform constant current discharge at 1/3C, 3C, 5C discharge current until the final voltage is 2.8V, and record the discharge capacity value at this time.
  • Embodiment 1-1 ⁇ 1-7 is adjusted by as well as Battery performance such as cycle expansion rate, cycle 1000 cycle capacity retention rate and 5C discharge capacity have achieved good results, especially In (80 ⁇ 100): 1, When (32 ⁇ 50):1, the battery performance is better.
  • Embodiment 2-1 ⁇ 2-4 is adjusted by Battery performance such as cycle expansion rate, cycle 1000 cycle capacity retention rate and 5C discharge capacity have achieved good results, especially In the range of 1: (1 ⁇ 1.3), the battery performance is better.
  • Examples 3-1 to 3-5 comprehensively adjust the mass content w 1 of the first polar substance in the first coating layer and the mass content m of the positive electrode binder in the positive film layer 1.
  • Examples 4-1 to 4-5 are adjusted by adjusting the mass ratio of the mass content k 1 of the first reinforcing agent in the first coating to the mass content k 2 of the second reinforcing agent in the second coating , battery performance such as cycle expansion rate, cycle 1000 cycle capacity retention rate and 5C discharge capacity have achieved good results, especially In the range of (0.8-1):1, the battery performance is better.
  • Examples 5-1 to 5-7 were adjusted by adjusting the mass content w 1 of the first polar substance in the first coating and the mass content k 1 of the first reinforcing agent in the first coating. Compare The mass ratio of the mass content w2 of the second polar substance in the second coating to the mass content k2 of the second reinforcing agent in the second coating Hydrogen bonds are easily formed between the enhancer and the polar substance, which can reduce the expansion of the bare cell, thereby improving battery performance. Battery performance such as cycle expansion rate, cycle 1000 cycle capacity retention rate and 5C discharge capacity have achieved good results, especially All in the range of (5-9):1, the performance of the battery is better.
  • Examples 6-1 to 6-5 reflect the influence of silicon particle size on battery performance.
  • Battery performance such as cycle expansion rate, 1000-cycle capacity retention rate and 5C discharge capacity have all achieved good results, especially when the particle size of silicon is in the range of 0.1-0.5 microns, the battery performance is even better.
  • the first polar substance is PEO
  • the first reinforcing agent is PVDF
  • the binder for the positive electrode is PEO
  • the second polar substance is PEI
  • the second reinforcing agent is PVDF
  • the binder for the negative electrode is PEO.
  • the agents are SA and SBR
  • the negative electrode active material is a carbon-silicon mixture.
  • F on the positive electrode binder PVDF and H on the first polar substance PEO form a hydrogen bond.
  • F on the first reinforcing agent PVDF forms hydrogen bonds with H on the first polar substance PEO.
  • the H on the -OH in the carbon-silicon mixture is more electron-deficient than the H on the -NH 2 , therefore, the second polar substance PEI on the -NH 2
  • the N in the carbon-silicon mixture easily forms a hydrogen bond with the H on the -OH.
  • the N on -NH 2 in the second polar substance PEI forms a hydrogen bond with the H on -COOH in the negative electrode binder SA. Hydrogen bonds can be formed between the H on -OH in the carbon-silicon mixture and the H on -COOH in SA.
  • the F of the second reinforcing agent PVDF forms hydrogen bonds with the H of PEI.
  • the present application is not limited to the above-mentioned embodiments.
  • the above-mentioned embodiments are merely examples, and within the scope of the technical solutions of the present application, embodiments that have substantially the same configuration as the technical idea and exert the same effects are included in the technical scope of the present application.
  • various modifications conceivable by those skilled in the art are added to the embodiments, and other forms constructed by combining some components in the embodiments are also included in the scope of the present application. .

Landscapes

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

Abstract

本申请提供了一种电池、电池模块、电池包和用电装置，所述电池包括正极、隔离膜、负极，所述隔离膜包括基膜、设于所述基膜第一表面的第一涂层、以及设于所述基膜第二表面的第二涂层，其中，所述第一涂层中包括第一极性物质，所述第一极性物质与正极用粘结剂之间具有氢键；所述第二极性物质与负极用粘结剂和/或负极活性组分之间具有氢键。本申请通过氢键可以增强隔离膜与正极和负极之间的粘结力，减少裸电芯的循环膨胀率，提高电池的高倍率放电性能、循环性能。

Description

一种电池、电池模块、电池包和用电装置 技术领域
本申请涉及锂电池技术领域，尤其涉及一种电池、电池模块、电池包和用电装置。
背景技术
近年来，随着锂离子电池的应用范围越来越广泛，锂离子电池广泛应用于水力、火力、风力和太阳能电站等储能电源系统，以及电动工具、电动自行车、电动摩托车、电动汽车、军事装备、航空航天等多个领域。由于锂离子电池取得了极大的发展，因此对其能量密度、群裕度、循环/倍率性能和安全性能等也提出了更高的要求。
另外，隔离膜是电池的组成成分之一，隔离膜可以有效防止正负极相接触而导致内部短路。但传统隔离膜与正极或负极并无氢键之间的连接，隔离膜与正极或负极仅是物理接触，因而容易导致裸电芯膨胀，不利于电芯整形。因此，现有的电池仍有待改进。
发明内容
本申请是鉴于上述课题而进行的，其目的在于，提供一种电池，以进一步提升电池综合性能(高倍率放电性能、循环性能)。
为了达到上述目的，本申请提供了一种电池、电池模块、电池包和用电装置。
本申请的第一方面提供了一种电池，所述电池包括正极、隔离膜、负极，所述隔离膜包括基膜、设于所述基膜第一表面的第一涂层、以及设于所述基膜第二表面的第二涂层，其中，所述第一涂层中包括第 一极性物质，所述第一极性物质包括聚烯烃酰胺类、聚烯烃亚胺类、聚氧化烯烃类、聚氨酯类、聚脲类物质中的一种或多种，所述第一极性物质与所述正极的正极用粘结剂之间具有氢键；所述第二涂层中包括第二极性物质，所述第二极性物质包括聚烯烃酰胺类、聚烯烃亚胺类、聚氧化烯烃类、聚氨酯类、聚脲类物质中的一种或多种，所述第二极性物质与所述负极的负极用粘结剂和/或负极活性组分之间具有氢键。
本申请中，可以将氢键用X-H-Y表示，其中，X、Y可分别独立选自N、O、F中的一种。正极用粘结剂(含-X)与第一极性物质(含-YH)间易形成氢键；同理，负极用粘结剂和/或负极活性组分(含-HX)与第二极性物质(含-YH)间也易形成氢键。因此，本申请通过氢键增强隔离膜与正极和负极间的粘结力，进而减少裸电芯在加工过程中的膨胀，以及数次循环后的循环膨胀率，提高电池的高倍率放电容量，缩短锂离子传输路径，提升电池的循环性能。
在任意实施方式中，所述第一涂层与所述正极的剥离力不低于0.075N，可选为0.075N～0.125N；所述第二涂层与所述负极的剥离力不低于0.075N，可选为0.075N～0.15N。由此，通过剥离力可以表征隔离膜与正负极间的粘结力大小。剥离力在合理范围内，裸电芯在加工过程中以及循环过程中均不易膨胀，隔离膜与正极、负极接触紧密，电池高倍率放电能力强。
在任意实施方式中，所述第一极性物质在所述第一涂层中的质量含量w 1与所述正极用粘结剂在所述正极的膜层中的质量含量m 1的比值
Figure PCTCN2021108971-appb-000001
为(80～100)∶1；所述第二极性物质在所述第二涂层中的质量含量w 2与所述负极用粘结剂在所述负极的膜层中的质量含量m 2的比值
Figure PCTCN2021108971-appb-000002
为(32～50)∶1。由此，通过限定
Figure PCTCN2021108971-appb-000003
以及
Figure PCTCN2021108971-appb-000004
数值在合理范围内，能够兼顾电池性能、成本的最优比，提升电池的高倍率放电容量和循环性能。
在任意实施方式中，所述第一极性物质在所述第一涂层中的质量含量w 1与所述第二极性物质在所述第二涂层中的质量含量w 2的比值
Figure PCTCN2021108971-appb-000005
为1∶(1～1.3)。由此，通过限定
Figure PCTCN2021108971-appb-000006
在合理范围内，可以使得隔离膜两侧张力一致，以防止张力不一致引发的电池内部的短路风险，且可以提高电池的循环性能。
在任意实施方式中，所述第一极性物质在所述第一涂层中的质量含量w 1为80％～90％，所述正极用粘结剂在所述正极的膜层中的质量含量m 1为0.9％～1.2％。所述第二极性物质在所述第二涂层中的质量含量w 2为80％～90％，所述负极用粘结剂在所述负极的膜层中的质量含量m 2为2％～3％。由此，通过将上述参数限定在合理范围内，使电池兼顾良好的高倍率放电性能和循环性能。
在任意实施方式中，所述第一极性物质包括聚氧化乙烯和聚丙烯酰胺；其中，所述聚氧化乙烯与聚丙烯酰胺的质量比值C1为(2～6)∶1。所述第二极性物质包括聚乙烯亚胺和聚氧化乙烯；其中，所述聚乙烯亚胺与聚氧化乙烯的质量比值C2为(2～6)∶1。由此，第一极性物质中，在聚氧化乙烯中混合少量聚丙烯酰胺长链分子，可以提高电池的循环稳定性。第二极性物质中，在极性强的聚乙烯亚胺中加入少量低成本的聚氧化乙烯，两者相互间也会形成氢键，进一步增强第二极性物质间的粘结力，从而进一步提高电池的高倍率放电性能和循 环性能。
在任意实施方式中，所述第一涂层包括第一增强剂，所述第一极性物质在所述第一涂层中的质量含量w1与所述第一增强剂在所述第一涂层中的质量含量k 1的质量之比
Figure PCTCN2021108971-appb-000007
为(5～9)∶1；所述第二涂层包括第二增强剂，所述第二极性物质在第二涂层中的质量含量w 2与所述第二增强剂在所述第二涂层中的质量含量k 2的质量之比
Figure PCTCN2021108971-appb-000008
为(5～9)∶1。由此，通过分别限定隔离膜上第一极性物质与第一增强剂的比例、第二极性物质与第二增强剂的比例在合理范围内，在第一增强剂与第一极性物质间以及第二增强剂与第二极性物质间可分别形成氢键，使裸电芯在加工过程中压实更紧密，多次循环充放电后裸电芯的循环膨胀率低，提升电池的高倍率放电性能和循环性能。
在任意实施方式中，所述第一增强剂在所述第一涂层中的质量含量k 1不高于所述第二增强剂在所述第二涂层中的质量含量k 2。由此，通过限定
Figure PCTCN2021108971-appb-000009
在合理范围内，可以保持隔离膜两侧张力一致，以防止张力不一致引发的电池内部短路，且可以提高电池的循环性能。
在任意实施方式中，所述第一增强剂在所述第一涂层中的质量含量k 1与所述第二增强剂在所述第二涂层中的质量含量k 2的比值
Figure PCTCN2021108971-appb-000010
为(0.8～1)∶1。由此，通过限定第一涂层和第二涂层中增强剂质量含量的比值在合理范围内，可以在提升隔离膜稳定性同时，对充放电过程中锂离子传输动力学影响较小，提高电池的循环性能和高倍率放电性能。
在任意实施方式中，所述第一增强剂或第二增强剂包括聚偏二氟 乙烯、海藻酸钠中的一种或多种。所述正极用粘结剂包括聚偏氟乙烯，所述负极用粘结剂包括丁苯橡胶、海藻酸钠中的一种以上。
在任意实施方式中，所述负极活性组分包括硅碳混合物，所述硅碳混合物中，硅的粒径为0.1～0.5微米，碳为人造石墨和天然石墨的混合碳，所述硅碳混合物在所述负极膜层中的含量为95％-97％。由此，通过限定硅的粒径在合理范围内，可以使得电池的循环性能更好，而通过限定硅碳混合物在所述负极膜层中的含量在合理范围内，可以实现电池的高倍率充放电性能。
在任意实施方式中，所述第一涂层和所述第二涂层的质量比为1∶(1～1.5)。由此，通过限定第一涂层和第二涂层的涂覆量在合理范围内，可以使得隔离膜张力一致，以防止张力不一致有短路风险，且可以提高电池的循环性能。
在任意实施方式中，所述第一涂层由第一涂层浆料制备获得，所述第一涂层浆料包括所述第一极性物质、所述第一增强剂和第一溶剂；其中，所述第一涂层浆料的粘度为8000mpa.s～12000mpa.s。所述第二涂层由第二涂层浆料制备获得，所述第二涂层浆料包括所述第二极性物质、所述第二增强剂和第二溶剂；其中，所述第二涂层浆料的粘度为5000mpa.s～20000mpa.s。由此，通过限定第一涂层浆料和第二涂层浆料分别在合适的粘度范围内，能够优化第一涂层浆料或第二涂层浆料的在基膜上的涂布工艺，改善涂布效果，以及保证电芯一致性良好，可以提高电池的循环性能和高倍率放电性能。
在任意实施方式中，所述正极包括正极材料LiNi xCo yMn zO 2， x+y+z＝1，x＝0.5～0.9；可选为x＝0.5～0.7，x＝0.8～0.9。本申请的隔离膜尤其对包含高镍正极材料的裸电芯的循环膨胀率改善效果显著，特别地，本申请的隔离膜对包含正极材料镍含量x＝0.5～0.7的裸电芯的循环膨胀率改善更为显著，因此对高镍电池的高倍率放电性能和循环性能改善更为显著。
本申请的第二方面提供一种电池模块，包括本申请的第一方面的电池。
本申请的第三方面提供一种电池包，包括本申请的第二方面的电池模块。
本申请的第四方面提供一种用电装置，包括选自本申请的第一方面的电池、本申请的第二方面的电池模块或本申请的第三方面的电池包中的至少一种。
相比于现有技术，本发明具有以下有益效果：
本申请第一极性物质与正极用粘结剂之间具有氢键，能够增强隔离膜与正极的粘结力。第二极性物质与负极用粘结剂和/或负极活性物质之间具有氢键，能够增加隔离膜与负极的粘结力。第一极性物质与第一增强剂之间具有氢键，能够增强隔离膜的第一涂层与基膜之间的粘结力。第二极性物质与第二增强剂之间具有氢键，能够增强隔离膜的第二涂层与基膜之间的粘结力。由此，本申请可以改善裸电芯在加工过程中的膨胀以及降低裸电芯循环过程中的循环膨胀率，有利于裸电芯整形，使得裸电芯更紧实，提高电池的高倍率放电性能和循环性能。
附图说明
图1是隔离膜上极性物质与正负极之间氢键形成的反应原理示意图。
图2是本申请实施例1-4和对比例1～3的红外表征示意图。
图3是本申请一实施方式的二次电池的示意图。
图4是图3所示的本申请一实施方式的二次电池的分解图。
图5是本申请一实施方式的电池模块的示意图。
图6是本申请一实施方式的电池包的示意图。
图7是图6所示的本申请一实施方式的电池包的分解图。
图8是本申请一实施方式的二次电池用作电源的用电装置的示意图。
附图标记说明：
1电池包；2上箱体；3下箱体；4电池模块；5二次电池；51壳体；52电极组件；53顶盖组件
具体实施方式
以下，适当地参照附图详细说明具体公开了本申请的电池、电池模块、电池包和电学装置的实施方式。但是会有省略不必要的详细说明的情况。例如，有省略对已众所周知的事项的详细说明、实际相同结构的重复说明的情况。这是为了避免以下的说明不必要地变得冗长，便于本领域技术人员的理解。此外，附图及以下说明是为了本领域技术人员充分理解本申请而提供的，并不旨在限定权利要求书所记载的主题。
本申请所公开的“范围”以下限和上限的形式来限定，给定范围是通过选定一个下限和一个上限进行限定的，选定的下限和上限限定了特别范围的边界。这种方式进行限定的范围可以是包括端值或不包 括端值的，并且可以进行任意地组合，即任何下限可以与任何上限组合形成一个范围。例如，如果针对特定参数列出了60-120和80-110的范围，理解为60-110和80-120的范围也是预料到的。此外，如果列出的最小范围值1和2，和如果列出了最大范围值3，4和5，则下面的范围可全部预料到：1-3、1-4、1-5、2-3、2-4和2-5。在本申请中，除非有其他说明，数值范围“a-b”表示a到b之间的任意实数组合的缩略表示，其中a和b都是实数。例如数值范围“0-5”表示本文中已经全部列出了“0-5”之间的全部实数，“0-5”只是这些数值组合的缩略表示。另外，当表述某个参数为≥2的整数，则相当于公开了该参数为例如整数2、3、4、5、6、7、8、9、10、11、12等。
如果没有特别的说明，本申请的所有实施方式以及可选实施方式可以相互组合形成新的技术方案。
如果没有特别的说明，本申请的所有技术特征以及可选技术特征可以相互组合形成新的技术方案。
如果没有特别的说明，本申请的所有步骤可以顺序进行，也可以随机进行，优选是顺序进行的。例如，所述方法包括步骤(a)和(b)，表示所述方法可包括顺序进行的步骤(a)和(b)，也可以包括顺序进行的步骤(b)和(a)。例如，所述提到所述方法还可包括步骤(c)，表示步骤(c)可以任意顺序加入到所述方法，例如，所述方法可以包括步骤(a)、(b)和(c)，也可包括步骤(a)、(c)和(b)，也可以包括步骤(c)、(a)和(b)等。
如果没有特别的说明，本申请所提到的“包括”和“包含”表示开放式，也可以是封闭式。例如，所述“包括”和“包含”可以表示还可以包括或包含没有列出的其他组分，也可以仅包括或包含列出的组分。
如果没有特别的说明，在本申请中，术语“或”是包括性的。举例来说，短语“A或B”表示“A，B，或A和B两者”。更具体地，以下任一条件均满足条件“A或B”：A为真(或存在)并且B为假(或不存在)；A为假(或不存在)而B为真(或存在)；或A和B都为真(或存在)。
经过长期制备锂离子电池的经验，本申请发明人发现：一方面，加工过程中，将正极、隔离膜、负极卷绕、压实成裸电芯，裸电芯虽然被在加工过程中已经被压实，但是经过一段时间，裸电芯本身会有反弹趋势，会造成裸电芯膨胀。另一方面，在循环过程中，负极活性材料本身，例如石墨晶格变大，石墨片之间层间距变大，会导致裸电芯厚度变厚，从而造成裸电芯膨胀。
基于上述两方面裸电芯膨胀的原因，裸电芯在膨胀之后，会产生气泡，破坏了电芯内部机构的界面稳定性，使得电解液会挤向极片边缘，造成析锂问题。另外，裸电芯膨胀之后，电芯的群裕度变小，会挤压铝壳变形，导致电池的循环能力下降，循环衰减变快，高倍率放电性能降低。
经过大量实验和研究，发明人发现，为了抑制裸电芯膨胀对电池性能的影响，可以从以下思路入手：第一方面，可以在隔离膜的基膜的表面涂覆极性物质，通过极性物质与正极用粘结剂、负极用粘结剂或负极活性物质之间形成氢键，从而增加隔离膜与正极、负极之间的粘结力。另一方面，可以在极性物质中混入一些增强剂，提高隔离膜的粘结力。因此，发明人从协同两方面的作用出发，通过对隔离膜进行综合改性，充分协同利用上述两方面的作用，设计出能够显著提高隔离膜与正极、负极粘结力的电池，并降低了裸电芯加工过程的膨胀以及循环使用过程中的循环膨胀率，大幅提高了电池的高倍率放电性 能以及循环性能。
电池
本申请的一个实施方式中，本申请提出了一种电池。
所述电池包括正极、隔离膜、负极和电解质，所述隔离膜包括基膜、设于所述基膜第一表面的第一涂层、以及设于所述基膜第二表面的第二涂层，其中，
所述第一涂层中包括第一极性物质，所述第一极性物质包括聚烯烃酰胺类、聚烯烃亚胺类、聚氧化烯烃类、聚氨酯类、聚脲类物质中的一种或多种，所述第一极性物质与所述正极的正极用粘结剂之间具有氢键；
所述第二涂层中包括第二极性物质，所述第二极性物质包括聚烯烃酰胺类、聚烯烃亚胺类、聚氧化烯烃类、聚氨酯类、聚脲类物质中的一种或多种，所述第二极性物质与所述负极的负极用粘结剂和/或负极活性组分之间具有氢键。
本申请隔离膜上的第一涂层是包括第一极性物质构成的具有预定厚度的结构，第一涂层能够通过第一极性物质与正极用粘结剂牢固的粘结，进而防止裸电芯加工过程中的膨胀以及循环使用过程中的循环膨胀率。
进一步的，第一极性物质例如聚烯烃酰胺类、聚烯烃亚胺类、聚氧化烯烃类、聚氨酯类、聚脲类等均包括极性官能团，一方面可以通过极性团能团与正极用粘结剂之间形成氢键，提高第一涂层与正极之间的粘结力；另一方面，第一极性物质本身就是粘结剂，也可以提高第一涂层与正极之间的粘结力。因此，通过前述第一极性物质中的极性官能团和以及第一极性物质本身是粘结剂两方面的作用，使得第一涂层与正极粘结的更为牢固。
具体的，本申请的第一极性物质带有YH基团，Y选自N、O、F中的一种。正极用粘结剂带有X基团，X选自N、O、F中的一种。这边带有X基团的正极用粘结剂能够与本申请的第一极性物质中的YH基团之间形成氢键X-H-Y，从而使得本申请的第一涂层与本申请的正极粘结的更牢固。更具体的，如图1，以正极用粘结剂含F为例说明，由于正极用粘结剂含F，因此正极用粘结剂与第一极性物质(-OH)易形成氢键。
本申请隔离膜的第二涂层是包括第二极性物质构成的具有预定厚度的结构，第二涂层能够通过第二极性物质与负极用粘结剂和/或负极活性物质牢固的粘结，进而防止裸电芯加工过程中的膨胀以及循环使用过程中的循环膨胀率。
进一步的，第二极性物质例如聚烯烃酰胺类、聚烯烃亚胺类、聚氧化烯烃类、聚氨酯类、聚脲类等均包括极性官能团，一方面可以通过极性团能团与负极用粘结剂和/或负极活性物质之间形成氢键，提高第一涂层与负极之间的粘结力；另一方面，第二极性物质本身就是粘结剂，也可以提高第二涂层与负极之间的粘结力。因此，通过前述第二极性物质中的极性官能团以及第二极性物质本身是粘结剂两方面的作用，使得第二涂层与负极粘结的更为牢固。
具体的，本申请的第二极性物质带有YH基团，Y选自N、O、F中的一种。负极用粘结剂和/或负极活性组分带有-HX基团，X选自N、O、F中的一种；这边带有X基团的负极用粘结剂和/或负极活性组分能够与本申请的第二极性物质中的YH基团之间形成氢键X-H-Y，从而使得本申请的第二涂层与本申请的负极粘结的更牢固。更具体的，如图1，负极含-OH/-COOH，更例如负极活性物质中含-OH、负极粘结剂中含-COOH，因此负极活性物质或负极粘结剂与第二极性物质 (含-NH 2)也易形成氢键。
本申请中，隔离膜的第一涂层和第二涂层中，可以分别通过氢键增强隔离膜对正极、负极间的粘结力，进而可以减少裸电芯在加工过程中的膨胀以及循环使用过程中的循环膨胀率，有利于裸电芯整形，使得裸电芯变的更紧实，从而缩短了锂离子的传输路径，使得锂离子可以传输的更快，从而使得电池高倍率放电性能和循环性能更好。
在一些实施方式中，所述第一涂层与所述正极的剥离力不低于0.075N，可选为0.075N～0.125N。所述第二涂层与所述负极的剥离力不低于0.075N，可选为0.075N～0.15N。
剥离力通常是指粘贴在一起的材料，从接触面进行单位宽度剥离时所需要的最大力。剥离力可以反映材料的粘结强度。剥离力的详细测试方法可参见实施例测试方法部分。具体到本申请中，可以从宏观方面用剥离力的大小来反映隔离膜与正极和负极间的氢键的存在及强弱，进而来反映隔离膜与正负极间的粘结力大小。
经过大量实验验证，本领域技术人员知悉的是，隔离膜(如果第一涂层不含第一极性物质)，其与正极之间的剥离力大小通常小于0.035N，此时隔离膜与正极之间的粘结力小，不存在或极少存在氢键，而本申请中，通过正极表面与隔离膜涂层之间剥离力测试，意外发现通过在第一涂层中加入第一极性物质，第一涂层与正极的剥离力不小于0.075N，因此，可以进一步证明第一极性物质与所述正极用粘结剂之间具有氢键。另外，本领域技术人员知悉的是，隔离膜(如果第二涂层不含第二极性物质)，其与负极之间的剥离力大小通常也小于0.035N，此时隔离膜与负极之间的粘结力小，不存在或极少存在氢键。而本申请中，通过负极表面与隔离膜涂层之间剥离力测试，意外发现通过在第二涂层中加入第二极性物质，第二涂层与负极的剥离力不小 于0.075N，可以进一步证明第二极性物质与所述负极用粘结剂或负极活性组分之间具有氢键。
本申请中，在第一涂层与正极的剥离力或第二涂层与负极的剥离力不低于0.075N时，在裸电芯加工过程中以及循环使用过程中，均可以使得裸电芯不易膨胀，隔离膜与正负极更加接触紧密，缩短了锂离子的传输路径，使得锂离子可以传输的更快，从而使得电池高倍率放电性能和循环性能更好。
在一些实施方式中，所述第一极性物质在所述第一涂层中的质量含量w 1与所述正极用粘结剂在所述正极的膜层中的质量含量m 1的比值
Figure PCTCN2021108971-appb-000011
可以为(80～100)∶1。
本申请中，可以通过
Figure PCTCN2021108971-appb-000012
来反映隔离膜中第一极性物质与正极用粘结剂的相对含量关系。
进一步的，当
Figure PCTCN2021108971-appb-000013
小于80∶1时，一方面可能由于第一极性物质在第一涂层中的含量过少，导致第一极性物质与正极用粘结剂之间氢键形成的较少，加上第一极性物质本身的粘结力也不够，进而使得第一涂层和正极用粘结剂粘结力不能牢固，从而不能很好的解决裸电芯加工过程以及循环过程中的膨胀问题。另外一方面可能由于正极用粘结剂含量过多，会堵塞电子传输通道，此外，通常正极用粘结剂为惰性绝缘体，导电性能差，极化大，影响电池的循环性能和高倍率放电性能。
进一步的，当
Figure PCTCN2021108971-appb-000014
大于100∶1时，一方面可能由于第一极性物质含量过多，一则容易堵塞基膜，进而降低透气率，影响隔离膜的动力学性能，二则，循环中后期会第一极性物质容易从基膜脱落，造成循环性能变差，高倍率放电性能变差。另一方面，可能由于正极用粘结 剂含量过少，会导致粘性不够，正极与第一涂层的粘结力小。
因此，
Figure PCTCN2021108971-appb-000015
数值在合理范围内，可以降低裸电芯在加工过程中以及循环使用过程中的膨胀，提升电池的高倍率放电性能以及循环性能。
可选的，所述第一极性物质在所述第一涂层中的质量含量w 1与所述正极用粘结剂在所述正极的膜层中的质量含量m 1的比值
Figure PCTCN2021108971-appb-000016
为80∶1、87∶1、93∶1、97∶1、或100∶1等。
Figure PCTCN2021108971-appb-000017
可以是上述任意点值或者任意点值之间所组成的范围值。
所述第二极性物质在所述第二涂层中的质量含量w 2与所述负极用粘结剂在所述负极的膜层中的质量含量m 2的比值
Figure PCTCN2021108971-appb-000018
可以为(32～50)∶1。
本申请中，可以通过
Figure PCTCN2021108971-appb-000019
反映隔离膜中第二极性物质与负极中粘结剂的相对含量关系。
进一步的，当
Figure PCTCN2021108971-appb-000020
小于32∶1时，一方面可能由于第二极性物质在第二涂层中的含量过少，导致第二极性物质与负极用粘结剂之间氢键形成的较少，加上第二极性物质本身的粘结力也不够，进而使得第二涂层和负极用粘结剂粘结力不能牢固，从而不能很好的解决裸电芯加工过程以及循环过程中的膨胀问题。另外一方面可能由于负极用粘结剂含量过多，会堵塞电子传输通道，此外，通常负极用粘结剂为惰性绝缘体，导电性能差，极化大，影响电池的循环性能和高倍率放电性能。
进一步的，当
Figure PCTCN2021108971-appb-000021
大于50∶1时，一方面可能由于第二极性物质含量过多，循环中后期会容易脱落，造成循环性能变差，高倍率放电性能变差。另一方面，可能由于负极用粘结剂含量过少，会导致粘性不 够，负极与第二涂层的粘结力小。
因此，
Figure PCTCN2021108971-appb-000022
数值在合理范围内，可以降低裸电芯加工过程以及循环过程中的裸电芯膨胀，提升电池的高倍率放电性能以及循环性能。
可选的，所述第二极性物质在所述第二涂层中的质量含量w 2与所述负极用粘结剂在所述负极的膜层中的质量含量m 2的比值
Figure PCTCN2021108971-appb-000023
可选为32∶1、36∶1、40∶1、45∶1、或50∶1等。
Figure PCTCN2021108971-appb-000024
可以是上述任意点值或者任意点值之间所组成的范围值。
在一些实施方式中，所述第一极性物质在所述第一涂层中的质量含量w 1与所述第二极性物质在所述第二涂层中的质量含量w 2的比值
Figure PCTCN2021108971-appb-000025
可以为1∶(1～1.3)。
本申请中，可以通过
Figure PCTCN2021108971-appb-000026
反映隔离膜两表面涂覆极性物质的含量。
本申请中，通过限定
Figure PCTCN2021108971-appb-000027
在合理范围内，可以使得隔离膜张力一致，更加稳定，一方面可以防止张力不一致有短路风险，另一方面，可以提高电池的循环性能和高倍率放电性能。如果
Figure PCTCN2021108971-appb-000028
小于1∶1或
Figure PCTCN2021108971-appb-000029
大于1∶1.3时，会导致隔离膜的两个表面张力不一致，隔离膜会打皱，表面产生气泡，电解液浸润不好，容易出现析锂，循环性能变差，循环衰减变快，高倍率放电性能变差。
可选的，所述第一极性物质在所述第一涂层中的质量含量w 1与所述第二极性物质在所述第二涂层中的质量含量w 2的比值
Figure PCTCN2021108971-appb-000030
为1∶1、或1∶1.3等。
Figure PCTCN2021108971-appb-000031
可以是上述任意点值或者任意点值之间所组成的范围值。
通常，第一极性物质和第二极性物质的涂覆量差异不能太大，可选为两者的涂覆量基本相等，即
Figure PCTCN2021108971-appb-000032
这样可以保证隔离膜两表面 的承受能力基本相同，电池的循环性能和高倍率放电性能更好。
在一些实施方式中，所述第一极性物质在所述第一涂层中的质量含量w 1可以为80％～90％。
本申请中，可以通过w 1来反映第一涂层中第一极性物质的含量。
本申请中，第一极性物质在第一涂层中占主体，可以提高第一极性物质与正极用粘结剂之间的氢键，进而使得第一涂层与正极粘结力更好。如果第一极性物质在第一涂层中的含量低于80％，与正极用粘结剂之间氢键产生较少，则对隔离膜与正极的粘结性改进有限，裸电芯加工过程以及循环使用过程中的膨胀改善效果不明显；如果第一极性物质在第一涂层中的含量大于90％，则容易堵塞基膜，进而降低透气率，影响隔离膜的动力学性能。
可选的，所述第一极性物质在所述第一涂层中的质量含量w 1可选为80％、85％、90％等。w 1可以是上述任意点值或者任意点值之间所组成的范围值。
在一些实施方式中，所述正极用粘结剂在所述正极的膜层中的质量含量m 1可以为0.9％～1.2％。
本申请中，可以通过m 1来反映正极膜层中正极用粘结剂的含量。
m 1在此范围内可以使得正极与第一涂层之间有牢固的粘结力，从而降低裸电芯加工过程或循环使用过程中的膨胀，提高电池的高倍率放电性能以及循环性能。通常正极用粘结剂在正极片中含量不能太大，m 1大于1.2％时，正极用粘结剂含量过多，会堵塞电子传输通道，另外，通常正极用粘结剂为惰性绝缘体，导电性能差，极化大，影响电池的循环性能和高倍率放电性能。通常正极用粘结剂在正极片中含量也不能太小，m 1小于0.9％时，可能由于正极用粘结剂含量过少，会导致粘性不够，正极与第一涂层的粘结力小。
可选的，所述正极用粘结剂在所述正极的膜层中的质量含量m 1可选为0.9％、1％、或1.2％等。m 1可以是上述任意点值或者任意点值之间所组成的范围值。
由此，通过将上述参数w 1、m 1限定在合理范围内可以兼顾动力学性能以及第一涂层和正极之间的粘结力，取得两者的最优比，提高电池的高倍率放电性能以及循环性能。
在一些实施方式中，所述第二极性物质在所述第二涂层中的质量含量w 2可以为80％～90％。
本申请中，可以通过w 2来反映第二涂层中第二极性物质的含量。
本申请中，第二极性物质在第二涂层中占主体，可以提高第二极性物质与负极用粘结剂之间的氢键，进而使得第二涂层与负极粘结力更好。如果第二极性物质在第二涂层中的含量低于80％，与负极用粘结剂之间氢键产生较少，则对隔离膜与负极的粘结性改进有限，裸电芯在加工过程中以及循环使用过程中的膨胀改善效果不明显；如果第二极性物质在第二涂层中的含量大于90％，则容易堵塞基膜，进而降低透气率，影响隔离膜的动力学性能。
可选的，所述第二极性物质在所述第二涂层中的质量含量w 2可选为80％、85％、或90％等。w 2可以是上述任意点值或者任意点值之间所组成的范围值。
在一些实施方式中，所述负极用粘结剂在所述负极的膜层中的质量含量m 2可以为2％～3％。
本申请中，可以通过m 2来反映负极膜层中正极用粘结剂的含量。
本申请中，m 2在此范围内可以使得负极与第二涂层之间有牢固的粘结力，从而降低裸电芯加工过程或循环使用过程中的膨胀，提高电池的高倍率放电性能以及循环性能。通常负极用粘结剂在负极片中 含量不能太大，m 1大于3％时，负极用粘结剂含量过多，会堵塞电子传输通道，另外，通常负极用粘结剂为惰性绝缘体，导电性能差，极化大，影响电池的循环性能和高倍率放电性能。通常负极用粘结剂在负极片中含量也不能太小，m 1小于2％时，可能由于负极用粘结剂含量过少，会导致粘性不够，负极与第二涂层的粘结力小。
可选的，所述负极用粘结剂在所述负极的膜层中的质量含量m 2可选为2％、2.6％、3％等。m 2可以是上述任意点值或者任意点值之间所组成的范围值。
由此，通过将上述参数w 2、m 2限定在合理范围内可以兼顾动力学性能以及第二涂层和负极之间的粘结力，取得两者的最优比，提高电池的高倍率放电性能以及循环性能。
在一些实施方式中，所述第一极性物质包括聚氧化乙烯和聚丙烯酰胺。其中，所述聚氧化乙烯与聚丙烯酰胺的质量比值C1可以为(2～6)∶1。
通常，不同极性物质可以发挥不同的功能，因此可以结合各物质的优势。具体到本申请，在第一活性物质中，聚氧化乙烯是锂离子导体，具有高电导率、低活化能和电极电位最负等特点，可以加快锂离子的传导，需要在第一极性物质中占主体。而由于聚丙烯酰胺与聚氧化乙烯(PEO)相比，聚丙烯酰胺链长、分子量大，且热稳定性好，而通常与正极相连那一面，已被高压氧化，因此如果在聚氧化乙烯中混合少量聚丙烯酰胺等长链分子，尤其在本申请限定的范围内，可以提高电池的循环稳定性和高倍率放电性能。
进一步的，如果所述聚氧化乙烯与聚丙烯酰胺的质量比值C1小于2∶1，由于聚丙烯酰胺不是锂离子导体，会使得锂离子传导速率慢，影响电池的循环性能和高倍率放电性能。而如果所述聚氧化乙烯 与聚丙烯酰胺的质量比值C1大于6∶1，聚丙烯酰胺含量过少，会导致热稳定差。
可选的，所述聚氧化乙烯与聚丙烯酰胺的质量比值C1可选为2∶1、3∶1、4.5∶1、5∶1、或6∶1等。C1可以是上述任意点值或者任意点值之间所组成的范围值。
所述第二极性物质包括聚乙烯亚胺和聚氧化乙烯。其中，所述聚乙烯亚胺与聚氧化乙烯的质量比值C2可以为(2～6)∶1。
通常，不同极性物质可以发挥不同的功能，因此可以结合各物质的优势。具体到本申请，在第二活性物质中，聚乙烯亚胺和聚氧化乙烯都是锂离子导体，具有高电导率、低活化能和电极电位最负等特点，可以加快锂离子的传导。此外，第二活性物质位于与负极相连的一侧，由于负极活性物质例如石墨易膨胀，因此需要选用极性强一些的粘结剂如聚乙烯亚胺(PEI)，此外，由于聚氧化乙烯较聚乙烯亚胺便宜，考虑成本因素，可以在聚乙烯亚胺中加入少量聚氧化乙烯，尤其在本申请限定的范围内，在降低成本的同时，两者相互间也会形成氢键，进一步增强粘结力，降低裸电芯加工和循环使用过程中的膨胀，提高电池的循环性能和高倍率放电性能。
如果所述聚乙烯亚胺与聚氧化乙烯的质量比值C2小于2∶1，由于聚乙烯亚胺极性强，如果含量过少，会导致第二极性物质与负极用粘结剂或负极活性物质之间氢键形成的较少，第二涂层与负极粘结力下降，降低裸电芯加工过程以及循环使用过程中的裸电芯膨胀，影响电池的循环性能和高倍率放电性能。而如果所述聚乙烯亚胺与聚氧化乙烯的质量比值C2大于6∶1，会增加成本。
可选的，所述聚乙烯亚胺与聚氧化乙烯的质量比值C2可选为2∶1、3∶1、4.5∶1、5∶1、或6∶1等。C2可以是上述任意点值或者 任意点值之间所组成的范围值。
在一些实施方式中，所述第一极性物质或第二极性物质中，所述聚酰胺类例如可以是聚丙烯酰胺(PAM)、尼龙-66、尼龙-6等中的一种或多种的组合。聚酰胺类的重均分子量可以为2万～8万；可选为2万、3万、4万、5万、6万、7万、或8万等，聚酰胺类的重均分子量可以是上述任意点值或者任意点值之间所组成的范围值。
在一些实施方式中，所述第一极性物质或第二极性物质中，聚烯烃亚胺类例如可以是聚乙烯亚胺(PEI)、多乙烯多胺等中的一种或多种。所述聚亚胺类的重均分子量可以为7万～10万；可选为7万、8万、9万、或10万等，聚烯烃亚胺类的重均分子量可以是上述任意点值或者任意点值之间所组成的范围值。
在一些实施方式中，所述第一极性物质或第二极性物质中，所述聚氧化烯烃类例如可以是聚氧化乙烯(PEO)等。所述聚氧化烯烃类的重均分子量可以为10万～20万；可选为10万、12万、14万、16万、18万、或20万等，聚氧化烯烃类的重均分子量可以是上述任意点值或者任意点值之间所组成的范围值。
在一些实施方式中，所述第一极性物质或第二极性物质中，聚氨酯类例如可以是通式中含有-NHCOO-的一类聚合物，更例如聚氨酯类可以由包括多异氰酸酯、甲苯二异氰酸酯(TDI)、二苯基甲烷-4，4′-二异氰酸酯(MDI)、多苯基多亚甲基多异氰酸酯(PAPI)中至少一种单体聚合形成，或两种以上单体共聚形成，聚合方式包括无规共聚、嵌段共聚等。所述聚氨酯类的重均分子量可以为0.1万～1万；可选为 0.1万、0.5万、或1万等，聚氨酯类的重均分子量可以是上述任意点值或者任意点值之间所组成的范围值。
在一些实施方式中，所述第一极性物质或第二极性物质中，聚脲类例如可以是通式中含有-NHCONH-的一类聚合物，更例如可以是聚脲、脲醛树脂等中的一种或多种。所述聚脲类物质的重均分子量可以为0.5万～5万；可选为0.5万、1万、2万、3万、4万、或5万等，聚脲类的重均分子量可以是上述任意点值或者任意点值之间所组成的范围值。
在一些实施方式中，所述第一涂层包括第一增强剂，所述第一极性物质在所述第一涂层中的质量含量w 1与所述第一增强剂在所述第一涂层中的质量含量k 1的质量之比
Figure PCTCN2021108971-appb-000033
可以为(5～9)∶1。
本申请中，通过
Figure PCTCN2021108971-appb-000034
来反映第一增强剂与第一极性物质的含量关系。
本申请中，由于第一极性物质电池循环的中期或后期，有从基膜上脱离的风险，因此，可以通过第一增强剂增强第一极性物质在基膜上的粘结力。隔离膜上第一极性物质与第一增强剂的比例在合理范围内，才能降低裸电芯在加工过程中的膨胀以及循环使用过程中的循环膨胀率，提高电池的循环性能以及高倍率放电性能。当
Figure PCTCN2021108971-appb-000035
大于9∶1时，第一极性物质含量过多，一则容易堵塞基膜，进而降低透气率，影响隔离膜的动力学性能，二则，循环中后期会第一极性物质容易从基膜脱落，造成循环性能变差，高倍率放电性能变差。当
Figure PCTCN2021108971-appb-000036
小于5∶1时，第一极性物质在第一涂层中的含量过少，导致第一极性物质与正极用粘结剂之间氢键形成的较少，加上第一极性物质本身的粘结力也不够，进而使得第一涂层和正极用粘结剂粘结力不能牢固，从而不 能很好的解决裸电芯加工和循环使用过程中的膨胀问题。
进一步，分析第一增强剂与第一极性物质之间的氢键形成机理，由于第一增强剂(含F)，与第一极性物质(-YH)之间易形成氢键Y-H-F，第一增强剂可以使得第一极性物质稳定存在于隔离膜上。从而可以降低裸电芯在加工过程中的膨胀以及循环使用过程中的循环膨胀率，提高电池的循环性能以及高倍率放电性能。
可选的，所述第一极性物质在所述第一涂层中的质量含量w 1与所述第一增强剂在所述第一涂层中的质量含量k 1的质量之比
Figure PCTCN2021108971-appb-000037
可以为5∶1、5.3∶1、6∶1、8∶1、9∶1等。
Figure PCTCN2021108971-appb-000038
可以是上述任意点值或者任意点值之间所组成的范围值。
在一些实施方式中，所述第二涂层包括第二增强剂，所述第二极性物质在第二涂层中的质量含量w 2与所述第二增强剂在所述第二涂层中的质量含量k 2的质量之比
Figure PCTCN2021108971-appb-000039
可以为(5～9)∶1。
本申请中，通过
Figure PCTCN2021108971-appb-000040
来反映第二增强剂与第二极性物质的含量关系。
本申请中，由于第二极性物质电池循环的中期或后期，有从基膜上脱离的风险，因此，可以通过第二增强剂增强第二极性物质在基膜上的粘结力。隔离膜上第二极性物质与第二增强剂的比例在合理范围内，才能降低裸电芯在加工过程中的膨胀以及循环使用过程中的循环膨胀率，提高电池的循环性能以及高倍率放电性能。当
Figure PCTCN2021108971-appb-000041
含量大于9∶1时，第二极性物质含量相对过多，循环中后期会容易脱落，造成循环性能变差，高倍率放电性能变差。当
Figure PCTCN2021108971-appb-000042
含量小于5∶1时，第二极性物质在第二涂层中的含量过少，导致第二极性物质与负极用粘结剂之间氢键形成的较少，加上第二极性物质本身的粘结力也不够，进而 使得第二涂层和负极用粘结剂粘结力不能牢固，从而不能很好的解决裸电芯加工以及循环使用过程中的膨胀问题。
进一步的，分析第二增强剂与第二极性物质之间的氢键形成机理，第二增强剂(含F)，与第二极性物质(-YH)之间易形成氢键Y-H-F，第二增强剂可以使得第二极性物质稳定存在于隔离膜上，从而可以降低裸电芯在加工过程中的膨胀以及循环使用过程中的循环膨胀率，提高电池的循环性能以及高倍率放电性能。
可选的，所述第二极性物质在第二涂层中的质量含量w 2与所述第二增强剂在所述第二涂层中的质量含量k 2的质量之比
Figure PCTCN2021108971-appb-000043
可以为5∶1、5.3∶1、6∶1、8∶1、9∶1等。
Figure PCTCN2021108971-appb-000044
可以是上述任意点值或者任意点值之间所组成的范围值。
在一些实施方式中，所述第一增强剂在所述第一涂层中的质量含量k 1不高于所述第二增强剂在所述第二涂层中的质量含量k 2。
本申请中，可以通过k 1、k 2反映隔离膜两表面涂覆增强剂的含量，其中，k 1和k 2的差异不能太大。
通常，当k 1不高于k 2时，可以保持隔离膜张力一致，更加稳定，一方面可以防止张力不一致有短路风险，另一方面，可以提高电池的循环性能和高倍率放电性能。如果k 1与k 2含量相差太大，会导致隔离膜的两个表面张力不一致，隔离膜会打皱，表面产生气泡，电解液浸润不好，容易出现析锂，循环性能变差，循环衰减变快，高倍率放电性能变差。
在一些实施方式中，所述第一增强剂在所述第一涂层中的质量含量k 1与所述第二增强剂在所述第二涂层中的质量含量k 2的比值
Figure PCTCN2021108971-appb-000045
可以为(0.8～1)∶1。
本申请中可以
Figure PCTCN2021108971-appb-000046
可以反映隔离膜两表面的增强剂的相对含量。由此，通过限定合适的增强剂比值，可以在提升隔离膜稳定性，同时，对锂离子传输动力学影响较小，可以提高电池的循环性能和高倍率放电性能。而如果
Figure PCTCN2021108971-appb-000047
小于0.8∶1或
Figure PCTCN2021108971-appb-000048
大于1∶1时，会导致隔离膜的两个表面张力不一致，隔离膜会打皱，表面产生气泡，电解液浸润不好，容易出现析锂，循环性能变差，循环衰减变快，高倍率放电性能变差。
其中，优选为，隔离膜两表面的含量基本一致，可以减少隔离膜两表面的差异性。
可选的，所述第一增强剂在所述第一涂层中的质量含量k 1与所述第二增强剂在所述第二涂层中的质量含量k 2的比值
Figure PCTCN2021108971-appb-000049
可以为0.80∶1、0.9∶1、0.95∶1、或1∶1等。
Figure PCTCN2021108971-appb-000050
可以是上述任意点值或者任意点值之间所组成的范围值。
在一些实施方式中，所述第一增强剂在所述第一涂层中的质量含量k 1可以为10％～20％。所述第二增强剂在所述第二涂层中的质量百分含量k 2可以为10％～20％。
本申请中，可以通过k 1反映第一增强剂在第一涂层中的含量。可以通过k 2反映第二增强剂在第二涂层中的含量。
本申请中，第一增强剂在第一涂层中含量以及第二增强剂在第二涂层中含量差别不能太大，如果k 1与k 2含量相差太大，会导致隔离膜的两个表面张力不一致，隔离膜会打皱，表面产生气泡，电解液浸润不好，容易出现析锂，循环性能变差，循环衰减变快，高倍率放电性能变差。由此，通过将上述参数限定在合理范围内，可以在提升隔膜稳定性同时，对锂离子传输动力学影响小，可以兼顾动力学和粘性，取得最优比，可以提高电池的循环性能和高倍率放电性能。
可选的，隔离膜两面的含量基本一致，可以减少隔膜两面的差异性，隔离膜张力一致，防止打皱。
可选的，所述第一增强剂在所述第一涂层中的质量含量k 1可以为14％、16.6％、18％、19％、或20％等。k 1可以是上述任意点值或者任意点值之间所组成的范围值。
可选的，所述第二增强剂在所述第二涂层中的质量百分含量k 2可以为10％、11％、14％、15.8％、16.6％、17％、或20％等。k 2可以是上述任意点值或者任意点值之间所组成的范围值。
在一些实施方式中，所述第一增强剂或第二增强剂包括聚偏二氟乙烯、海藻酸钠中的一种或多种，其中，由于聚偏二氟乙烯成本低，可以优先使用聚偏二氟乙烯。所述正极用粘结剂包括聚偏氟乙烯。所述负极用粘结剂包括丁苯橡胶、海藻酸钠中的一种以上。
在一些实施方式中，所述第一增强剂或第二增强剂的重均分子量为0.05万～60万；可选为0.05万、1万、10万、20万、30万、40万、50万、或60万等，第一增强剂或第二增强剂的重均分子量可以是上述任意点值或者任意点值之间所组成的范围值。
进一步的，所述聚偏二氟乙烯的重均分子量可以为10-60万；可选为10万、20万、30万、40万、50万、或60万等，聚偏二氟乙烯的重均分子量可以是上述任意点值或者任意点值之间所组成的范围值。
进一步的，海藻酸钠的重均分子量可以为0.05～5万；可选为0.05万、1万、2万、3万、4万、或5万等，海藻酸钠的重均分子量可以是上述任意点值或者任意点值之间所组成的范围值。其中，前述聚偏二氟乙烯和海藻酸钠可适用于第一增强剂、第二增强剂、正极用粘结剂或负极用粘结剂中。
在一些实施方式中，所述第一涂层和所述第二涂层的质量比可以为1∶(1～1.5)。
本申请中，通过第一涂层和第二涂层可以反映隔离膜两面涂覆物质的含量，两者的差异不能太大；由此，通过限定第一涂层和第二涂层的涂覆量在合理范围内，可以使得隔离膜张力一致，更加稳定，一方面可以防止张力不一致有短路风险。另一方面，可以提高电池的循环性能和高倍率放电性能。如果第一涂层和第二涂层含量相差太大，会导致隔离膜的两个表面张力不一致，隔离膜会打皱，表面产生气泡，电解液浸润不好，容易出现析锂，循环性能变差，循环衰减变快，高倍率放电性能变差。
可选为，第一涂层和所述第二涂层的质量比可以为1∶1、1∶2、1∶3、1∶4、1∶5等。第一涂层和所述第二涂层的质量比可以是上述任意点值或者任意点值之间所组成的范围值。
在一些实施方式中，第一涂层或第二涂层中还可以包括填料，所述填料例如可以是氧化铝，可以提高涂层的耐热性和稳定性，与第一极性物质配合使用，可以降低裸电芯在加工过程以及循环使用过程中的膨胀，提高电池的循环性能和高倍率放电性能。所述填料的含量没有特别限定，例如可以填料在第一涂层或第二涂层中的质量比大于0小于等于25％。填料在第一涂层或第二涂层中的含量大于25％会导致堵塞基膜的孔，导致离子传输速率慢，影响电池的循环性能和高倍率放电性能。
可选的，所述填料在第一涂层或第二涂层中的质量百分比可以为3.2％、8％、10％、15％、18.9％、20％、或25％等。填料在第一涂层或第二涂层中的质量比可以是上述任意点值或者任意点值之间所组成的范围值。
在一些实施方式中，所述第一涂层由第一涂层浆料制备获得。所述第一涂层浆料包括所述第一极性物质、所述第一增强剂和第一溶剂；其中，所述第一涂层浆料的粘度可以为8000mpa.s～12000mpa.s。
本申请中，第一涂层浆料的制备方法可以采用本领域的公知方法。例如可以是将第一极性物质、第一增强剂混合于第一溶剂中，形成均匀的浆料，即为第一涂层浆料，可选的，在第一涂层浆料制备过程中，也可以将第一极性物质、第一增强剂、填料混合后溶于第一溶剂中制备过程。各物质间的用量可参照本申请前述关于各组分在第一涂层中的质量比例设定。
本申请中，第一涂层浆料粘度对涂布，以及电芯电化学性能影响很大，第一涂层浆料粘度太高容易形成凝胶，涂布不均匀，造成电芯一致性差，电池的循环性能和高倍率放电性能会降低。而如果第一涂层浆料粘度过低，从而会使得第一涂层浆料不能很好的涂覆在基膜上。由此，通过限定第一涂层浆料在合适的粘度范围内，可以使得第一涂层浆料更好的在基膜上涂布，并且可以保证电芯一致性良好，提高电池的循环性能和高倍率放电性能。
可选的，所述第一涂层浆料的粘度可以为8000mpa.s、9000mpa.s、10000mpa.s、11000mpa.s、或12000mpa.s等。第一涂层浆料的重均分子量可以是上述任意点值或者任意点值之间所组成的范围值。
进一步的，第一溶剂通常没有限定，更具体的，第一增强剂选自海藻酸钠时，第一溶剂的选择没有限定。而当第一增强剂选自聚偏二氟乙烯时，第一溶剂选自有机溶剂，所述有机溶剂例如可以是N，N-二甲基吡咯烷酮、丙酮等。
在一些实施方式中，所述第二涂层由第二涂层浆料制备获得，第 二涂层的制备方法可以采用本领域的公知方法。所述第二涂层浆料包括所述第二极性物质、所述第二增强剂和第二溶剂；其中，所述第二涂层浆料的粘度为5000mpa.s～20000mpa.s。
本申请中，第二涂层浆料的制备方法可以采用本领域的公知方法。例如可以是将第二极性物质、第二增强剂混合于第二溶剂中，形成均匀的浆料，即为第二涂层浆料，可选的，在第二涂层浆料制备过程中，也可以将第二极性物质、第二增强剂、填料混合后溶于第二溶剂中制备过程。各物质间的用量可参照本申请前述关于各组分在第二涂层中的质量比例设定。
本申请中，第二涂层浆料粘度对涂布，以及电芯电化学性能影响很大，第二涂层浆料粘度太高容易形成凝胶，涂布不均匀，造成电芯一致性差，电池的循环性能和高倍率放电性能会降低。而如果第二涂层浆料粘度过低，从而会使得第二涂层浆料不能很好的涂覆在基膜上。由此，通过限定第二涂层浆料在合适的粘度范围内，可以使得第二涂层浆料更好的在基膜上涂布，并且可以保证电芯一致性良好，提高电池的循环性能和高倍率放电性能。
可选的，所述第二涂层浆料的粘度可以为5000mpa.s、8000mpa.s、10000mpa.s、13000mpa.s、15000mpa.s、18000mpa.s、或20000mpa.s等。第二涂层浆料的重均分子量可以是上述任意点值或者任意点值之间所组成的范围值。
进一步的，第二溶剂通常没有限定，更具体的，第二增强剂选自海藻酸钠时，第二溶剂的选择没有限定。而当第二增强剂选自聚偏二氟乙烯时，第二溶剂选自有机溶剂，所述有机溶剂例如可以是N，N-二甲基吡咯烷酮、丙酮等。
[基膜]
在一些实施方式中，本申请对基膜的种类没有特别的限制，可以选用任意公知的具有良好的化学稳定性和机械稳定性的多孔结构基膜。
在一些实施方式中，基膜的材质可选自玻璃纤维、无纺布、聚乙烯、聚丙烯及聚偏二氟乙烯中的至少一种。基膜可以是单层薄膜，也可以是多层复合薄膜，没有特别限制。在基膜为多层复合薄膜时，各层的材料可以相同或不同，没有特别限制。
[负极]
负极包括负极集流体以及设置在负极集流体至少一个表面上的负极膜层，所述负极膜层包括负极活性组分。
在一些实施方式中，所述负极活性组分包括硅碳混合物，所述硅碳混合物，硅的粒径可以为0.1-0.5微米。碳为人造石墨和天然石墨的混合碳。
本申请中，硅的粒径对电化学性能影响比较大，微米硅相对于纳米硅的比表面积更小，副反应少，电池的循环性能更好，高倍率放电性能更佳，因此选用微米硅。
可选的，所述硅的粒径为0.1微米、0.3微米、0.5微米等。硅的粒径可以是上述任意点值或者任意点值之间所组成的范围值。
可选的，硅碳混合物中C∶Si可以为95～97∶3～5等。更例如C∶Si可以是95∶5。
进一步的，所述硅碳混合物在所述负极膜层中的含量可以为95％-97％。由于硅碳混合物的含量影响着电芯的能量密度，通常硅碳 混合物在所述负极膜层中的含量大于95％才能实现电池的高容量，提高电池的循环性能和高倍率放电性能。
可选的，硅碳混合物在负极膜层中的含量可以为95.9％、96％、96.7％、96.8％、或97％等。硅碳混合物在负极膜层中的含量可以是上述任意点值或者任意点值之间所组成的范围值。
可选的，负极活性组分可采用本领域公知的用于电池的负极活性材料。作为示例，负极活性组分可包括以下材料中的至少一种：人造石墨、天然石墨、软炭、硬炭、硅基材料、锡基材料和钛酸锂等。所述硅基材料可选自单质硅、硅氧化合物、硅氮复合物以及硅合金中的至少一种。所述锡基材料可选自单质锡、锡氧化合物以及锡合金中的至少一种。但本申请并不限定于这些材料，还可以使用其他可被用作电池负极活性组分的传统材料。这些负极活性组分可以仅单独使用一种，也可以将两种以上组合使用。
作为示例，负极集流体具有在其自身厚度方向相对的两个表面，负极膜层设置在负极集流体相对的两个表面中的任意一者或两者上。
在一些实施方式中，所述负极集流体可采用金属箔片或复合集流体。例如，作为金属箔片，可以采用铜箔。复合集流体可包括高分子材料基层和形成于高分子材料基材至少一个表面上的金属层。复合集流体可通过将金属材料(铜、铜合金、镍、镍合金、钛、钛合金、银及银合金等)形成在高分子材料基材(如聚丙烯(PP)、聚对苯二甲酸乙二醇酯(PET)、聚对苯二甲酸丁二醇酯(PBT)、聚苯乙烯(PS)、聚乙烯(PE)等的基材)上而形成。
在一些实施方式中，负极膜层还可选地包括负极用粘结剂。所述负极用粘结剂可选自丁苯橡胶(SBR)、聚丙烯酸(PAA)、聚丙烯酸钠(PAAS)、聚丙烯酰胺(PAM)、聚乙烯醇(PVA)、海藻酸钠(SA)、 聚甲基丙烯酸(PMAA)及羧甲基壳聚糖(CMCS)中的至少一种。可选的，负极用粘结剂选自丁苯橡胶(SBR)和海藻酸钠(SA)。
在一些实施方式中，负极膜层还可选地包括导电剂。导电剂可选自超导碳、乙炔黑、炭黑、科琴黑、碳点、碳纳米管、石墨烯及碳纳米纤维中的至少一种。
在一些实施方式中，负极膜层还可选地包括其他助剂，例如增稠剂(如羧甲基纤维素钠(CMC-Na))等
在一些实施方式中，可以通过以下方式制备负极：将上述用于制备负极的组分，例如负极活性组分、导电剂、粘结剂和任意其他组分分散于溶剂(例如去离子水)中，形成负极浆料；将负极浆料涂覆在负极集流体上，经烘干、冷压等工序后，即可得到负极。
[正极]
正极包括正极集流体以及设置在正极集流体至少一个表面的正极膜层，所述正极膜层包括本申请第一方面的正极材料。
在一些实施方式中，所述正极包括正极材料LiNi xCo yMn zO 2，其中，x+y+z＝1，x＝0.5～0.9，可选的，x＝0.5～0.7、x＝0.8～0.9。
本申请中，通常来说，正极材料镍含量大于0.5即可，但由于不同正极体系电芯，裸电芯膨胀变化不同，本申请的隔离膜尤其对包含高镍正极材料的裸电芯的循环膨胀率改善效果显著。
更具体的，当镍含量x＝0.5～0.7时，正极材料的晶胞参数变化较大，正极材料的体积变化也大，最终的裸电芯膨胀相较于初始裸电芯膨胀变化较大，而获得的裸电芯循环膨胀率较小，本申请在前述范围内，裸电芯的循环膨胀率改善更为显著，循环保持率更好。而当镍含 量例如为0.8～0.9时，虽然正极材料的晶胞参数变化较小，但是由于最终的裸电芯循环膨胀率也很小，因此也是在本申请要求的范围内。
可选的，x＝0.4、x＝0.5、x＝0.6、x＝0.7、x＝0.8或x＝0.9等，镍含量可以是上述任意点值或者任意点值之间所组成的范围值。
可选的，正极材料可以为LiNi 0.4Co 0.4Mn 0.2O 2、LiNi 0.5Co 0.2Mn 0.3O 2、LiNi 0.6Co 0.2Mn 0.2O 2、LiNi 0.7Co 0.2Mn 0.1O 2、LiNi 0.8Co 0.1Mn 0.1O 2、LiNi 0.9Co 0.05Mn 0.05O 2等。
进一步可选的，正极活性材料可采用本领域公知的用于电池的正极活性材料。作为示例，正极活性材料可包括以下材料中的至少一种：橄榄石结构的含锂磷酸盐、锂过渡金属氧化物及其各自的改性化合物。但本申请并不限定于这些材料，还可以使用其他可被用作电池正极活性材料的传统材料。这些正极活性材料可以仅单独使用一种，也可以将两种以上组合使用。其中，锂过渡金属氧化物的示例可包括但不限于锂钴氧化物(如LiCoO 2)、锂镍氧化物(如LiNiO 2)、锂锰氧化物(如LiMnO 2、LiMn 2O 4)、锂镍钴氧化物、锂锰钴氧化物、锂镍锰氧化物、锂镍钴锰氧化物(如LiNi 1/3Co 1/3Mn 1/3O 2(也可以简称为NCM 333)、LiNi 0.5Co 0.25Mn 0.25O 2(也可以简称为NCM 211)、锂镍钴铝氧化物(如LiNi 0.85Co 0.15Al 0.05O 2)及其改性化合物等中的至少一种。橄榄石结构的含锂磷酸盐的示例可包括但不限于磷酸铁锂(如LiFePO 4(也可以简称为LFP))、磷酸铁锂与碳的复合材料、磷酸锰锂(如LiMnPO 4)、磷酸锰锂与碳的复合材料、磷酸锰铁锂、磷酸锰铁锂与碳的复合材料中的至少一种。
作为示例，正极集流体具有在其自身厚度方向相对的两个表面，正极膜层设置在正极集流体相对的两个表面的其中任意一者或两者上。
在一些实施方式中，所述正极集流体可采用金属箔片或复合集流体。例如，作为金属箔片，可采用铝箔。复合集流体可包括高分子材料基层和形成于高分子材料基层至少一个表面上的金属层。复合集流体可通过将金属材料(铝、铝合金、镍、镍合金、钛、钛合金、银及银合金等)形成在高分子材料基材(如聚丙烯(PP)、聚对苯二甲酸乙二醇酯(PET)、聚对苯二甲酸丁二醇酯(PBT)、聚苯乙烯(PS)、聚乙烯(PE)等的基材)上而形成。
在一些实施方式中，正极膜层还可选地包括负极用粘结剂。作为示例，所述负极用粘结剂可以包括聚偏氟乙烯(PVDF)、聚四氟乙烯(PTFE)、偏氟乙烯-四氟乙烯-丙烯三元共聚物、偏氟乙烯-六氟丙烯-四氟乙烯三元共聚物、四氟乙烯-六氟丙烯共聚物及含氟丙烯酸酯树脂中的至少一种。可选的，负极用粘结剂选自聚偏氟乙烯(PVDF)。
在一些实施方式中，正极膜层还可选地包括导电剂。作为示例，所述导电剂可以包括超导碳、乙炔黑、炭黑、科琴黑、碳点、碳纳米管、石墨烯及碳纳米纤维中的至少一种。
在一些实施方式中，可以通过以下方式制备正极：将上述用于制备正极的组分，例如正极材料、导电剂、粘结剂和任意其他的组分分散于溶剂(例如N-甲基吡咯烷酮)中，形成正极浆料；将正极浆料涂覆在正极集流体上，经烘干、冷压等工序后，即可得到正极。
[电解质]
电解质在正极极片和负极极片之间起到传导离子的作用。本申请 对电解质的种类没有具体的限制，可根据需求进行选择。例如，电解质可以是液态的、凝胶态的或全固态的。
在一些实施方式中，所述电解质采用电解液。所述电解液包括电解质盐和溶剂。
在一些实施方式中，电解质盐可选自六氟磷酸锂、四氟硼酸锂、高氯酸锂、六氟砷酸锂、双氟磺酰亚胺锂、双三氟甲磺酰亚胺锂、三氟甲磺酸锂、二氟磷酸锂、二氟草酸硼酸锂、二草酸硼酸锂、二氟二草酸磷酸锂及四氟草酸磷酸锂中的至少一种。
在一些实施方式中，溶剂可选自碳酸亚乙酯、碳酸亚丙酯、碳酸甲乙酯、碳酸二乙酯、碳酸二甲酯、碳酸二丙酯、碳酸甲丙酯、碳酸乙丙酯、碳酸亚丁酯、氟代碳酸亚乙酯、甲酸甲酯、乙酸甲酯、乙酸乙酯、乙酸丙酯、丙酸甲酯、丙酸乙酯、丙酸丙酯、丁酸甲酯、丁酸乙酯、1，4-丁内酯、环丁砜、二甲砜、甲乙砜及二乙砜中的至少一种。
在一些实施方式中，所述电解液还可选地包括添加剂。例如添加剂可以包括负极成膜添加剂、正极成膜添加剂，还可以包括能够改善电池某些性能的添加剂，例如改善电池过充性能的添加剂、改善电池高温或低温性能的添加剂等。
以下适当参照附图对本申请的电池进行说明。
本申请的一个实施方式中，提供一种二次电池。通常情况下，二次电池包括正极、负极、电解质和隔离膜。在电池充放电过程中，活性离子在正极和负极之间往返嵌入和脱出。电解质在正极和负极之间起到传导离子的作用。隔离膜设置在正极极片和负极极片之间，主要起到防止正负极短路的作用，同时可以使离子通过。
在一些实施方式中，正极、负极和隔离膜可通过卷绕工艺或叠片 工艺制成电极组件。
在一些实施方式中，二次电池可包括外包装。该外包装可用于封装上述电极组件及电解质。
在一些实施方式中，二次电池的外包装可以是硬壳，例如硬塑料壳、铝壳、钢壳等。二次电池的外包装也可以是软包，例如袋式软包。软包的材质可以是塑料，作为塑料，可列举出聚丙烯、聚对苯二甲酸丁二醇酯以及聚丁二酸丁二醇酯等。
本申请对二次电池的形状没有特别的限制，其可以是圆柱形、方形或其他任意的形状。例如，图3是作为一个示例的方形结构的二次电池5。
在一些实施方式中，参照图4，外包装可包括壳体51和盖板53。其中，壳体51可包括底板和连接于底板上的侧板，底板和侧板围合形成容纳腔。壳体51具有与容纳腔连通的开口，盖板53能够盖设于所述开口，以封闭所述容纳腔。正极极片、负极极片和隔离膜可经卷绕工艺或叠片工艺形成电极组件52。电极组件52封装于所述容纳腔内。电解液浸润于电极组件52中。二次电池5所含电极组件52的数量可以为一个或多个，本领域技术人员可根据具体实际需求进行选择。
另外，以下适当参照附图对本申请的电池模块、电池包和用电装置进行说明。
电池模块
在一些实施方式中，二次电池可以组装成电池模块，电池模块所含二次电池的数量可以为一个或多个，具体数量本领域技术人员可根据电池模块的应用和容量进行选择。
图5是作为一个示例的电池模块4。参照图5，在电池模块4中， 多个二次电池5可以是沿电池模块4的长度方向依次排列设置。当然，也可以按照其他任意的方式进行排布。进一步可以通过紧固件将该多个二次电池5进行固定。
可选地，电池模块4还可以包括具有容纳空间的外壳，多个二次电池5容纳于该容纳空间。
电池包
在一些实施方式中，上述电池模块还可以组装成电池包，电池包所含电池模块的数量可以为一个或多个，具体数量本领域技术人员可根据电池包的应用和容量进行选择。
图6和图7是作为一个示例的电池包1。参照图6和图7，在电池包1中可以包括电池箱和设置于电池箱中的多个电池模块4。电池箱包括上箱体2和下箱体3，上箱体2能够盖设于下箱体3，并形成用于容纳电池模块4的封闭空间。多个电池模块4可以按照任意的方式排布于电池箱中。
用电装置
另外，本申请还提供一种用电装置，所述用电装置包括本申请提供的二次电池、电池模块、或电池包中的至少一种。所述二次电池、电池模块、或电池包可以用作所述用电装置的电源，也可以用作所述用电装置的能量存储单元。所述用电装置可以包括移动设备(例如手机、笔记本电脑等)、电动车辆(例如纯电动车、混合动力电动车、插电式混合动力电动车、电动自行车、电动踏板车、电动高尔夫球车、电动卡车等)、电气列车、船舶及卫星、储能系统等，但不限于此。
作为所述用电装置，可以根据其使用需求来选择二次电池、电池 模块或电池包。
图8是作为一个示例的用电装置。该用电装置为纯电动车、混合动力电动车、或插电式混合动力电动车等。为了满足该用电装置对二次电池的高功率和高能量密度的需求，可以采用电池包或电池模块。
作为另一个示例的装置可以是手机、平板电脑、笔记本电脑等。该装置通常要求轻薄化，可以采用二次电池作为电源。
实施例
以下，说明本申请的实施例。下面描述的实施例是示例性的，仅用于解释本申请，而不能理解为对本申请的限制。实施例中未注明具体技术或条件的，按照本领域内的文献所描述的技术或条件或者按照产品说明书进行。所用试剂或仪器未注明生产厂商者，均为可以通过市购获得的常规产品。
实施例1-1：
1、隔离膜的制备
1)将第一极性物质PEO和氧化铝按照质量比为80∶20的比例溶于NMP中，搅拌均匀获得第一涂层浆料，用凹版涂布将第一涂层浆料涂布于PE基膜的A面(PE基膜靠近正极的一面)。
2)将第二极性物质PEI和氧化铝按照质量比为80∶20的比例溶于去离子水中，搅拌均匀获得第二涂层浆料，用凹版涂布将第二涂层浆料涂布于PE基膜的B面(PE基膜靠近负极的一面)。
3)将经过步骤1)涂布第一涂层浆料和步骤2)涂布第二涂层浆料后的PE基膜在60℃烘干1h，在PE基膜的两表面形成第一涂层和 第二涂层，制备获得隔离膜。
2、正极的制备
将正极活性物质LiNi 0.6Co 0.2Mn 0.2O 2、正极用粘结剂PVDF、导电碳按照质量比为97∶1.07∶1.93混合，并溶于NMP中，搅拌6h获得正极浆料，将正极浆料涂覆于铝箔上，烘干，冷压后制备获得正极。
其中第一极性物质在所述第一涂层中的质量含量w 1与所述正极用粘结剂在所述正极的膜层中的质量含量m 1的比值
Figure PCTCN2021108971-appb-000051
为75∶1。
3、负极的制备
将SA和SBR按照质量比80∶20混合得到负极用粘结剂，再将负极活性物质碳硅混合物(C∶Si＝95∶5)、负极用粘结剂、碳纳米管按照质量比为97∶2.66∶0.34混合，并溶于水中，搅拌6h获得负极浆料，将负极浆料涂覆于铜箔上，烘干，冷压后制备获得负极。
其中第二极性物质在所述第二涂层中的质量含量w 2与所述负极用粘结剂在所述负极的膜层中的质量含量m 2的比值
Figure PCTCN2021108971-appb-000052
为30∶1。
4、电池的制备
将正极、隔离膜、负极按顺序叠好，其中，隔离膜的第一涂层与正极接触，隔离膜的第二涂层与负极接触，然后卷绕得到裸电芯。将裸电芯放入铝壳内，焊接顶盖，经过注液，高温静置，化成，老化，等工序获得锂离子电池。
实施例1-2：
锂离子电池的制备过程整体上参照实施例1-1，区别在于，正极活性物质LiNi 0.6Co 0.2Mn 0.2O 2、正极用粘结剂PVDF、导电碳的质量比 为97∶1∶2；负极活性物质碳硅混合物、负极用粘结剂、碳纳米管的质量比为97∶2.5∶0.5。
第一极性物质在第一涂层中的质量含量w 1与正极用粘结剂在正极的膜层中的质量含量m 1的比值
Figure PCTCN2021108971-appb-000053
为80∶1。第二极性物质在第二涂层中的质量含量w 2与负极用粘结剂在负极的膜层中的质量含量m 2的比值
Figure PCTCN2021108971-appb-000054
为32∶1。
实施例1-3：
锂离子电池的制备过程整体上参照实施例1-1，区别在于，正极活性物质LiNi 0.6Co 0.2Mn 0.2O 2、正极用粘结剂PVDF、导电碳的质量比为97∶0.91∶2.09；负极活性物质碳硅混合物、负极用粘结剂、碳纳米管的质量比为97∶2.2∶0.8。
第一极性物质在第一涂层中的质量含量w 1与正极用粘结剂在正极的膜层中的质量含量m 1的比值
Figure PCTCN2021108971-appb-000055
为87∶1。第二极性物质在第二涂层中的质量含量w 2与负极用粘结剂在负极的膜层中的质量含量m 2的比值
Figure PCTCN2021108971-appb-000056
为36∶1。
实施例1-4：
锂离子电池的制备过程整体上参照实施例1-1，正极活性物质LiNi 0.6Co 0.2Mn 0.2O 2、正极用粘结剂PVDF、导电碳的质量比为97∶0.86∶2.14；负极活性物质碳硅混合物、负极用粘结剂、碳纳米管的质量比为97∶2∶1。
第一极性物质在第一涂层中的质量含量w 1与正极用粘结剂在正 极的膜层中的质量含量m 1的比值
Figure PCTCN2021108971-appb-000057
为93∶1。第二极性物质在第二涂层中的质量含量w 2与负极用粘结剂在负极的膜层中的质量含量m 2的比值
Figure PCTCN2021108971-appb-000058
为40∶1。
实施例1-5：
锂离子电池的制备过程整体上参照实施例1-1，区别在于，正极活性物质LiNi 0.6Co 0.2Mn 0.2O 2、正极用粘结剂PVDF、导电碳的质量比为97∶0.82∶2.18；负极活性物质碳硅混合物、负极用粘结剂、碳纳米管的质量比为97∶1.77∶1.23。
第一极性物质在第一涂层中的质量含量w 1与正极用粘结剂在正极的膜层中的质量含量m 1的比值
Figure PCTCN2021108971-appb-000059
为97∶1。第二极性物质在第二涂层中的质量含量w 2与负极用粘结剂在负极的膜层中的质量含量m 2的比值
Figure PCTCN2021108971-appb-000060
为45∶1。
实施例1-6：
锂离子电池的制备过程整体上参照实施例1-1，区别在于，正极活性物质LiNi 0.6Co 0.2Mn 0.2O 2、正极用粘结剂PVDF、导电碳的质量比为97∶0.8∶2.2；负极活性物质碳硅混合物、负极用粘结剂、碳纳米管的质量比为97∶1.6∶1.4。
第一极性物质在第一涂层中的质量含量w 1与正极用粘结剂在正极的膜层中的质量含量m 1的比值
Figure PCTCN2021108971-appb-000061
为100∶1。第二极性物质在第二涂层中的质量含量w 2与负极用粘结剂在负极的膜层中的质量含量m 2的比值
Figure PCTCN2021108971-appb-000062
为50∶1。
实施例1-7：
锂离子电池的制备过程整体上参照实施例1-1，区别在于，正极活性物质LiNi 0.6Co 0.2Mn 0.2O 2、正极用粘结剂PVDF、导电碳按照质量比为97∶0.76∶2.24混合；负极活性物质碳硅混合物、负极用粘结剂、碳纳米管的质量比为97∶1.5∶1.5混合。
第一极性物质在第一涂层中的质量含量w 1与正极用粘结剂在正极的膜层中的质量含量m 1的比值
Figure PCTCN2021108971-appb-000063
为105∶1。第二极性物质在第二涂层中的质量含量w 2与负极用粘结剂在负极的膜层中的质量含量m 2的比值
Figure PCTCN2021108971-appb-000064
为53∶1。
实施例2-1：
1、隔离膜的制备
1)将第一极性物质PAM和氧化铝按照质量比为96.8∶3.2的比例溶于NMP中，搅拌均匀获得第一涂层浆料，用凹版涂布将第一涂层浆料涂布于PE基膜的A面(PE基膜靠近正极的一面)。
2)将第二极性物质PEO和氧化铝按照质量比为77.5∶22.5的比例溶于去离子水中，搅拌均匀获得第二涂层浆料，用凹版涂布将第二涂层浆料涂布于PE基膜的B面(PE基膜靠近负极的一面)。
3)将经过步骤1)涂布第一涂层浆料和步骤2)涂布第二涂层浆料后的PE基膜在60℃烘干1h，在PE基膜的两表面形成第一涂层和第二涂层，制备获得隔离膜。
其中，第一极性物质在第一涂层中的质量含量w 1与第二极性物 质在第二涂层中的质量含量w 2的比值
Figure PCTCN2021108971-appb-000065
为1∶0.8。
2、正极的制备
将正极活性物质LiNi 0.6Co 0.2Mn 0.2O 2、正极用粘结剂PVDF、导电碳按照质量比为97∶1∶2混合，并溶于NMP中，搅拌6h获得正极浆料，将正极浆料涂覆于铝箔上，烘干，冷压后制备获得正极。
3、负极的制备
将SA和SBR按照质量比80∶20混合得到负极用粘结剂，再将负极活性物质碳硅混合物(C∶Si＝95∶5)、负极用粘结剂、碳纳米管按照质量比为97∶2.5∶0.5混合后，溶于水中，搅拌6h获得负极浆料，将负极浆料涂覆于铜箔上，烘干，冷压后制备获得负极。
4、电池的制备
将正极、隔离膜、负极按顺序叠好，其中，将隔离膜的第一涂层与正极接触，将隔离膜的第二涂层与负极接触，然后卷绕得到裸电芯。将裸电芯放入铝壳内，焊接顶盖，经过注液，高温静置，化成，老化，等工序获得锂离子电池。
实施例2-2：
与实施例2-1基本相同，区别在于，第一极性物质PAM和氧化铝的质量比为85∶15；第二极性物质PEO和氧化铝的质量比为85∶15。第一极性物质在第一涂层中的质量含量w 1与第二极性物质在第二涂层中的质量含量w 2的比值
Figure PCTCN2021108971-appb-000066
为1∶1。
实施例2-3：
锂离子电池的制备过程整体上参照实施例2-1，区别在于，第一 极性物质PAM和氧化铝的质量比为71.1∶28.9；第二极性物质PEO和氧化铝的质量比为92.5∶7.5。第一极性物质在第一涂层中的质量含量w 1与第二极性物质在第二涂层中的质量含量w 2的比值
Figure PCTCN2021108971-appb-000067
为1∶1.3。
实施例2-4：
锂离子电池的制备过程整体上参照实施例2-1，区别在于，第一极性物质PAM和氧化铝的质量比为65∶35；第二极性物质PEO和氧化铝的质量比为97.5∶2.5。第一极性物质在第一涂层中的质量含量w 1与第二极性物质在第二涂层中的质量含量w 2的比值
Figure PCTCN2021108971-appb-000068
为1∶1.5。
实施例3-1：
1、隔离膜的制备
1)将第一极性物质聚脲和氧化铝按照质量比为75∶25的比例溶于NMP中，搅拌均匀获得第一涂层浆料，用凹版涂布将第一涂层浆料涂布于PE基膜的A面(PE基膜靠近正极的一面)。
2)将第二极性物质PAM和氧化铝按照质量比为75∶25的比例溶于去离子水中，搅拌均匀获得第二涂层浆料，用凹版涂布将第二涂层浆料涂布于PE基膜的B面(PE基膜靠近负极的一面)。
3)将经过步骤1)涂布第一涂层浆料和步骤2)涂布第二涂层浆料后的PE基膜在60℃烘干1h，在PE基膜的两表面形成第一涂层和第二涂层，制备获得隔离膜。
2、正极的制备
将正极活性物质LiNi 0.6Co 0.2Mn 0.2O 2、正极用粘结剂PVDF、导电碳按照质量比为97∶0.8∶2.2混合，并溶于NMP中，获得正极浆料，搅拌6h，将正极浆料涂覆于铝箔上，烘干，冷压后制备获得正极。
3、负极的制备
将SA和SBR按照质量比80∶20混合得到负极用粘结剂，再将负极活性物质碳硅混合物(C∶Si＝95∶5)、负极用粘结剂、碳纳米管按照质量比为97∶1.8∶1.2混合后，溶于水中，搅拌6h获得负极浆料，将负极浆料涂覆于铜箔上，烘干，冷压后制备获得负极。
4、电池的制备
将正极、隔离膜、负极按顺序叠好，其中，隔离膜的第一涂层与正极接触，隔离膜的第二涂层与负极接触，然后卷绕得到裸电芯。将裸电芯放入铝壳内，焊接顶盖，经过注液，高温静置，化成，老化，等工序获得锂离子电池。
实施例3-2：
锂离子电池的制备过程整体上参照实施例3-1，区别在于，第一极性物质聚脲在第一涂层中的质量占比为80％；第二极性物质PAM在第二涂层中的质量占比为80％。正极活性物质LiNi 0.6Co 0.2Mn 0.2O 2、正极用粘结剂PVDF、导电碳的质量比为97∶0.9∶2.3。负极活性物质碳硅混合物、负极用粘结剂、碳纳米管的质量比为97∶2∶1。
实施例3-3：
锂离子电池的制备过程整体上参照实施例3-1，区别在于，第一极性物质聚脲在第一涂层中的质量占比为85％；第二极性物质PAM 在第二涂层中的质量占比为85％。正极活性物质LiNi 0.6Co 0.2Mn 0.2O 2、正极用粘结剂PVDF、导电碳的质量比为97∶1∶2。负极活性物质碳硅混合物、负极用粘结剂、碳纳米管的质量比为97∶2.6∶0.4。
实施例3-4：
锂离子电池的制备过程整体上参照实施例3-1，区别在于，第一极性物质聚脲在第一涂层中的质量占比为90％；第二极性物质PAM在第二涂层中的质量占比为90％。正极活性物质LiNi 0.6Co 0.2Mn 0.2O 2、正极用粘结剂PVDF、导电碳的质量比为97∶1.2∶1.8。负极活性物质碳硅混合物、负极用粘结剂、碳纳米管的质量比为97∶3∶0。
实施例3-5：
锂离子电池的制备过程整体上参照实施例3-1，区别在于，第一极性物质聚脲在第一涂层中的质量占比为92％；第二极性物质PAM在第二涂层中的质量占比为92％。正极活性物质LiNi 0.6Co 0.2Mn 0.2O 2、正极用粘结剂PVDF、导电碳的质量比为97∶1.5∶0.5。负极活性物质碳硅混合物、负极用粘结剂、碳纳米管的质量比为96.8∶3.2∶0。
实施例4-1：
1、隔离膜的制备
1)将第一极性物质PEO、第一增强剂PVDF、氧化铝按照质量比为80∶14∶6的比例溶于NMP中，搅拌均匀获得第一涂层浆料，用凹版涂布将第一涂层浆料涂布于PE基膜的A面(PE基膜靠近正极的一面)。
2)将第二极性物质PEI和第一增强剂PVDF按照质量比为80∶20的比例溶于去离子水中，搅拌均匀获得第二涂层浆料，用凹版涂布将第二涂层浆料涂布于PE基膜的B面(PE基膜靠近负极的一面)。
3)将经过步骤1)涂布第一涂层浆料和步骤2)涂布第二涂层浆料后的PE基膜在60℃烘干1h，在PE基膜的两表面形成第一涂层和第二涂层，制备获得隔离膜。
其中，第一增强剂在第一涂层中的质量含量k 1与第二增强剂在第二涂层中的质量含量k 2的比值
Figure PCTCN2021108971-appb-000069
为0.7∶1。
2、正极的制备
将正极活性物质LiNi 0.6Co 0.2Mn 0.2O 2、正极用粘结剂PVDF、导电碳按照质量比为97∶1∶2混合，并溶于NMP中，搅拌6h获得正极浆料，将正极浆料涂覆于铝箔上，烘干，冷压后制备获得正极。
3、负极的制备
将SA和SBR按照质量比80∶20混合得到负极用粘结剂，再将负极活性物质碳硅混合物(C∶Si＝95∶5)、负极用粘结剂、碳纳米管按照质量比为97∶2.5∶0.5混合后，溶于水中，搅拌6h获得负极浆料，将负极浆料涂覆于铜箔上，烘干，冷压后制备获得负极。
4、电池的制备
将正极、隔离膜、负极按顺序叠好，其中，将隔离膜的第一涂层与正极接触，将隔离膜的第二涂层与负极接触，然后卷绕得到裸电芯。将裸电芯放入铝壳内，焊接顶盖，经过注液，高温静置，化成，老化，等工序获得锂离子电池。
实施例4-2：
锂离子电池的制备过程整体上参照实施例4-1，区别在于，第一极性物质PEO、第一增强剂PVDF、氧化铝的质量比为80∶16.6∶3.4。第一增强剂在第一涂层中的质量含量k 1与第二增强剂在第二涂层中的质量含量k 2的比值
Figure PCTCN2021108971-appb-000070
为0.8∶1。
实施例4-3：
锂离子电池的制备过程整体上参照实施例4-1，区别在于，第一极性物质PEO、第一增强剂PVDF、氧化铝的质量比为80∶18∶2。第一增强剂在第一涂层中的质量含量k 1与第二增强剂在第二涂层中的质量含量k 2的比值
Figure PCTCN2021108971-appb-000071
为0.9∶1。
实施例4-4：
锂离子电池的制备过程整体上参照实施例4-1，区别在于，第一极性物质PEO、第一增强剂PVDF、氧化铝的质量比为80∶19∶1。第一增强剂在第一涂层中的质量含量k 1与第二增强剂在第二涂层中的质量含量k 2的比值
Figure PCTCN2021108971-appb-000072
为0.95∶1。
实施例4-5：
锂离子电池的制备过程整体上参照实施例4-1，区别在于，第一极性物质PEO、第一增强剂PVDF的质量比为80∶20。第一增强剂在第一涂层中的质量含量k 1与第二增强剂在第二涂层中的质量含量k 2的比值
Figure PCTCN2021108971-appb-000073
为1∶1。
实施例5-1：
1、隔离膜的制备
1)将第一极性物质PAM、第一增强剂PVDF、氧化铝按照质量比为80∶17.4∶2.6的比例溶于NMP中，搅拌均匀获得第一涂层浆料，用凹版涂布将第一涂层浆料涂布于PE基膜的A面(PE基膜靠近正极的一面)。
2)将第二极性物质PEO和第一增强剂PVDF按照质量比为83∶17的比例溶于去离子水中，搅拌均匀获得第二涂层浆料，用凹版涂布将第二涂层浆料涂布于PE基膜的B面(PE基膜靠近负极的一面)。
3)将经过步骤1)涂布第一涂层浆料和步骤2)涂布第二涂层浆料后的PE基膜在60℃烘干1h，在PE基膜的两表面形成第一涂层和第二涂层，制备获得隔离膜。
其中，第一极性物质在第一涂层中的质量含量w 1与第一增强剂在第一涂层中的质量含量k 1的质量之比
Figure PCTCN2021108971-appb-000074
为4.6∶1；第二涂层包括第二增强剂，第二极性物质在第二涂层中的质量含量w 2与第二增强剂在第二涂层中的质量含量k 2的质量之比
Figure PCTCN2021108971-appb-000075
为4.9∶1。
2、正极的制备
将正极活性物质LiNi 0.6Co 0.2Mn 0.2O 2、正极用粘结剂PVDF、导电碳按照质量比为97∶1∶2混合，并溶于NMP中，搅拌6h获得正极浆料，将正极浆料涂覆于铝箔上，烘干，冷压后制备获得正极。
3、负极的制备
将SA和SBR按照质量比80∶20混合得到负极用粘结剂，再将负极活性物质碳硅混合物(C∶Si＝95∶5)、负极用粘结剂、碳纳米管 按照质量比为97∶2.5∶0.5混合后，溶于水中，搅拌6h获得负极浆料，将负极浆料涂覆于铜箔上，烘干，冷压后制备获得负极。
4、电池的制备
将正极、隔离膜、负极按顺序叠好，其中，隔离膜的第一涂层与正极接触，隔离膜的第二涂层与负极接触，然后卷绕得到裸电芯。将裸电芯放入铝壳内，焊接顶盖，经过注液，高温静置，化成，老化，等工序获得锂离子电池。
实施例5-2：
锂离子电池的制备过程整体上参照实施例5-1，区别在于，第一极性物质PAM、第一增强剂PVDF、氧化铝的质量比为80∶16∶4。第二极性物质PEO、第二增强剂PVDF的质量比为83.4∶16.6。
第一极性物质在第一涂层中的质量含量w 1与第一增强剂在第一涂层中的质量含量k 1的质量之比
Figure PCTCN2021108971-appb-000076
为5∶1；第二极性物质在第二涂层中的质量含量w 2与第二增强剂在第二涂层中的质量含量k 2的质量之比
Figure PCTCN2021108971-appb-000077
为5∶1。
实施例5-3：
锂离子电池的制备过程整体上参照实施例5-1，区别在于，第一极性物质PAM、第一增强剂PVDF、氧化铝按照质量比为80∶15∶5。第二极性物质PEO、第二增强剂PVDF、氧化铝的质量比为84.2∶15.8。
第一极性物质在第一涂层中的质量含量w 1与第一增强剂在第一涂层中的质量含量k 1的质量之比
Figure PCTCN2021108971-appb-000078
为5.3∶1；第二极性物质在第二涂层中的质量含量w 2与第二增强剂在第二涂层中的质量含量k 2的质 量之比
Figure PCTCN2021108971-appb-000079
为5.3∶1。
实施例5-4：
锂离子电池的制备过程整体上参照实施例5-1，区别在于，第一极性物质PAM、第一增强剂PVDF、氧化铝按照质量比为80∶13.3∶6.7。第二极性物质PEO、第二增强剂PVDF的质量比为86∶14。
第一极性物质在第一涂层中的质量含量w 1与第一增强剂在第一涂层中的质量含量k 1的质量之比
Figure PCTCN2021108971-appb-000080
为6∶1；第二极性物质在第二涂层中的质量含量w 2与第二增强剂在第二涂层中的质量含量k 2的质量之比
Figure PCTCN2021108971-appb-000081
为6∶1。
实施例5-5：
锂离子电池的制备过程整体上参照实施例5-1，区别在于，第一极性物质PAM、第一增强剂PVDF、氧化铝的质量比为80∶10∶10。第二极性物质PEO、第二增强剂PVDF的质量比为89∶11。
第一极性物质在第一涂层中的质量含量w 1与第一增强剂在第一涂层中的质量含量k 1的质量之比
Figure PCTCN2021108971-appb-000082
为8∶1；第二极性物质在第二涂层中的质量含量w 2与第二增强剂在第二涂层中的质量含量k 2的质量之比
Figure PCTCN2021108971-appb-000083
为8∶1。
实施例5-6：
锂离子电池的制备过程整体上参照实施例5-1，区别在于，第一极性物质PAM、第一增强剂PVDF、氧化铝按照质量比为80∶8.9∶11.1。第二极性物质PEO、第二增强剂PVDF、氧化铝按照质量比为90∶10。
第一极性物质在第一涂层中的质量含量w 1与第一增强剂在第一涂层中的质量含量k 1的质量之比
Figure PCTCN2021108971-appb-000084
为9∶1；第二涂层包括第二增强剂，第二极性物质在第二涂层中的质量含量w 2与第二增强剂在第二涂层中的质量含量k 2的质量之比
Figure PCTCN2021108971-appb-000085
为9∶1。
实施例5-7：
锂离子电池的制备过程整体上参照实施例5-1，区别在于，第一极性物质PAM、第一增强剂PVDF、氧化铝按照质量比为80∶8.6∶11.4。第二极性物质PEO、第二增强剂PVDF的质量比为90.3∶9.7。
第一极性物质在第一涂层中的质量含量w 1与第一增强剂在第一涂层中的质量含量k 1的质量之比
Figure PCTCN2021108971-appb-000086
为9.3∶1；第二涂层包括第二增强剂，第二极性物质在第二涂层中的质量含量w 2与第二增强剂在第二涂层中的质量含量k 2的质量之比
Figure PCTCN2021108971-appb-000087
为9.3∶1。
实施例6-1：
1、隔离膜的制备
1)将第一极性物质PEO、第一增强剂PVDF按照质量比为80∶20的比例溶于NMP中，搅拌均匀获得第一涂层浆料，用凹版涂布将第一涂层浆料涂布于PE基膜的A面(PE基膜靠近正极的一面)。
2)将第二极性物质PEO和第一增强剂PVDF按照质量比为80∶20的比例溶于去离子水中，搅拌均匀获得第二涂层浆料，用凹版涂布将第二涂层浆料涂布于PE基膜的B面(PE基膜靠近负极的一面)。
3)将经过步骤1)涂布第一涂层浆料和步骤2)涂布第二涂层浆 料后的PE基膜在60℃烘干1h，在PE基膜的两表面形成第一涂层和第二涂层，制备获得隔离膜。
2、正极的制备
将正极活性物质LiNi 0.6Co 0.2Mn 0.2O 2、正极用粘结剂PVDF、导电碳按照质量比为97∶1∶2混合，并溶于NMP中，搅拌6h获得正极浆料，将正极浆料涂覆于铝箔上，烘干，冷压后制备获得正极。
3、负极的制备
将SA和SBR按照质量比80∶20混合得到负极用粘结剂，再将负极活性物质碳硅混合物(C∶Si＝95∶5；Si的粒径为0.05μm)、负极用粘结剂、碳纳米管按照质量比为95.9∶2.5∶1.6混合后，溶于水中，搅拌6h获得负极浆料，将负极浆料涂覆于铜箔上，烘干，冷压后制备获得负极。
4、电池的制备
将正极、隔离膜、负极按顺序叠好，其中，将隔离膜的第一涂层与正极接触，将隔离膜的第二涂层与负极接触，然后卷绕得到裸电芯。将裸电芯放入铝壳内，焊接顶盖，经过注液，高温静置，化成，老化，等工序获得锂离子电池。
实施例6-2：
锂离子电池的制备过程整体上参照实施例6-1，区别在于，负极活性物质碳硅混合物(C∶Si＝95∶5；Si的粒径为0.1μm)、负极用粘结剂、碳纳米管按照质量比为96.7∶2.5∶0.8。
实施例6-3：
与实施例6-1基本相同，区别在于，负极活性物质碳硅混合物(Si的粒径为0.3μm)、负极用粘结剂、碳纳米管按照质量比为97∶2.5∶0.5。
实施例6-4：
锂离子电池的制备过程整体上参照实施例6-1，区别在于，负极活性物质碳硅混合物(C∶Si＝95∶5；Si的粒径为0.5μm)、负极用粘结剂、碳纳米管按照质量比为96.8∶2.5∶0.7。
实施例6-5：
锂离子电池的制备过程整体上参照实施例6-1，区别在于，负极活性物质碳硅混合物(Si的粒径为0.6μm)、负极用粘结剂、碳纳米管按照质量比为96∶2.5∶1.5。
实施例7-1：
1、隔离膜的制备
1)将第一极性物质PEO、第一增强剂PVDF按照质量比为80∶20的比例溶于NMP中，搅拌均匀获得第一涂层浆料，用凹版涂布将第一涂层浆料涂布于PE基膜的A面(PE基膜靠近正极的一面)。
2)将第二极性物质PEO和第一增强剂PVDF按照质量比为80∶20的比例溶于去离子水中，搅拌均匀获得第二涂层浆料，用凹版涂布将第二涂层浆料涂布于PE基膜的B面(PE基膜靠近负极的一面)。
3)将经过步骤1)涂布第一涂层浆料和步骤2)涂布第二涂层浆料后的PE基膜在60℃烘干1h，在PE基膜的两表面形成第一涂层和 第二涂层，制备获得隔离膜。
2、正极的制备
将正极活性物质LiNi 0.4Co 0.4Mn 0.2O 2、正极用粘结剂PVDF、导电碳按照质量比为97∶1∶2混合，并溶于NMP中，搅拌6h获得正极浆料，将正极浆料涂覆于铝箔上，烘干，冷压后制备获得正极。
3、负极的制备
将SA和SBR按照质量比80∶20混合得到负极用粘结剂，再将负极活性物质碳硅混合物(C∶Si＝95∶5；Si的粒径为0.3μm)、负极用粘结剂、碳纳米管按照质量比为97∶2.5∶0.5混合后，溶于水中，搅拌6h，得到负极浆料，将负极浆料涂覆于铜箔上，烘干，冷压后制备获得负极。
4、电池的制备
将正极、隔离膜、负极按顺序叠好，其中，将隔离膜的第一涂层与正极接触，将隔离膜的第二涂层与负极接触，然后卷绕得到裸电芯。将裸电芯放入铝壳内，焊接顶盖，经过注液，高温静置，化成，老化，等工序获得锂离子电池。
实施例7-2：
锂离子电池的制备过程整体上参照实施例7-1，区别在于，正极活性物质为LiNi 0.5Co 0.2Mn 0.3O 2。
实施例7-3：
锂离子电池的制备过程整体上参照实施例7-1，区别在于，正极活性物质LiNi 0.6Co 0.2Mn 0.2O 2。
实施例7-4：
锂离子电池的制备过程整体上参照实施例7-1，区别在于，正极活性物质为LiNi 0.8Co 0.1Mn 0.1O 2。
实施例7-5：
锂离子电池的制备过程整体上参照实施例7-1，区别在于，正极活性物质为LiNi 0.9Co 0.05Mn 0.05O 2。
实施例8-1：
1、隔离膜的制备
1)将PEO和PAM按质量比1.8∶1混合得到第一极性物质，第一极性物质和第一增强剂PVDF按照质量比为80∶20的比例溶于NMP中，搅拌均匀获得第一涂层浆料，用凹版涂布将第一涂层浆料涂布于PE基膜的A面(PE基膜靠近正极的一面)。
2)将PEI和PEO按质量比1.8∶1混合得到第二极性物质，第二极性物质和第一增强剂PVDF按照质量比为80∶20的比例溶于去离子水中，搅拌均匀获得第二涂层浆料，用凹版涂布将第二涂层浆料涂布于PE基膜的B面(PE基膜靠近负极的一面)。
3)将经过步骤1)涂布第一涂层浆料和步骤2)涂布第二涂层浆料后的PE基膜在60℃烘干1h，在PE基膜的两表面形成第一涂层和第二涂层，制备获得隔离膜。
2、正极的制备
将正极活性物质LiNi 0.4Co 0.4Mn 0.4O 2、正极用粘结剂PVDF、导电碳按照质量比为97∶1∶2混合，并溶于NMP中，搅拌6h获得正极 浆料，将正极浆料涂覆于铝箔上，烘干，冷压后制备获得正极。
3、负极的制备
将SA和SBR按照质量比80∶20混合得到负极用粘结剂，再将负极活性物质碳硅混合物(C∶Si＝95∶5；Si的粒径为0.3μm)、负极用粘结剂、碳纳米管按照质量比为97∶2.5∶0.5混合后，溶于水中，搅拌6h获得负极浆料，将负极浆料涂覆于铜箔上，烘干，冷压后制备获得负极。
4、电池的制备
将正极、隔离膜、负极按顺序叠好，其中，将隔离膜的第一涂层与正极接触，将隔离膜的第二涂层与负极接触，然后卷绕得到裸电芯。将裸电芯放入铝壳内，焊接顶盖，经过注液，高温静置，化成，老化，等工序获得锂离子电池。
实施例8-2：
锂离子电池的制备过程整体上参照实施例8-1，区别在于，第一极性物质中PEO和PAM的质量比2∶1；第一极性物质中PEI和PEO的质量比2∶1。
实施例8-3：
锂离子电池的制备过程整体上参照实施例8-1，区别在于，第一极性物质中PEO和PAM的质量比3∶1；第一极性物质中PEI和PEO的质量比3∶1。
实施例8-4：
锂离子电池的制备过程整体上参照实施例8-1，区别在于，第一 极性物质中PEO和PAM的质量比4.5∶1；第一极性物质中PEI和PEO的质量比4.5∶1。
实施例8-5：
锂离子电池的制备过程整体上参照实施例8-1，区别在于，第一极性物质中PEO和PAM的质量比5∶1；第一极性物质中PEI和PEO的质量比5∶1。
实施例8-6：
锂离子电池的制备过程整体上参照实施例8-1，区别在于，第一极性物质中PEO和PAM的质量比6∶1；第一极性物质中PEI和PEO的质量比6∶1。
实施例8-7：
锂离子电池的制备过程整体上参照实施例8-1，区别在于，第一极性物质中PEO和PAM的质量比6.3∶1；第一极性物质中PEI和PEO的质量比6.3∶1。
对比例1：
锂离子电池的制备过程整体上参照实施例1-2，区别在于，不含有第一极性物质PEO和第二极性物质PEI。
对比例2：
锂离子电池的制备过程整体上参照实施例1-2，区别在于，不含有第一极性物质中PEO，第二极性物质PEI在第二涂层中的占比为100％。
对比例3：
锂离子电池的制备过程整体上参照实施例1-2，区别在于，不含有第二极性物质中PEI，第一极性物质PEO在第一涂层中的占比为100％。
二、性能测试
1、正负极表面与隔离膜涂层之间剥离力的测试方法
将实施例和对比例的隔离膜，分别裁成长100mm、宽10mm的测试样品。取一条宽度25mm的不锈钢板，贴双面胶(宽度11mm)，将测试样品粘贴在不锈钢板上的双面胶上，用2000g压辊在其表面来回滚压三次(300mm/min)。将测试样品180度弯折，手动将测试样品的有机-无机混合层与基膜剥开25mm，将该测试样品固定在试验机上(例如INSTRON 336)，使剥离面与试验机力线保持一致，试验机以30mm/min连续剥离，得到的剥离力曲线，取平稳断的均值作为剥离力F0，则通过以下公式算出测试样品中有机-无机混合层与集流体之间的粘结力F。F＝F0/测试样品的宽度(F的计量单位：N/m)。
2、红外光谱测试
依据标准GB/T6040-2002红外光谱分析方法，采用美国尼高力(nicolet)公司的IS10型傅里叶变换红外光谱仪。将实施例和对比例中获得的正极浆料抽滤后获得正极粉体；将实施例和对比例获得第一涂层浆料涂覆在PE基膜上，抽滤后，去除PE基膜，得到第一涂层粉体。将正极粉体和第一涂层粉体混合，进一步烘干后获得混合粉体；将混合粉体进行红外测试。第二涂层和负极间的红外测试方法同上。
3、常温循环性能：在25℃的环境中，对所有实施例和对比例的 电池在1C的充电电流下进行恒流和恒压充电，直到上限电压为4.35V。然后，在1C的放电电流下进行恒流放电，直到最终电压为2.8V，记录此时的首次放电容量值C0。随后将所有实施例和对比例的电池在3.3-4.3V的电压下以0.33C0充电，1C0放电，不断循环，记录循环1000次后的放电容量Cn。第1000次循环的容量保持率＝(第1000次循环的放电容量/首次循环的放电容量)×100％。
4、高倍率放电容量：在25℃的环境中，对所有实施例和对比例的电池在1/3C的充电电流下进行恒流和恒压充电，直到上限电压为4.35V。然后，在1/3C，3C，5C的放电电流下进行恒流放电，直到最终电压为2.8V，记录此时放电容量值。
5、卷绕组件循环膨胀率测试方法
将热压完的裸电芯，用游标卡尺测量厚度，循环1000圈后，拆解电芯测量裸电芯厚度，膨胀率＝(循环后裸电芯直径-循环前裸电芯直径)/循环前裸电芯厚度。
Figure PCTCN2021108971-appb-000088
Figure PCTCN2021108971-appb-000089
Figure PCTCN2021108971-appb-000090
Figure PCTCN2021108971-appb-000091
Figure PCTCN2021108971-appb-000092
Figure PCTCN2021108971-appb-000093
Figure PCTCN2021108971-appb-000094
Figure PCTCN2021108971-appb-000095
Figure PCTCN2021108971-appb-000096
根据上述结果可知，表1中，
Figure PCTCN2021108971-appb-000097
和
Figure PCTCN2021108971-appb-000098
反映隔离膜中第一极性物质与正极用粘结剂的相对含量关系、第二极性物质与负极中粘结剂的相对含量关系对电池性能的影响。实施例1-1～1-7通过调整
Figure PCTCN2021108971-appb-000099
以及
Figure PCTCN2021108971-appb-000100
电池性能例如循环膨胀率、循环1000圈容量保持率以及5C放电容量均取得了良好的效果，尤其是
Figure PCTCN2021108971-appb-000101
在(80～100)∶1、
Figure PCTCN2021108971-appb-000102
在(32～50)∶1时，电池性能更加。
表2中，
Figure PCTCN2021108971-appb-000103
反映隔离膜第一极性物质在第一涂层中相对含量与第二极性物质在第二涂层中相对含量之比对电池性能的影响。实施例2-1～2-4通过调整
Figure PCTCN2021108971-appb-000104
电池性能例如循环膨胀率、循环1000圈容量保持率以及5C放电容量均取得了良好的效果，尤其是
Figure PCTCN2021108971-appb-000105
在1∶(1～1.3)范围时，电池性能更加。
表3中，在保持
Figure PCTCN2021108971-appb-000106
基本为定值时，实施例3-1～3-5通过综合调整第一极性物质在第一涂层中的质量含量w 1、正极用粘结剂在正极的膜层中的质量含量m 1、第二极性物质在第二涂层中的质量含量w 2、负极用粘结剂在负极的膜层中的质量含量m 2，使电池性能例如循环膨胀率、循环1000圈容量保持率以及5C放电容量均取得了良好的效果，尤其是m 1在1～1.2％、m 2在2％～3％范围内，电池性能更加。
表4中，实施例4-1～4-5通过调整第一增强剂在第一涂层中的质量含量k 1与第二增强剂在第二涂层中的质量含量k 2的质量之比，电池性能例如循环膨胀率、循环1000圈容量保持率以及5C放电容量均取得了良好的效果，尤其是
Figure PCTCN2021108971-appb-000107
在(0.8-1)∶1范围内，电池性能更加。
表5中，实施例5-1～5-7通过调整第一极性物质在第一涂层中的 质量含量w 1与第一增强剂在第一涂层中的质量含量k 1的质量之比
Figure PCTCN2021108971-appb-000108
第二极性物质在第二涂层中的质量含量w 2与第二增强剂在第二涂层中的质量含量k2的质量之比
Figure PCTCN2021108971-appb-000109
增强剂与极性物质之间易形成氢键，可以降低裸电芯膨胀，从而可以提升电池性能。电池性能例如循环膨胀率、循环1000圈容量保持率以及5C放电容量均取得了良好的效果，尤其是
Figure PCTCN2021108971-appb-000110
均在(5～9)∶1范围内，电池性能更加。
表6中，实施例6-1～6-5反映了硅的粒径对电池性能的影响。电池性能例如循环膨胀率、循环1000圈容量保持率以及5C放电容量均取得了良好的效果，尤其是硅的粒径在0.1～0.5微米范围内，电池性能更加。
表7中，实施例7-1～7-4中，通过调整三元正极材料中的Ni含量，可以显著改善裸电芯膨胀，电池性能例如循环膨胀率、循环1000圈容量保持率均取得了良好的效果，尤其是Ni含量在0.5～0.9范围内，电池性能更加。
表8中，实施例8-1～8-7中，通过调整聚氧化乙烯与聚丙烯酰胺的质量比值C1和聚乙烯亚胺与聚氧化乙烯的质量比值C2，电池性能例如循环膨胀率、循环1000圈容量保持率以及5C放电容量均取得了良好的效果，尤其是C1和C2取值分别在(2～6)∶1范围内，电池性能更加。
而相对于此，表9中，对比例1～3电池性能例如循环膨胀率、循环1000圈容量保持率以及5C放电容量方面，未取得有效提高。
此外，如图1所示，第一极性物质为PEO，第一增强剂为PVDF，正极用粘结剂为PEO，第二极性物质为PEI，第二增强剂为PVDF，负极用粘结剂为SA和SBR，负极活性物质为碳硅混合物。
在正极与隔膜之间，正极用粘结剂PVDF上的F与第一极性物质PEO的H形成氢键。
在第一涂层中，第一增强剂PVDF上的F与第一极性物质PEO的H形成氢键。
在负极与隔离膜之间，由于电负性N＜O＜F，碳硅混合物中-OH上的H比-NH 2的H更缺电子，因此，第二极性物质PEI中-NH 2上的N与碳硅混合物中-OH上的H易形成氢键。同理，第二极性物质PEI中-NH 2上的N与负极用粘结剂SA中-COOH上的H形成氢键。碳硅混合物中-OH上的H与SA中-COOH上的H之间可以形成氢键。
在第二涂层中，第二增强剂PVDF的F与PEI的H形成氢键。
如图2所示，在3200cm -1～3600cm -1之间，是氢键的峰，对比例1未添加第一极性物质或第二极性物质时，几乎不产生氢键，而实施例1由于AB面均产生氢键连接，所以峰宽且明显。另外需要说明的是，O-H-O，F-H-O，N-H-O，F-H-N这四种氢键键键能大小排序为F-H-O＞F-H-N＞O-H-O＞N-H-O，键能在25-40KJ/mol之间差别比较小，一个波数范围存在多个氢键，正常情况下氢键越多，峰显示的越多、也越宽。
需要说明的是，本申请不限定于上述实施方式。上述实施方式仅为示例，在本申请的技术方案范围内具有与技术思想实质相同的构成、发挥相同作用效果的实施方式均包含在本申请的技术范围内。此外，在不脱离本申请主旨的范围内，对实施方式施加本领域技术人员能够想到的各种变形、将实施方式中的一部分构成要素加以组合而构筑的其它方式也包含在本申请的范围内。

Claims (17)

  1. 一种电池，其特征在于，
    所述电池包括正极、隔离膜、负极，所述隔离膜包括基膜、设于所述基膜第一表面的第一涂层、以及设于所述基膜第二表面的第二涂层，其中，
    所述第一涂层中包括第一极性物质，所述第一极性物质包括聚烯烃酰胺类、聚烯烃亚胺类、聚氧化烯烃类、聚氨酯类、聚脲类物质中的一种或多种，所述第一极性物质与所述正极的正极用粘结剂之间具有氢键；
    所述第二涂层中包括第二极性物质，所述第二极性物质包括聚烯烃酰胺类、聚烯烃亚胺类、聚氧化烯烃类、聚氨酯类、聚脲类物质中的一种或多种，所述第二极性物质与所述负极的负极用粘结剂和/或负极活性组分之间具有氢键。
  2. 根据权利要求1所述的电池，其特征在于，
    所述第一涂层与所述正极的剥离力不低于0.075N，可选为0.075N～0.125N；所述第二涂层与所述负极的剥离力不低于0.075N，可选为0.075N～0.15N。
  3. 根据权利要求1或2任一项所述的电池，其特征在于，
    所述第一极性物质在所述第一涂层中的质量含量w 1与所述正极用粘结剂在所述正极的膜层中的质量含量m 1的比值
    Figure PCTCN2021108971-appb-100001
    为(80～100)：1；
    所述第二极性物质在所述第二涂层中的质量含量w 2与所述负极用粘结剂在所述负极的膜层中的质量含量m 2的比值
    Figure PCTCN2021108971-appb-100002
    为(32～50)：1。
  4. 根据权利要求1至3任一项所述的电池，其特征在于，
    所述第一极性物质在所述第一涂层中的质量含量w 1与所述第二极性物质在所述第二涂层中的质量含量w 2的比值
    Figure PCTCN2021108971-appb-100003
    为1：(1～1.3)。
  5. 根据权利要求1至4任一项所述的电池，其特征在于，
    所述第一极性物质在所述第一涂层中的质量含量w 1为80％～90％，所述正极用粘结剂在所述正极的膜层中的质量含量m 1为0.9％～1.2％。
    所述第二极性物质在所述第二涂层中的质量含量w 2为80％～90％，所述负极用粘结剂在所述负极的膜层中的质量含量m 2为2％～3％。
  6. 根据权利要求1至5任一项所述的电池，其特征在于，
    所述第一极性物质包括聚氧化乙烯和聚丙烯酰胺；其中，所述聚氧化乙烯与聚丙烯酰胺的质量比值C1为(2～6)：1。
    所述第二极性物质包括聚乙烯亚胺和聚氧化乙烯；其中，所述聚乙烯亚胺与聚氧化乙烯的质量比值C2为(2～6)：1。
  7. 根据权利要求1至6任一项所述的电池，其特征在于，
    所述第一涂层包括第一增强剂，所述第一极性物质在所述第一涂层中的质量含量w 1与所述第一增强剂在所述第一涂层中的质量含量 k 1的质量之比
    Figure PCTCN2021108971-appb-100004
    为(5～9)：1；所述第二涂层包括第二增强剂，所述第二极性物质在第二涂层中的质量含量w 2与所述第二增强剂在所述第二涂层中的质量含量k 2的质量之比
    Figure PCTCN2021108971-appb-100005
    为(5～9)：1。
  8. 根据权利要求7所述的电池，其特征在于，
    所述第一增强剂在所述第一涂层中的质量含量k 1不高于所述第二增强剂在所述第二涂层中的质量含量k 2。
  9. 根据权利要求7所述的电池，其特征在于，
    所述第一增强剂在所述第一涂层中的质量含量k 1与所述第二增强剂在所述第二涂层中的质量含量k 2的比值
    Figure PCTCN2021108971-appb-100006
    为(0.8～1)：1。
  10. 根据权利要求7所述的电池，其特征在于，
    所述第一增强剂或第二增强剂包括聚偏二氟乙烯、海藻酸钠中的一种或多种。
    所述正极用粘结剂包括聚偏氟乙烯，所述负极用粘结剂包括丁苯橡胶、海藻酸钠中的一种以上。
  11. 根据权利要求1至10任一项所述的电池，其特征在于，
    所述负极活性组分包括硅碳混合物，所述硅碳混合物中，硅的粒径为0.1～0.5微米，碳为人造石墨和天然石墨的混合碳，所述硅碳混合物在所述负极的膜层中的含量为95％-97％。
  12. 根据权利要求1至11任一项所述的电池，其特征在于，
    所述第一涂层和所述第二涂层的质量比为1:(1～1.5)。
  13. 根据权利要求7所述的电池，其特征在于，
    所述第一涂层由第一涂层浆料制备获得，所述第一涂层浆料包括所述第一极性物质、所述第一增强剂和第一溶剂；其中，
    所述第一涂层浆料的粘度为8000mpa.s～12000mpa.s。
    所述第二涂层由第二涂层浆料制备获得，所述第二涂层浆料包括所述第二极性物质、所述第二增强剂和第二溶剂；其中，
    所述第二涂层浆料的粘度为5000mpa.s～20000mpa.s。
  14. 根据权利要求1至13任一项所述的电池，其特征在于，
    所述正极包括正极材料LiNixCoyMnzO 2，x+y+z＝1，x＝0.5～0.9；可选为x＝0.5～0.7、x＝0.8～0.9。
  15. 一种电池模块，其特征在于，包括权利要求1至14任一项所述的电池。
  16. 一种电池包，其特征在于，包括权利要求15所述的电池模块。
  17. 一种用电装置，其特征在于，包括选自权利要求1至14任 一项所述的电池、权利要求15所述的电池模块或权利要求16所述的电池包中的一种以上。
PCT/CN2021/108971 2021-07-28 2021-07-28 一种电池、电池模块、电池包和用电装置 WO2023004633A1 (zh)

Priority Applications (6)

Application Number Priority Date Filing Date Title
PCT/CN2021/108971 WO2023004633A1 (zh) 2021-07-28 2021-07-28 一种电池、电池模块、电池包和用电装置
CN202180071500.2A CN116349077A (zh) 2021-07-28 2021-07-28 一种电池、电池模块、电池包和用电装置
KR1020227029101A KR20230019406A (ko) 2021-07-28 2021-07-28 배터리, 배터리 모듈, 배터리 팩 및 전기 소모 장치
EP21927065.9A EP4148891A4 (en) 2021-07-28 2021-07-28 BATTERY, BATTERY MODULE, BATTERY PACK AND ELECTRICAL DEVICE
JP2022550822A JP7432753B2 (ja) 2021-07-28 2021-07-28 電池、電池モジュール、電池パックおよび電気設備
US17/937,768 US20230117614A1 (en) 2021-07-28 2022-10-03 Battery, battery module, battery pack and electric device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/CN2021/108971 WO2023004633A1 (zh) 2021-07-28 2021-07-28 一种电池、电池模块、电池包和用电装置

Related Child Applications (1)

Application Number Title Priority Date Filing Date
US17/937,768 Continuation US20230117614A1 (en) 2021-07-28 2022-10-03 Battery, battery module, battery pack and electric device

Publications (1)

Publication Number Publication Date
WO2023004633A1 true WO2023004633A1 (zh) 2023-02-02

Family

ID=85086116

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CN2021/108971 WO2023004633A1 (zh) 2021-07-28 2021-07-28 一种电池、电池模块、电池包和用电装置

Country Status (6)

Country Link
US (1) US20230117614A1 (zh)
EP (1) EP4148891A4 (zh)
JP (1) JP7432753B2 (zh)
KR (1) KR20230019406A (zh)
CN (1) CN116349077A (zh)
WO (1) WO2023004633A1 (zh)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN116799437A (zh) * 2023-08-18 2023-09-22 荣耀终端有限公司 电池及电子设备

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103247819A (zh) * 2012-02-06 2013-08-14 三星Sdi株式会社 锂二次电池
CN109792020A (zh) * 2017-01-06 2019-05-21 株式会社Lg化学 包括功能性粘合剂的电池隔板以及包括该电池隔板的电化学装置
CN109841783A (zh) * 2017-11-28 2019-06-04 宁德时代新能源科技股份有限公司 锂离子电池及其隔离膜
CN110197922A (zh) * 2018-02-26 2019-09-03 宁德新能源科技有限公司 隔离膜和锂离子电池
CN111370761A (zh) * 2020-03-25 2020-07-03 中航锂电技术研究院有限公司 Peo膜及其制备方法与固态电池
WO2020141684A1 (ko) * 2019-01-04 2020-07-09 삼성에스디아이 주식회사 리튬 이차 전지용 분리막 및 이를 포함하는 리튬 이차 전지

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10243188B2 (en) * 2015-06-09 2019-03-26 GM Global Technology Operations LLC Separator for lithium-based batteries
JP6779157B2 (ja) 2017-02-22 2020-11-04 帝人株式会社 非水系二次電池用セパレータ及び非水系二次電池
TW202044646A (zh) 2019-04-04 2020-12-01 美商希爾格得有限公司 用於高能量可充電鋰電池之聚醯胺—醯亞胺塗覆分隔件
CN111403664A (zh) 2020-03-24 2020-07-10 珠海冠宇动力电池有限公司 一种聚苯脲隔膜及其制备方法和锂离子电池

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103247819A (zh) * 2012-02-06 2013-08-14 三星Sdi株式会社 锂二次电池
CN109792020A (zh) * 2017-01-06 2019-05-21 株式会社Lg化学 包括功能性粘合剂的电池隔板以及包括该电池隔板的电化学装置
CN109841783A (zh) * 2017-11-28 2019-06-04 宁德时代新能源科技股份有限公司 锂离子电池及其隔离膜
CN110197922A (zh) * 2018-02-26 2019-09-03 宁德新能源科技有限公司 隔离膜和锂离子电池
WO2020141684A1 (ko) * 2019-01-04 2020-07-09 삼성에스디아이 주식회사 리튬 이차 전지용 분리막 및 이를 포함하는 리튬 이차 전지
CN111370761A (zh) * 2020-03-25 2020-07-03 中航锂电技术研究院有限公司 Peo膜及其制备方法与固态电池

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See also references of EP4148891A4 *

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN116799437A (zh) * 2023-08-18 2023-09-22 荣耀终端有限公司 电池及电子设备
CN116799437B (zh) * 2023-08-18 2023-10-31 荣耀终端有限公司 电池及电子设备

Also Published As

Publication number Publication date
US20230117614A1 (en) 2023-04-20
EP4148891A1 (en) 2023-03-15
JP7432753B2 (ja) 2024-02-16
EP4148891A4 (en) 2024-06-19
CN116349077A (zh) 2023-06-27
JP2023538163A (ja) 2023-09-07
KR20230019406A (ko) 2023-02-08

Similar Documents

Publication Publication Date Title
US11114659B2 (en) Negative electrode sheet and secondary battery
US11978905B2 (en) Secondary battery, apparatus containing the secondary battery, method for the preparation of the secondary battery, and binder composition
WO2021008429A1 (zh) 二次电池及其相关的电池模块、电池包和装置
WO2021189424A1 (zh) 二次电池和含有该二次电池的装置
CN112349953A (zh) 一种锂离子电池
WO2023029002A1 (zh) 负极集流体、含有其的二次电池、电池模块、电池包及用电装置
WO2023004633A1 (zh) 一种电池、电池模块、电池包和用电装置
WO2021189423A1 (zh) 二次电池和含有该二次电池的装置
WO2023130910A1 (zh) 电池极片的制备方法、电池极片和二次电池
WO2023130791A1 (zh) 电极极片及其制备方法、二次电池、电池模块和电池包
WO2024021018A1 (zh) 干法电极用底涂胶及其制备方法、复合集流体、电池极片、二次电池、电池模块、电池包和用电装置
WO2023077516A1 (zh) 负极极片及其制备方法、二次电池、电池模块、电池包及用电装置
WO2023130210A1 (zh) 二次电池的补锂方法及充放电方法
WO2023044754A1 (zh) 粘结剂化合物、导电粘结剂及包含其的二次电池
CN115036458B (zh) 一种锂离子电池
US20220416305A1 (en) Battery Pack and Battery Cell
WO2024007149A1 (zh) 聚合物改性多孔材料、膜电极、二次电池和用电装置
WO2022246630A1 (zh) 二次电池、其制备方法和包含其的装置、以及粘结剂配方
WO2023216241A1 (zh) 二次电池及其制备方法、电池模块、电池包和用电装置
WO2023142934A1 (zh) 正极极片、二次电池及其制备方法和含有二次电池的装置
WO2023141954A1 (zh) 锂离子电池、电池模块、电池包和用电装置
WO2023060587A1 (zh) 负极极片、二次电池、电池模块、电池包及用电装置
WO2023240485A1 (zh) 正极极片及其制备方法、二次电池、电池模块、电池包及用电装置
WO2024082277A1 (zh) 负极极片、二次电池和用电装置
WO2024040585A1 (zh) 补锂浆料、正极浆料、二次电池、二次电池的制备方法和用电装置

Legal Events

Date Code Title Description
ENP Entry into the national phase

Ref document number: 2022550822

Country of ref document: JP

Kind code of ref document: A

ENP Entry into the national phase

Ref document number: 2021927065

Country of ref document: EP

Effective date: 20221010

NENP Non-entry into the national phase

Ref country code: DE