WO2023072110A1 - Battery - Google Patents

Battery Download PDF

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Publication number
WO2023072110A1
WO2023072110A1 PCT/CN2022/127500 CN2022127500W WO2023072110A1 WO 2023072110 A1 WO2023072110 A1 WO 2023072110A1 CN 2022127500 W CN2022127500 W CN 2022127500W WO 2023072110 A1 WO2023072110 A1 WO 2023072110A1
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WO
WIPO (PCT)
Prior art keywords
lithium
battery
negative electrode
hexafluoropropylene
battery according
Prior art date
Application number
PCT/CN2022/127500
Other languages
French (fr)
Chinese (zh)
Inventor
母英迪
张祖来
王海
李素丽
Original Assignee
珠海冠宇电池股份有限公司
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Application filed by 珠海冠宇电池股份有限公司 filed Critical 珠海冠宇电池股份有限公司
Publication of WO2023072110A1 publication Critical patent/WO2023072110A1/en

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Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/056Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes
    • H01M10/0564Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes the electrolyte being constituted of organic materials only
    • H01M10/0566Liquid materials
    • H01M10/0569Liquid materials characterised by the solvents
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/052Li-accumulators
    • H01M10/0525Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/056Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes
    • H01M10/0564Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes the electrolyte being constituted of organic materials only
    • H01M10/0566Liquid materials
    • H01M10/0567Liquid materials characterised by the additives
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/42Methods or arrangements for servicing or maintenance of secondary cells or secondary half-cells
    • H01M10/4235Safety or regulating additives or arrangements in electrodes, separators or electrolyte
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/409Separators, membranes or diaphragms characterised by the material
    • H01M50/449Separators, membranes or diaphragms characterised by the material having a layered structure
    • H01M50/457Separators, membranes or diaphragms characterised by the material having a layered structure comprising three or more layers
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/489Separators, membranes, diaphragms or spacing elements inside the cells, characterised by their physical properties, e.g. swelling degree, hydrophilicity or shut down properties
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M2300/00Electrolytes
    • H01M2300/0017Non-aqueous electrolytes
    • H01M2300/0025Organic electrolyte
    • H01M2300/0028Organic electrolyte characterised by the solvent
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

Definitions

  • the disclosure belongs to the technical field of batteries, and in particular relates to a battery.
  • lithium-ion batteries have been widely used in smartphones, tablet computers, smart wearables, power tools, and electric vehicles.
  • consumers' demands on the service life and application environment of lithium-ion batteries continue to increase, which requires lithium-ion batteries to have a long cycle life while taking into account high and low temperature performance.
  • the SEI film structure leads to the continuous increase of the negative electrode impedance and battery thickness, which in turn causes the battery temperature to continue to rise and cause safety accidents; on the other hand, the battery impedance increases at low temperatures, and the high SEI film impedance affects low-temperature discharge.
  • the purpose of this disclosure is to solve the problems of potential safety hazards in the use process of existing batteries, failure to balance battery cycle life and low temperature performance, and provide a battery with high voltage, long cycle life and low expansion performance .
  • a battery comprising a positive electrode sheet, a negative electrode sheet, a separator placed between the positive electrode sheet and the negative electrode sheet, and a non-aqueous electrolyte;
  • the non-aqueous electrolytic solution includes a non-aqueous organic solvent and an additive, wherein the non-aqueous organic solvent includes at least ethyl propionate; the additive includes 1,3-propane sultone and lithium difluorooxalate borate;
  • the diaphragm includes a base material, a heat-resistant layer and a glue layer, the heat-resistant layer is relatively arranged on both sides of the base material, and the glue layer is arranged on the heat-resistant layer;
  • the glue layer includes Adhesive, including hexafluoropropylene-vinylidene fluoride copolymer in the adhesive;
  • the ratio of the mass proportion of ethyl propionate in the non-aqueous electrolyte to the mass proportion of hexafluoropropylene (HFP) in the hexafluoropropylene-vinylidene fluoride copolymer is 0.2 to 60, exemplarily 0.26, 0.5, 1, 2.4, 5.8, 9.2, 11.3, 13.7, 15, 20, 30, 35, 36.7, 40, 50, 60 or any point value within the range composed of two pairs of the above point values. .
  • the change rate of the adhesive force between the adhesive layer of the separator and the positive and negative electrodes is within 10% in the first 100 cycles (including the 100th cycle) of the battery cycle, that is, when the battery cycle is ⁇ 100 cycles ( For example, when the battery is cycled for 1 week, 5 weeks, 10 weeks, 50 weeks or 100 cycles), the change rate of the adhesive force between the adhesive layer and the positive electrode sheet or the negative electrode sheet is within 10%.
  • the ratio of the mass proportion of ethyl propionate in the non-aqueous electrolyte to the mass proportion of hexafluoropropylene in the hexafluoropropylene-vinylidene fluoride copolymer is 0.5-35.
  • the mass proportion of hexafluoropropylene in the hexafluoropropylene-vinylidene fluoride copolymer is 1wt.% to 25wt.%, preferably 1.5wt.% to 15wt.%, exemplarily 1wt. %, 1.5wt.%, 2wt.%, 2.5wt.%, 3wt.%, 3.5wt.%, 5wt.%, 6.5wt.%, 9wt.%, 10wt.%, 15wt.%, 20wt.%, 23wt.%, 25wt.%, or any value within the range composed of the aforementioned pairwise values.
  • the hexafluoropropylene-vinylidene fluoride copolymer is, for example, polyvinylidene fluoride-hexafluoropropylene copolymer.
  • polyvinylidene fluoride-hexafluoropropylene copolymer refers to polyvinylidene fluoride modified by hexafluoropropylene.
  • the number average molecular weight of the polyvinylidene fluoride (PVDF) is 500,000 Da to 2 million Da, exemplarily 500,000 Da, 600,000 Da, 700,000 Da, 800,000 Da, and 1 million Da , 2,000,000 Da or any point value within the range composed of two pairs of the above point values.
  • the sum of the molecular weights of vinylidene fluoride units is 500,000 Da to 2 million Da, exemplarily 500,000 Da, 600,000 Da, and 700,000 Da .
  • the quality of ethyl propionate is 5wt.% ⁇ 60wt.% of the total mass of the nonaqueous electrolytic solution, (that is, the amount of ethyl propionate in the nonaqueous electrolytic solution % by mass) is 5wt.% ⁇ 60wt.%; preferably 10wt.% ⁇ 40wt.%, exemplarily 5wt.%, 6wt.%, 10wt.%, 12wt.%, 15wt.%, 20wt.%, 22wt.%, 23wt.%, 25wt.%, 30wt.%, 34wt.%, 35wt.%, 38wt.%, 40wt.%, 48wt.%, 50wt.%, 55wt.%, 60wt.% or the above Any point value within a range consisting of two pairs of values.
  • the additives used can be prepared by methods known in the art, or purchased from commercial channels.
  • the mass proportion of the 1,3-propane sultone is 0.5wt.% ⁇ 5wt.%, preferably 2 ⁇ 4wt.%, exemplarily 1wt.%, 2wt.%, 3wt.%, 3.5wt.%, 4wt.%, 4.5wt.%, 5wt.%, or any value within the range composed of the aforementioned pairwise values.
  • the mass proportion of lithium difluorooxalate borate is 0.01wt.% ⁇ 2wt.%, exemplarily 0.01wt.%, 0.02wt.%, 0.05wt. .%, 0.1wt.%, 0.2wt.%, 0.5wt.%, 1wt.%, 2wt.%, or any value within the range composed of the aforementioned pairwise values.
  • the additives may also include other additives, for example, the other additives may be tris(trimethylsilyl) phosphite, tris(trimethylsilyl) borate, bistrifluoro Lithium methanesulfonyl imide, lithium bisfluorosulfonyl imide, 1,3-propene sultone, vinyl sulfite, vinyl sulfate, vinylene carbonate, lithium dioxalate borate, lithium difluorooxalate phosphate and At least one of vinyl ethylene carbonate.
  • the other additives may be tris(trimethylsilyl) phosphite, tris(trimethylsilyl) borate, bistrifluoro Lithium methanesulfonyl imide, lithium bisfluorosulfonyl imide, 1,3-propene sultone, vinyl sulfite, vinyl sulfate, vinylene carbonate, lithium dioxalate borate, lithium di
  • the mass proportion of the other additives is 0wt.% to 10wt%, exemplarily 0wt.%, 1wt.%, 2wt.%, 5wt.%, 8wt. %, 10wt.%, or any value within the range composed of the aforementioned pairwise values.
  • the non-aqueous organic solvent also includes ethylene carbonate (EC), propylene carbonate (PC), dimethyl carbonate, diethyl carbonate, ethyl methyl carbonate, propyl propionate (PP) and at least one of propyl acetate.
  • EC ethylene carbonate
  • PC propylene carbonate
  • PP propyl propionate
  • the nonaqueous organic solvent includes ethylene carbonate (EC), propylene carbonate (PC), and propyl propionate (PP).
  • EC ethylene carbonate
  • PC propylene carbonate
  • PP propyl propionate
  • the mass ratio of the ethylene carbonate (EC), the propylene carbonate (PC) and the propyl propionate (PP) is 2:(1-2):2, for example 2:1.5 :2.
  • the non-aqueous electrolytic solution further includes lithium salt.
  • the lithium salt is selected from at least one of lithium bistrifluoromethanesulfonyl imide, lithium bisfluorosulfonyl imide and lithium hexafluorophosphate (LiPF 6 ), preferably lithium hexafluorophosphate (LiPF 6 ).
  • the mass proportion of the lithium salt is 13wt.% to 20wt.%, exemplarily 13wt.%, 14wt.%, 15wt.%, 16wt.%, 17wt. .%, 18wt.%, 19wt.%, 20wt.%, or any value within the range composed of the aforementioned pairwise values.
  • the heat-resistant layer includes ceramic and adhesive.
  • the mass proportion of the ceramic is 20wt.% to 99wt.%, for example, 20wt.%, 30wt.%, 40wt.%, 60wt.%, 80wt.%. %, 90wt.%, 95wt.%, 99wt.%, or any value within the range of the aforementioned pairwise values.
  • the mass proportion of the binder is 1-80wt.%, exemplarily 1wt.%, 5wt.%, 10wt.%, 20wt.%, 30wt.%. %, 50wt.%, 60wt.%, 80wt.%, or any value within the range of the aforementioned pairwise values.
  • the ceramic is selected from one, two or more of alumina, boehmite, magnesium oxide, boron nitride and magnesium hydroxide.
  • the binder in the heat-resistant layer is selected from polytetrafluoroethylene, polyvinylidene fluoride, hexafluoropropylene-vinylidene fluoride copolymer (for example, polyvinylidene fluoride-hexafluoropropylene copolymer ), polyimide, polyacrylonitrile and polymethyl methacrylate, two or more.
  • the glue layer has a thickness of 0.5 ⁇ m ⁇ 2 ⁇ m, exemplarily 0.5 ⁇ m, 1 ⁇ m or 2 ⁇ m.
  • the solvent used in the heat-resistant layer and the adhesive layer is selected from acetone, tetrahydrofuran, methylene chloride, chloroform, dimethylformamide, N-methyl-2-pyrrolidone, cyclohexane At least one of alkanes, methanol, ethanol, isopropanol and water.
  • the battery is, for example, a Li-ion battery.
  • the positive electrode sheet includes a positive electrode current collector and a positive electrode active material layer coated on one or both sides of the positive electrode current collector.
  • the positive active material layer includes a positive active material, a conductive agent and a binder.
  • the mass ratio of the positive electrode active material, the conductive agent and the binder is 98:1.0:1.0.
  • the positive electrode active material is selected from lithium cobaltate (LiCoO 2 ) or lithium cobaltate that has been doped and coated with two or more elements among Al, Mg, Mn, Cr, Ti, and Zr.
  • LiCoO 2 the chemical formula of lithium cobalt oxide that has been doped and coated with two or more elements in Al, Mg, Mn, Cr, Ti, Zr is Li x Co 1-y1-y2-y3-y4 A y1 B y2 C y3 D y4 O 2 ; 0.95 ⁇ x ⁇ 1.05, 0.01 ⁇ y1 ⁇ 0.1, 0.01 ⁇ y2 ⁇ 0.1, 0 ⁇ y3 ⁇ 0.1, 0 ⁇ y4 ⁇ 0.1,
  • A, B, C, D are selected from Two or more elements in Al, Mg, Mn, Cr, Ti, Zr.
  • the conductive agent in the positive electrode active material layer is selected from acetylene black.
  • the binder in the positive electrode active material layer is selected from polyvinylidene fluoride (PVDF).
  • the negative electrode sheet includes a negative electrode current collector and a negative electrode active material layer coated on one or both sides of the negative electrode current collector, the negative electrode active material layer includes the negative electrode active material, the conductive agent and the binder.
  • the negative electrode active material is selected from graphite.
  • the negative active material further optionally contains SiOx/C or Si/C, where 0 ⁇ x ⁇ 2.
  • the negative electrode active material also contains 1wt%-15wt% SiOx/C or Si/C, exemplarily 1wt.%, 2wt.%, 5wt.%, 8wt.%, 10wt.%, 12wt.%, 15wt .% or any value within the range composed of the aforementioned pairwise values. .
  • the charging cut-off voltage of the battery is 4.45V or above.
  • the present disclosure provides a battery, which is prepared through the synergistic effect of the separator and the non-aqueous electrolyte, and is used in combination with positive and negative electrode materials, while effectively improving the cycle life of the battery and reducing the cycle expansion of the battery It can also take into account the low temperature performance of the battery.
  • the battery of the present disclosure includes a positive electrode sheet, a negative electrode sheet, a separator interposed between the positive electrode sheet and the negative electrode sheet, and a non-aqueous electrolyte.
  • the ratio of the mass proportion of ethyl propionate in the non-aqueous electrolyte to the mass proportion of hexafluoropropylene (HFP) in the hexafluoropropylene-vinylidene fluoride copolymer is controlled between 0.2 and 60, wherein: propionic acid Ethyl non-aqueous organic solvent has a strong swelling effect on polyvinylidene fluoride (PVDF) in the diaphragm, and the synergistic effect of ethyl propionate non-aqueous organic solvent and hexafluoropropylene (HFP) can enhance the swelling of the diaphragm.
  • PVDF polyvinylidene fluoride
  • the present disclosure can not only improve the adhesion between the separator and the positive and negative electrodes, but also ensure the adhesion between the diaphragm coating layer and the positive and negative electrodes.
  • the change rate of the relay in the first 100 weeks of the battery cycle is within 10%, and it can also make the positive and negative electrodes of the battery have a better interface to reduce cycle expansion, thereby reducing the damage and reorganization of the CEI film, thereby improving the performance of the positive electrode material at high temperature.
  • ethyl propionate can also reduce the viscosity of the solvent to improve the wettability and ion conductivity of the electrolyte, thereby improving the low-temperature performance of the battery.
  • the synergistic effect between the additives in the electrolyte formula further ensures the long cycle life of the battery, in which 1,3-propane sultone and lithium difluorooxalate borate additives can form a strong and stable compound on the surface of the positive and negative electrodes.
  • SEI protective film to prevent the electrolyte from being decomposed by redox on the surface of the positive and negative electrodes, thereby reducing the heat release of side reactions and cycle expansion, while improving the battery cycle life.
  • the lithium-ion batteries of Comparative Examples 1-5 and Examples 1-8 were prepared according to the following preparation methods, the only difference being the choice of diaphragm and non-aqueous electrolyte, and the specific differences are shown in Table 1.
  • the positive electrode active material LiCoO 2 LiCoO 2
  • the binder polyvinylidene fluoride (PVDF) the binder polyvinylidene fluoride
  • NMP N-methylpyrrolidone
  • the positive electrode slurry is evenly coated on an aluminum foil with a thickness of 10 ⁇ m; after the above-mentioned coated aluminum foil is baked in an oven with 5 different temperature gradients, Dry in an oven at 120° C. for 8 hours, and then roll and cut to obtain the desired positive electrode sheet.
  • a 1% sodium carboxymethylcellulose (CMC) binder and a 1.1% styrene-butadiene rubber (SBR) binder are made into a slurry by a wet process and coated on the negative electrode current collector copper foil The surface was dried (temperature: 85° C., time: 5 h), rolled and die-cut to obtain the negative electrode sheet.
  • a layer of aluminum oxide ceramic layer with a thickness of 2 ⁇ m is coated on both sides of a polyethylene substrate with a thickness of 5 ⁇ m, and a glue layer with a thickness of 1 ⁇ m is coated on the surface of the ceramic coating, and the glue layer adopts
  • the adhesive is polyvinylidene fluoride (PVDF)-hexafluoropropylene (HFP) copolymer, and the mass percentage of hexafluoropropylene in polyvinylidene fluoride (PVDF)-hexafluoropropylene (HFP) copolymer is detailed in the table 1.
  • Electrochemical performance test is carried out to the battery obtained in the above-mentioned comparative examples and examples, and the relevant instructions are as follows:
  • 25°C cycle test Place the batteries obtained in the above examples and comparative examples in an environment of (25 ⁇ 2)°C, and let them stand for 2-3 hours. Charging, the cut-off current is 0.05C, and the battery is left for 5 minutes after it is fully charged, and then discharged to a cut-off voltage of 3.0V with a constant current of 1C, and the highest discharge capacity of the first three cycles is recorded as the initial capacity Q. When the number of cycles reaches 1000, record The last discharge capacity Q 1 of the battery; record the initial thickness T of the battery cell, and record the thickness after 1000 cycles as T 1 , and record the results as shown in Table 2.
  • 10°C cycle test Place the batteries obtained in the above examples and comparative examples in an environment of (10 ⁇ 2)°C, and let them stand for 2-3 hours. When the battery body reaches (10 ⁇ 2)°C, the battery will The current charging cut-off current is 0.05C. After the battery is fully charged, it is left for 5 minutes, and then discharged at a constant current of 0.5C to a cut-off voltage of 3.0V. The highest discharge capacity recorded in the first 3 cycles is the initial capacity Q 2 . When the cycle reaches 300 times, Record the last discharge capacity Q 3 of the battery; record the initial thickness T 2 of the cell, select the thickness after 300 cycles as T 3 , and record the results as shown in Table 2.
  • the separator and the negative electrode at an angle of 180 degrees are tested on a universal stretching machine at a speed of 100mm/min and a test displacement of 50mm, and the test result is recorded as the adhesion between the diaphragm and the negative electrode N (unit N/m), the adhesive force of fresh battery (not cycled after battery preparation) test is N 1 (unit N/m), the adhesive force of cycle 100 cycle battery test is N 2 (unit N/m );
  • the lithium-ion battery prepared by the present disclosure through the synergistic effect of the diaphragm and the electrolyte and the combination of positive and negative materials can effectively improve the battery cycle life and reduce battery cycle expansion. It can also take into account the low temperature performance of the battery.

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Abstract

Disclosed in the present disclosure is a battery. The battery comprises a positive electrode plate, a negative electrode plate, a separator, and a non-aqueous electrolyte; the non-aqueous electrolyte comprises a non-aqueous organic solvent and an additive; the non-aqueous organic solvent at least comprises ethyl propionate; the additive comprises 1,3-propanesultone and lithium difluoro(oxalato)borate; the separator comprises a substrate, a heat-resistant layer, and a gluing layer; the heat-resistant layer is oppositely arranged on the two surfaces of the substrate, and the gluing layer is arranged on the heat-resistant layer; and a ratio of the percentage by mass of ethyl propionate in the non-aqueous electrolyte to the percentage by mass of HFP in a hexafluoropropylene-vinylidene fluoride copolymer in an adhesive of the gluing layer is 0.2-60. According to the present invention, the battery is manufactured by means of the synergistic effect of the separator and the electrolyte after a positive electrode material and a negative electrode material are used in combination, and thus, the cycle service life of the battery can be effectively prolonged, the cycle expansion of the battery can further be effectively reduced, and the low-temperature performance of the battery is considered.

Description

一种电池a battery 技术领域technical field
本公开属于电池技术领域,具体涉及一种电池。The disclosure belongs to the technical field of batteries, and in particular relates to a battery.
背景技术Background technique
近年来,锂离子电池在智能手机、平板电脑、智能穿戴、电动工具和电动汽车等领域得到了广泛的应用。随着锂离子电池的广泛应用,消费者对锂离子电池的使用寿命、应用环境的需求不断提高,这就要求锂离子电池能够兼顾高低温性能的同时具有长循环寿命。In recent years, lithium-ion batteries have been widely used in smartphones, tablet computers, smart wearables, power tools, and electric vehicles. With the wide application of lithium-ion batteries, consumers' demands on the service life and application environment of lithium-ion batteries continue to increase, which requires lithium-ion batteries to have a long cycle life while taking into account high and low temperature performance.
目前,锂离子电池在使用过程中存在安全隐患,例如当电池使用时间较长、使用环境温度过高后,电池会出现析锂、厚度膨胀增加等问题,进而容易引发严重的安全事故,例如起火甚至爆炸。同时,电池在较低环境温度下使用时难以放电,进而出现自动关机影响使用。造成上述问题的主要原因一方面是活性材料在高温高电压下结构不稳定,金属离子极易从正极中溶出并在负极表面还原沉积,并催化电解液在负极表面被还原分解,从而破坏负极的SEI膜结构,导致负极阻抗和电池厚度不断增大,进而使电池温度持续上升引起安全事故;另一方面是低温下电池阻抗增加,SEI膜阻抗较大影响低温放电。At present, there are safety hazards in the use of lithium-ion batteries. For example, when the battery is used for a long time and the ambient temperature is too high, the battery will have problems such as lithium deposition and increased thickness expansion, which will easily lead to serious safety accidents, such as fire. Even explode. At the same time, it is difficult to discharge the battery when it is used in a lower ambient temperature, and then the automatic shutdown will affect the use. The main reason for the above problems is that the structure of the active material is unstable under high temperature and high voltage. Metal ions are easily dissolved from the positive electrode and deposited on the surface of the negative electrode. The SEI film structure leads to the continuous increase of the negative electrode impedance and battery thickness, which in turn causes the battery temperature to continue to rise and cause safety accidents; on the other hand, the battery impedance increases at low temperatures, and the high SEI film impedance affects low-temperature discharge.
基于此现状,急需开发具有长循环寿命低膨胀的高电压锂离子电池,例如通过向电解液中添加负极成膜剂能够改善循环性能,但负极成膜剂的使用往往会导致电池低温性能严重劣化。因此能够开发在不影响电池低温性能的前提下,同时具有长循环寿命低膨胀的高电压锂离子电池是目前的首要任务。Based on this situation, there is an urgent need to develop high-voltage lithium-ion batteries with long cycle life and low expansion. For example, the cycle performance can be improved by adding negative electrode film-forming agents to the electrolyte, but the use of negative electrode film-forming agents often leads to serious deterioration of battery low-temperature performance. . Therefore, the ability to develop high-voltage lithium-ion batteries with long cycle life and low expansion without affecting the low-temperature performance of the battery is the current priority.
发明内容Contents of the invention
本公开的目的是为了解决现有的电池在使用过程中存在安全隐患、电池循环寿命与低温性能未能兼顾等问题,提供一种电池,其兼具高电压、长循环寿命和低膨胀的性能。The purpose of this disclosure is to solve the problems of potential safety hazards in the use process of existing batteries, failure to balance battery cycle life and low temperature performance, and provide a battery with high voltage, long cycle life and low expansion performance .
为实现上述目的,本公开采用如下的技术方案:In order to achieve the above purpose, the present disclosure adopts the following technical solutions:
一种电池,其包括正极片、负极片、置于所述正极片和所述负极片之间的隔膜,以及非水电解液;A battery comprising a positive electrode sheet, a negative electrode sheet, a separator placed between the positive electrode sheet and the negative electrode sheet, and a non-aqueous electrolyte;
所述非水电解液包括非水有机溶剂和添加剂,其中所述非水有机溶剂至少包括丙酸乙酯;所述添加剂包括1,3-丙烷磺酸内酯和二氟草酸硼酸锂;The non-aqueous electrolytic solution includes a non-aqueous organic solvent and an additive, wherein the non-aqueous organic solvent includes at least ethyl propionate; the additive includes 1,3-propane sultone and lithium difluorooxalate borate;
所述隔膜包括基材、耐热层和涂胶层,所述耐热层相对设置于所述基材的两面,所述涂胶层设置于所述耐热层上;所述涂胶层包括粘接剂,所述粘接剂中包括六氟丙烯-偏氟乙烯共聚物;The diaphragm includes a base material, a heat-resistant layer and a glue layer, the heat-resistant layer is relatively arranged on both sides of the base material, and the glue layer is arranged on the heat-resistant layer; the glue layer includes Adhesive, including hexafluoropropylene-vinylidene fluoride copolymer in the adhesive;
所述非水电解液中丙酸乙酯的质量占比与六氟丙烯-偏氟乙烯共聚物中六氟丙烯(HFP)的质量占比的比值为0.2~60,示例性为0.26、0.5、1、2.4、5.8、9.2、11.3、13.7、15、20、30、35、36.7、40、50、60或者是上述点值两两数值组成的范围内的任一点值。。The ratio of the mass proportion of ethyl propionate in the non-aqueous electrolyte to the mass proportion of hexafluoropropylene (HFP) in the hexafluoropropylene-vinylidene fluoride copolymer is 0.2 to 60, exemplarily 0.26, 0.5, 1, 2.4, 5.8, 9.2, 11.3, 13.7, 15, 20, 30, 35, 36.7, 40, 50, 60 or any point value within the range composed of two pairs of the above point values. .
根据本发明,所述隔膜的涂胶层与正负极之间的粘接力在电池循环前100周(包括第100周)的变化率在10%以内,即,当电池循环≤100周(例如,电池循环1周、5周、10周、50周或100周)时,所述涂胶层与所述正极片或所述负极片之间的粘接力的变化率在10%以内。According to the present invention, the change rate of the adhesive force between the adhesive layer of the separator and the positive and negative electrodes is within 10% in the first 100 cycles (including the 100th cycle) of the battery cycle, that is, when the battery cycle is ≤ 100 cycles ( For example, when the battery is cycled for 1 week, 5 weeks, 10 weeks, 50 weeks or 100 cycles), the change rate of the adhesive force between the adhesive layer and the positive electrode sheet or the negative electrode sheet is within 10%.
在一实施例中,所述非水电解液中丙酸乙酯的质量占比与六氟丙烯-偏氟乙烯共聚物中六氟丙烯的质量占比的比值为0.5~35。In one embodiment, the ratio of the mass proportion of ethyl propionate in the non-aqueous electrolyte to the mass proportion of hexafluoropropylene in the hexafluoropropylene-vinylidene fluoride copolymer is 0.5-35.
在一实施例中,所述六氟丙烯-偏氟乙烯共聚物中六氟丙烯的质量占比为1wt.%~25wt.%,优选为1.5wt.%~15wt.%,示例性为1wt.%、1.5wt.%、2wt.%、2.5wt.%、3wt.%、3.5wt.%、5wt.%、6.5wt.%、9wt.%、10wt.%、15wt.%、20wt.%、23wt.%、25wt.%或者是前述两两数值组成的范围内的任一点值。In one embodiment, the mass proportion of hexafluoropropylene in the hexafluoropropylene-vinylidene fluoride copolymer is 1wt.% to 25wt.%, preferably 1.5wt.% to 15wt.%, exemplarily 1wt. %, 1.5wt.%, 2wt.%, 2.5wt.%, 3wt.%, 3.5wt.%, 5wt.%, 6.5wt.%, 9wt.%, 10wt.%, 15wt.%, 20wt.%, 23wt.%, 25wt.%, or any value within the range composed of the aforementioned pairwise values.
在一实施例中,所述六氟丙烯-偏氟乙烯共聚物例如为聚偏氟乙烯-六氟丙烯共聚物。In one embodiment, the hexafluoropropylene-vinylidene fluoride copolymer is, for example, polyvinylidene fluoride-hexafluoropropylene copolymer.
所述“聚偏氟乙烯-六氟丙烯共聚物”是指六氟丙烯改性的聚偏氟乙烯。The "polyvinylidene fluoride-hexafluoropropylene copolymer" refers to polyvinylidene fluoride modified by hexafluoropropylene.
在一实施例中,所述聚偏氟乙烯(PVDF)的数均分子量为50万Da~200万Da,示例性为50万Da、60万Da、70万Da、80万Da、100万Da、200万Da或者是上述点值两两数值组成的范围内的任一点值。In one embodiment, the number average molecular weight of the polyvinylidene fluoride (PVDF) is 500,000 Da to 2 million Da, exemplarily 500,000 Da, 600,000 Da, 700,000 Da, 800,000 Da, and 1 million Da , 2,000,000 Da or any point value within the range composed of two pairs of the above point values.
在一实例中,在所述六氟丙烯-偏氟乙烯共聚物中,偏氟乙烯单元的分子量之和为50万Da~200万Da,示例性为50万Da、60万Da、70万Da、80万Da、100万Da、200万Da或者是上述点值两两数值组成的范围内的任一点值。In one example, in the hexafluoropropylene-vinylidene fluoride copolymer, the sum of the molecular weights of vinylidene fluoride units is 500,000 Da to 2 million Da, exemplarily 500,000 Da, 600,000 Da, and 700,000 Da .
在一实施例中,所述非水有机溶剂中,丙酸乙酯的质量为非水电解液总质量的5wt.%~60wt.%,(即所述非水电解液中丙酸乙酯的质量占比)为5wt.%~60wt.%;优选为10wt.%~40wt.%,示例性为5wt.%、6wt.%、10wt.%、12wt.%、15wt.%、20wt.%、22wt.%、23wt.%、25wt.%、30wt.%、34wt.%、35wt.%、38wt.%、40wt.%、48wt.%、50wt.%、55wt.%、60wt.%或者是前述两两数值组成的范围内的任一点值。In one embodiment, in the nonaqueous organic solvent, the quality of ethyl propionate is 5wt.%~60wt.% of the total mass of the nonaqueous electrolytic solution, (that is, the amount of ethyl propionate in the nonaqueous electrolytic solution % by mass) is 5wt.%~60wt.%; preferably 10wt.%~40wt.%, exemplarily 5wt.%, 6wt.%, 10wt.%, 12wt.%, 15wt.%, 20wt.%, 22wt.%, 23wt.%, 25wt.%, 30wt.%, 34wt.%, 35wt.%, 38wt.%, 40wt.%, 48wt.%, 50wt.%, 55wt.%, 60wt.% or the above Any point value within a range consisting of two pairs of values.
在一实施例中,采用的所述添加剂均可以采用本领域已知的方法制备得到,也可以采用商业途径购买后获得。In one embodiment, the additives used can be prepared by methods known in the art, or purchased from commercial channels.
在一实施例中,所述非水电解液中,所述1,3-丙烷磺酸内酯的质量占比为0.5wt.%~5wt.%;优选为2~4wt.%,示例性为1wt.%、2wt.%、3wt.%、3.5wt.%、4wt.%、4.5wt.%、5wt.%或者是前述两两数值组成的范围内的任一点值。In one embodiment, in the non-aqueous electrolyte, the mass proportion of the 1,3-propane sultone is 0.5wt.%~5wt.%, preferably 2~4wt.%, exemplarily 1wt.%, 2wt.%, 3wt.%, 3.5wt.%, 4wt.%, 4.5wt.%, 5wt.%, or any value within the range composed of the aforementioned pairwise values.
在一实施例中,所述非水电解液中,所述二氟草酸硼酸锂的质量占比为0.01wt.%~2wt.%,示例性为0.01wt.%、0.02wt.%、0.05wt.%、0.1wt.%、0.2wt.%、0.5wt.%、1wt.%、2wt.%或者是前述两两数值组成的范围内的任一点值。In one embodiment, in the non-aqueous electrolyte, the mass proportion of lithium difluorooxalate borate is 0.01wt.%~2wt.%, exemplarily 0.01wt.%, 0.02wt.%, 0.05wt. .%, 0.1wt.%, 0.2wt.%, 0.5wt.%, 1wt.%, 2wt.%, or any value within the range composed of the aforementioned pairwise values.
在一实施例中,所述添加剂还可以包括其他添加剂,例如,所述其他添加剂可以为三(三甲基硅烷)亚磷酸酯、三(三甲基甲硅烷基)硼酸酯、双三氟甲烷磺酰亚胺锂、双氟磺酰亚胺锂、1,3-丙烯磺酸内酯、亚硫酸乙烯酯、硫酸乙烯酯、碳酸亚乙烯酯、二草酸硼酸锂、二氟草酸磷酸锂和乙烯基碳酸乙烯酯中的至少一种。In one embodiment, the additives may also include other additives, for example, the other additives may be tris(trimethylsilyl) phosphite, tris(trimethylsilyl) borate, bistrifluoro Lithium methanesulfonyl imide, lithium bisfluorosulfonyl imide, 1,3-propene sultone, vinyl sulfite, vinyl sulfate, vinylene carbonate, lithium dioxalate borate, lithium difluorooxalate phosphate and At least one of vinyl ethylene carbonate.
在一实施例中,在非水电解液中,所述其他添加剂的质量占比为0wt.%~10wt%,示例性为0wt.%、1wt.%、2wt.%、5wt.%、8wt.%、10wt.%或者是前述两两数值组成的范围内的任一点值。In one embodiment, in the non-aqueous electrolyte, the mass proportion of the other additives is 0wt.% to 10wt%, exemplarily 0wt.%, 1wt.%, 2wt.%, 5wt.%, 8wt. %, 10wt.%, or any value within the range composed of the aforementioned pairwise values.
在一实施例中,所述非水有机溶剂还包括碳酸乙烯酯(EC)、碳酸丙烯酯(PC)、碳酸二甲酯、碳酸二乙酯、碳酸甲乙酯、丙酸丙酯(PP)和乙酸丙酯中的至少一种。In one embodiment, the non-aqueous organic solvent also includes ethylene carbonate (EC), propylene carbonate (PC), dimethyl carbonate, diethyl carbonate, ethyl methyl carbonate, propyl propionate (PP) and at least one of propyl acetate.
根据本公开一个示例性的实施方案,所述非水有机溶剂包括碳酸乙烯酯(EC)、碳酸丙烯酯(PC)和丙酸丙酯(PP)。示例性地,所述碳酸乙烯酯(EC)、所述碳酸丙烯酯(PC)和所述丙酸丙酯(PP)的质量比为2:(1~2):2,例如为2:1.5:2。According to an exemplary embodiment of the present disclosure, the nonaqueous organic solvent includes ethylene carbonate (EC), propylene carbonate (PC), and propyl propionate (PP). Exemplarily, the mass ratio of the ethylene carbonate (EC), the propylene carbonate (PC) and the propyl propionate (PP) is 2:(1-2):2, for example 2:1.5 :2.
在一实施例中,所述非水电解液中还包括锂盐。In one embodiment, the non-aqueous electrolytic solution further includes lithium salt.
在一实施例中,所述锂盐选自双三氟甲基磺酰亚胺锂、双氟磺酰亚胺锂和六氟磷酸锂(LiPF 6)中的至少一种,优选为六氟磷酸锂(LiPF 6)。 In one embodiment, the lithium salt is selected from at least one of lithium bistrifluoromethanesulfonyl imide, lithium bisfluorosulfonyl imide and lithium hexafluorophosphate (LiPF 6 ), preferably lithium hexafluorophosphate (LiPF 6 ).
在一实施例中,在所述非水电解液,所述锂盐质量占比为13wt.%~20wt.%,示例性为13wt.%、14wt.%、15wt.%、16wt.%、17wt.%、18wt.%、19wt.%、20wt.%或者是前述两两数值组成的范围内的任一点值。In one embodiment, in the non-aqueous electrolyte, the mass proportion of the lithium salt is 13wt.% to 20wt.%, exemplarily 13wt.%, 14wt.%, 15wt.%, 16wt.%, 17wt. .%, 18wt.%, 19wt.%, 20wt.%, or any value within the range composed of the aforementioned pairwise values.
在一实施例中,所述耐热层包括陶瓷和粘结剂。In one embodiment, the heat-resistant layer includes ceramic and adhesive.
在一实施例中,所述耐热层中,所述陶瓷的质量占比为20wt.%~99wt.%,示例性为20wt.%、30wt.%、40wt.%、60wt.%、80wt.%、90wt.%、95wt.%、99wt.%或者是前述两两数值组成的范围内的任一点值。In one embodiment, in the heat-resistant layer, the mass proportion of the ceramic is 20wt.% to 99wt.%, for example, 20wt.%, 30wt.%, 40wt.%, 60wt.%, 80wt.%. %, 90wt.%, 95wt.%, 99wt.%, or any value within the range of the aforementioned pairwise values.
在一实施例中,所述耐热层中,所述粘结剂的质量占比为1~80wt.%,示例性为1wt.%、5wt.%、10wt.%、20wt.%、30wt.%、50wt.%、60wt.%、80wt.%或者是前述两两数值组成的范围内的任一点值。In one embodiment, in the heat-resistant layer, the mass proportion of the binder is 1-80wt.%, exemplarily 1wt.%, 5wt.%, 10wt.%, 20wt.%, 30wt.%. %, 50wt.%, 60wt.%, 80wt.%, or any value within the range of the aforementioned pairwise values.
在一实施例中,所述陶瓷选自氧化铝、勃姆石、氧化镁、氮化硼和氢氧化镁中的一种、两种或更多种。In one embodiment, the ceramic is selected from one, two or more of alumina, boehmite, magnesium oxide, boron nitride and magnesium hydroxide.
在一实施例中,所述耐热层中的粘结剂选自聚四氟乙烯、聚偏氟乙烯、六氟丙烯-偏氟乙烯共聚物(例如为聚偏氟乙烯-六氟丙烯共聚物)、聚酰亚胺、聚丙烯腈和聚甲基丙烯酸甲酯中的一种、两种或更多种。In one embodiment, the binder in the heat-resistant layer is selected from polytetrafluoroethylene, polyvinylidene fluoride, hexafluoropropylene-vinylidene fluoride copolymer (for example, polyvinylidene fluoride-hexafluoropropylene copolymer ), polyimide, polyacrylonitrile and polymethyl methacrylate, two or more.
在一实施例中,所述涂胶层的厚度为0.5μm~2μm,示例性为0.5μm、1μm或2μm。In one embodiment, the glue layer has a thickness of 0.5 μm˜2 μm, exemplarily 0.5 μm, 1 μm or 2 μm.
在一实施例中,所述耐热层和所述涂胶层所采用的溶剂选自丙酮、四氢呋喃、二氯甲烷、氯仿、二甲基甲酰胺、N-甲基-2-吡咯烷酮、环己烷、甲醇、乙醇、异丙醇和水中的至少一种。In one embodiment, the solvent used in the heat-resistant layer and the adhesive layer is selected from acetone, tetrahydrofuran, methylene chloride, chloroform, dimethylformamide, N-methyl-2-pyrrolidone, cyclohexane At least one of alkanes, methanol, ethanol, isopropanol and water.
在一实施例中,所述电池例如为锂离子电池。In one embodiment, the battery is, for example, a Li-ion battery.
在一实施例中,所述正极片包括正极集流体和涂覆在正极集流体一侧或两侧表面的正极活性物质层。In one embodiment, the positive electrode sheet includes a positive electrode current collector and a positive electrode active material layer coated on one or both sides of the positive electrode current collector.
在一实施例中,所述正极活性物质层包括正极活性物质、导电剂和粘结剂。In one embodiment, the positive active material layer includes a positive active material, a conductive agent and a binder.
根据本公开一个示例性的实施方案,所述正极活性物质、所述导电剂和所述粘结剂的质量比为98:1.0:1.0。According to an exemplary embodiment of the present disclosure, the mass ratio of the positive electrode active material, the conductive agent and the binder is 98:1.0:1.0.
在一实施例中,所述的正极活性物质选自钴酸锂(LiCoO 2)或经过Al、Mg、Mn、Cr、Ti、Zr中两种或多种元素掺杂包覆处理的钴酸锂(LiCoO 2),所述经过Al、Mg、Mn、Cr、Ti、Zr中两种或多种元素掺杂包覆处理的钴酸锂的化学式为Li xCo 1-y1-y2-y3-y4A y1B y2C y3D y4O 2;0.95≤x≤1.05,0.01≤y1≤0.1,0.01≤y2≤0.1,0≤y3≤0.1,0≤y4≤0.1,A、B、C、D选自Al、Mg、Mn、Cr、Ti、Zr中两种或多种元素。 In one embodiment, the positive electrode active material is selected from lithium cobaltate (LiCoO 2 ) or lithium cobaltate that has been doped and coated with two or more elements among Al, Mg, Mn, Cr, Ti, and Zr. (LiCoO 2 ), the chemical formula of lithium cobalt oxide that has been doped and coated with two or more elements in Al, Mg, Mn, Cr, Ti, Zr is Li x Co 1-y1-y2-y3-y4 A y1 B y2 C y3 D y4 O 2 ; 0.95≤x≤1.05, 0.01≤y1≤0.1, 0.01≤y2≤0.1, 0≤y3≤0.1, 0≤y4≤0.1, A, B, C, D are selected from Two or more elements in Al, Mg, Mn, Cr, Ti, Zr.
在一实施例中,所述正极活性物质层中的所述导电剂选自乙炔黑。In one embodiment, the conductive agent in the positive electrode active material layer is selected from acetylene black.
在一实施例中,所述正极活性物质层中的所述粘结剂选自聚偏氟乙烯(PVDF)。In one embodiment, the binder in the positive electrode active material layer is selected from polyvinylidene fluoride (PVDF).
在一实施例中,所述负极片包括负极集流体和涂覆在负极集流体一侧或两侧表面的负极活性物质层,所述负极活性物质层包括所述负极活性物质、所述导电剂和所述粘结剂。In one embodiment, the negative electrode sheet includes a negative electrode current collector and a negative electrode active material layer coated on one or both sides of the negative electrode current collector, the negative electrode active material layer includes the negative electrode active material, the conductive agent and the binder.
在一实施例中,所述负极活性物质选自石墨。In one embodiment, the negative electrode active material is selected from graphite.
在一实施例中,所述负极活性物质还任选地含有SiOx/C或Si/C,其中0<x<2。例如,所述负极活性物质还含有1wt%~15wt%SiOx/C或 Si/C,示例性为1wt.%、2wt.%、5wt.%、8wt.%、10wt.%、12wt.%、15wt.%或者是前述两两数值组成的范围内的任一点值。。In one embodiment, the negative active material further optionally contains SiOx/C or Si/C, where 0<x<2. For example, the negative electrode active material also contains 1wt%-15wt% SiOx/C or Si/C, exemplarily 1wt.%, 2wt.%, 5wt.%, 8wt.%, 10wt.%, 12wt.%, 15wt .% or any value within the range composed of the aforementioned pairwise values. .
在一实施例中,所述电池的充电截止电压在4.45V及以上。In one embodiment, the charging cut-off voltage of the battery is 4.45V or above.
本公开的有益效果:Beneficial effects of the present disclosure:
(1)本公开提供一种电池,通过隔膜与非水电解液的协同作用,并在正负极材料组合下联用后制备得到的电池,在有效提高电池循环寿命、降低电池循环膨胀的同时还能兼顾电池的低温性能。(1) The present disclosure provides a battery, which is prepared through the synergistic effect of the separator and the non-aqueous electrolyte, and is used in combination with positive and negative electrode materials, while effectively improving the cycle life of the battery and reducing the cycle expansion of the battery It can also take into account the low temperature performance of the battery.
(2)本公开的电池包括正极片、负极片、置于正极片和负极片之间的隔膜以及非水电解液。将非水电解液中丙酸乙酯的质量占比与六氟丙烯-偏氟乙烯共聚物中六氟丙烯(HFP)的质量占比的比值控制在0.2~60范围之间,其中:丙酸乙酯非水有机溶剂对于隔膜中聚偏氟乙烯(PVDF)具有较强的溶胀效果,通过丙酸乙酯非水有机溶剂与六氟丙烯(HFP)的协同作用可对隔膜溶胀起到加强的效果。基于此,本公开通过控制丙酸乙酯和六氟丙烯(HFP)的含量比,不仅可以提升隔膜与正负极片的粘结力,保证了隔膜涂胶层与正负极之间的粘接力在电池循环前100周的变化率在10%以内,还能使电池得正负极拥有更好的界面,以降低循环膨胀,进而减少CEI膜的破坏和重组,从而提高正极材料在高温高电压下的稳定性;同时丙酸乙酯还可以降低溶剂粘度,以提高电解液浸润性以及离子电导率,进而提高电池的低温性能。另外,电解液配方中添加剂之间的协同作用还进一步保障了电池得长循环寿命,其中1,3-丙烷磺酸内酯和二氟草酸硼酸锂添加剂能够在正负极表面形成坚固稳定的复合SEI保护膜,以阻止电解液在正负极表面被氧化还原分解,从而降低副反应放热并降低循环膨胀,同时提升电池循环寿命。(2) The battery of the present disclosure includes a positive electrode sheet, a negative electrode sheet, a separator interposed between the positive electrode sheet and the negative electrode sheet, and a non-aqueous electrolyte. The ratio of the mass proportion of ethyl propionate in the non-aqueous electrolyte to the mass proportion of hexafluoropropylene (HFP) in the hexafluoropropylene-vinylidene fluoride copolymer is controlled between 0.2 and 60, wherein: propionic acid Ethyl non-aqueous organic solvent has a strong swelling effect on polyvinylidene fluoride (PVDF) in the diaphragm, and the synergistic effect of ethyl propionate non-aqueous organic solvent and hexafluoropropylene (HFP) can enhance the swelling of the diaphragm. Effect. Based on this, by controlling the content ratio of ethyl propionate and hexafluoropropylene (HFP), the present disclosure can not only improve the adhesion between the separator and the positive and negative electrodes, but also ensure the adhesion between the diaphragm coating layer and the positive and negative electrodes. The change rate of the relay in the first 100 weeks of the battery cycle is within 10%, and it can also make the positive and negative electrodes of the battery have a better interface to reduce cycle expansion, thereby reducing the damage and reorganization of the CEI film, thereby improving the performance of the positive electrode material at high temperature. Stability under high voltage; at the same time, ethyl propionate can also reduce the viscosity of the solvent to improve the wettability and ion conductivity of the electrolyte, thereby improving the low-temperature performance of the battery. In addition, the synergistic effect between the additives in the electrolyte formula further ensures the long cycle life of the battery, in which 1,3-propane sultone and lithium difluorooxalate borate additives can form a strong and stable compound on the surface of the positive and negative electrodes. SEI protective film to prevent the electrolyte from being decomposed by redox on the surface of the positive and negative electrodes, thereby reducing the heat release of side reactions and cycle expansion, while improving the battery cycle life.
具体实施方式Detailed ways
下文将结合具体实施例对本公开做更进一步的详细说明。应当理解,下列实施例仅为示例性地说明和解释本公开,而不应被解释为对本公开保护范围的限制。凡基于本公开上述内容所实现的技术均涵盖在本公开旨在保护的范围内。The present disclosure will be further described in detail in conjunction with specific embodiments below. It should be understood that the following examples are only for illustrating and explaining the present disclosure, and should not be construed as limiting the protection scope of the present disclosure. All technologies implemented based on the above contents of the present disclosure are covered within the intended protection scope of the present disclosure.
下述实施例中所使用的实验方法如无特殊说明,均为常规方法;下述实施例中所用的试剂、材料等,如无特殊说明,均可从商业途径得到。The experimental methods used in the following examples are conventional methods unless otherwise specified; the reagents and materials used in the following examples can be obtained from commercial sources unless otherwise specified.
对比例1-5和实施例1-8Comparative Examples 1-5 and Examples 1-8
对比例1-5和实施例1-8的锂离子电池均按照下述制备方法进行制备,区别仅在于隔膜和非水电解液的选择不同,具体区别如表1所示。The lithium-ion batteries of Comparative Examples 1-5 and Examples 1-8 were prepared according to the following preparation methods, the only difference being the choice of diaphragm and non-aqueous electrolyte, and the specific differences are shown in Table 1.
(1)正极片制备(1) Preparation of positive electrode sheet
将正极活性物质LiCoO 2、粘结剂聚偏氟乙烯(PVDF)、导电剂乙炔黑按照重量比98:1.0:1.0进行混合,加入N-甲基吡咯烷酮(NMP),在真空搅拌机作用下搅拌,直至混合体系成均一流动性的正极浆料;将正极浆料均匀涂覆于厚度为10μm的铝箔上;将上述涂覆好的铝箔在5段不同温度梯度的烘箱烘烤后,再将其在120℃的烘箱干燥8h,然后经过辊压、分切得到所需的正极片。 Mix the positive electrode active material LiCoO 2 , the binder polyvinylidene fluoride (PVDF), and the conductive agent acetylene black at a weight ratio of 98:1.0:1.0, add N-methylpyrrolidone (NMP), and stir under the action of a vacuum mixer. Until the mixed system becomes a positive electrode slurry with uniform fluidity; the positive electrode slurry is evenly coated on an aluminum foil with a thickness of 10 μm; after the above-mentioned coated aluminum foil is baked in an oven with 5 different temperature gradients, Dry in an oven at 120° C. for 8 hours, and then roll and cut to obtain the desired positive electrode sheet.
(2)负极片制备(2) Negative sheet preparation
将质量占比为97%的人造石墨负极材料,质量占比为0.1%的单壁碳纳米管(SWCNT)导电剂、质量占比为0.8%的导电炭黑(SP)导电剂、质量占比为1%的羧甲基纤维素钠(CMC)粘结剂及质量占比为1.1%的丁苯橡胶(SBR)粘结剂以湿法工艺制成浆料,涂覆于负极集流体铜箔的表面,经烘干(温度:85℃,时间:5h)、辊压和模切得到负极片。The artificial graphite negative electrode material with a mass proportion of 97%, the single-walled carbon nanotube (SWCNT) conductive agent with a mass proportion of 0.1%, the conductive carbon black (SP) conductive agent with a mass proportion of 0.8%, and the mass proportion A 1% sodium carboxymethylcellulose (CMC) binder and a 1.1% styrene-butadiene rubber (SBR) binder are made into a slurry by a wet process and coated on the negative electrode current collector copper foil The surface was dried (temperature: 85° C., time: 5 h), rolled and die-cut to obtain the negative electrode sheet.
(3)非水电解液制备(3) Preparation of non-aqueous electrolyte
在充满氩气的手套箱(水分<10ppm,氧分<1ppm)中,将碳酸乙烯酯(EC)、碳酸丙烯酯(PC)、丙酸丙酯(PP)以2:1.5:2质量比混合均匀,在混合溶液中缓慢加入基于非水电解液总质量14wt.%的LiPF 6、基于非水电解液总质量5~60wt.%的丙酸乙酯(丙酸乙酯的具体用量如表1所示)和添加剂(添加剂的具体用量和选择如表1所示),搅拌均匀得到非水电解液。 In an argon-filled glove box (moisture <10ppm, oxygen <1ppm), mix ethylene carbonate (EC), propylene carbonate (PC), and propyl propionate (PP) in a mass ratio of 2:1.5:2 Uniformly, slowly add 14wt.% LiPF 6 based on the total mass of the non-aqueous electrolytic solution, and 5-60 wt.% ethyl propionate based on the total mass of the non-aqueous electrolytic solution (the specific amount of ethyl propionate is shown in Table 1 shown) and additives (the specific dosage and selection of additives are shown in Table 1), and stirred evenly to obtain non-aqueous electrolyte.
(4)隔膜的制备(4) Preparation of diaphragm
在厚度为5μm的聚乙烯基材的双面各涂覆一层厚度为2μm的氧化铝陶瓷层,在陶瓷涂层表面涂覆一层厚度为1μm的涂胶层,所述涂胶层采用的粘接剂为聚偏氟乙烯(PVDF)-六氟丙烯(HFP)共聚物,聚偏氟 乙烯(PVDF)-六氟丙烯(HFP)共聚物中六氟丙烯的质量百分含量具体详见表1。A layer of aluminum oxide ceramic layer with a thickness of 2 μm is coated on both sides of a polyethylene substrate with a thickness of 5 μm, and a glue layer with a thickness of 1 μm is coated on the surface of the ceramic coating, and the glue layer adopts The adhesive is polyvinylidene fluoride (PVDF)-hexafluoropropylene (HFP) copolymer, and the mass percentage of hexafluoropropylene in polyvinylidene fluoride (PVDF)-hexafluoropropylene (HFP) copolymer is detailed in the table 1.
(5)锂离子电池的制备(5) Preparation of lithium ion battery
将上述准备的正极片、隔膜、负极片通过卷绕得到未注液的裸电池;将裸电池置于外包装箔中,将上述制备好的电解液注入到干燥后的裸电池中,经过真空封装、静置、化成、整形、分选等工序,获得所需的锂离子电池。Wind the above-prepared positive electrode sheet, separator, and negative electrode sheet to obtain a bare cell without liquid injection; place the bare cell in the outer packaging foil, inject the above-mentioned prepared electrolyte into the dried bare cell, and vacuum Encapsulation, standing, formation, shaping, sorting and other processes to obtain the required lithium-ion batteries.
表1 对比例1-5和实施例1-8制备得到的锂离子电池Table 1 Lithium-ion batteries prepared in Comparative Examples 1-5 and Examples 1-8
Figure PCTCN2022127500-appb-000001
Figure PCTCN2022127500-appb-000001
对上述对比例和实施例所得电池进行电化学性能测试,相关说明如下:Electrochemical performance test is carried out to the battery obtained in the above-mentioned comparative examples and examples, and the relevant instructions are as follows:
25℃循环实验:将上述实施例和对比例所得电池置于(25±2)℃环境中,静置2-3个小时,待电池本体达到(25±2)℃时,电池按照1C恒流充电,截止电流为0.05C,电池充满电后搁置5min,再以1C恒流放电至截止电压3.0V,记录前3次循环的最高放电容量为初始容量Q,当循环次数达到1000次时,记录电池最后一次的放电容量Q 1;记录电芯初始厚度T,当循环至1000次的厚度记为T 1,记录结果如表2。 25°C cycle test: Place the batteries obtained in the above examples and comparative examples in an environment of (25±2)°C, and let them stand for 2-3 hours. Charging, the cut-off current is 0.05C, and the battery is left for 5 minutes after it is fully charged, and then discharged to a cut-off voltage of 3.0V with a constant current of 1C, and the highest discharge capacity of the first three cycles is recorded as the initial capacity Q. When the number of cycles reaches 1000, record The last discharge capacity Q 1 of the battery; record the initial thickness T of the battery cell, and record the thickness after 1000 cycles as T 1 , and record the results as shown in Table 2.
其中用到的计算公式如下:容量保持率(%)=Q1/Q×100%;厚度变化率(%)=(T 1-T)/T×100%。 The calculation formula used therein is as follows: capacity retention rate (%)=Q1/Q×100%; thickness change rate (%)=(T 1 −T)/T×100%.
10℃循环实验:将上述实施例和对比例所得电池置于(10±2)℃环境中,静置2-3个小时,待电池本体达到(10±2)℃时,电池按照0.7C恒流充电截止电流为0.05C,电池充满电后搁置5min,再以0.5C恒流放电至截止电压3.0V,记录前3次循环的最高放电容量为初始容量Q 2,当循环达到300次数时,记录电池的最后一次的放电容量Q 3;记录电芯初始厚度T 2,选循环至300周的厚度记为T 3,记录结果如表2。 10°C cycle test: Place the batteries obtained in the above examples and comparative examples in an environment of (10±2)°C, and let them stand for 2-3 hours. When the battery body reaches (10±2)°C, the battery will The current charging cut-off current is 0.05C. After the battery is fully charged, it is left for 5 minutes, and then discharged at a constant current of 0.5C to a cut-off voltage of 3.0V. The highest discharge capacity recorded in the first 3 cycles is the initial capacity Q 2 . When the cycle reaches 300 times, Record the last discharge capacity Q 3 of the battery; record the initial thickness T 2 of the cell, select the thickness after 300 cycles as T 3 , and record the results as shown in Table 2.
其中用到的计算公式如下:容量保持率(%)=Q 3/Q 2×100%;厚度变化率(%)=(T 3-T 2)/T 2×100%。 The calculation formula used therein is as follows: capacity retention rate (%)=Q 3 /Q 2 ×100%; thickness change rate (%)=(T 3 −T 2 )/T 2 ×100%.
低温放电实验:将上述实施例和对比例所得电池在环境温度25±3℃,先以0.2C放电至3.0V,搁置5min;以0.7C充电,当电池端电压达到充电限制电压时,改为恒压充电,直到充电电流≤截止电流,停止充电,搁置5分钟后,以0.2C放电至3.0V,记录此次放电容量为常温容量Q 4。然后电池以0.7C充电,当电池端电压达到充电限制电压时,改为恒压充电,直到充电电流小于或等于截止电流,停止充电;将充满电的电池在-20±2℃条件下搁置4h后,以0.25C电流放电至截止电压3.0V,记录放电容量Q 5,计算可得低温放电容量保持率,记录结果如表2。 Low-temperature discharge experiment: Discharge the battery obtained in the above examples and comparative examples at an ambient temperature of 25±3°C to 3.0V at 0.2C, and leave it for 5 minutes; charge at 0.7C, when the battery terminal voltage reaches the charging limit voltage, change to Charge at a constant voltage until the charging current ≤ cut-off current, stop charging, and then discharge to 3.0V at 0.2C after standing aside for 5 minutes, record the discharge capacity as room temperature capacity Q 4 . Then the battery is charged at 0.7C. When the terminal voltage of the battery reaches the charging limit voltage, change to constant voltage charging until the charging current is less than or equal to the cut-off current, then stop charging; put the fully charged battery at -20±2℃ for 4 hours Afterwards, discharge at a current of 0.25C to a cut-off voltage of 3.0V, record the discharge capacity Q 5 , and calculate the low-temperature discharge capacity retention rate. The recorded results are shown in Table 2.
其中用到的计算公式如下:低温放电容量保持率(%)=Q 5/Q 4×100%。 The calculation formula used therein is as follows: low-temperature discharge capacity retention (%)=Q 5 /Q 4 ×100%.
130℃热冲击实验:将上述实施例和对比例所得电池用对流方式或循环热空气箱以起始温度(25±3)℃进行加热,温变率(5±2)℃/min,升温至(130±2)℃,保持60min后结束试验,记录电池状态结果如表2。130°C thermal shock test: The batteries obtained in the above examples and comparative examples were heated at an initial temperature of (25±3)°C in a convection mode or a circulating hot air box, with a temperature change rate of (5±2)°C/min, and the temperature was raised to (130±2)°C, keep the test for 60 minutes and end the test, record the battery status results as shown in Table 2.
隔膜涂胶层与负极之间粘接力的测量方法:The measurement method of the adhesive force between the diaphragm coating layer and the negative electrode:
将上述实施例和对比例所得电池置于(25±2)℃环境中,静置2-3个小时,待电池本体达到(25±2)℃时,将电池按照0.7C恒流充电,截止电流为0.05C,当电池端电压达到充电限制电压时,改为恒压充电,直到充电电流≤截止电流,停止充电搁置5min,将充满电的电池进行解剖,沿着极耳方向选择长30mm*15mm宽的隔膜与负极整体样品,将隔膜与负极呈180度夹角在万能拉伸机上以100mm/min的速度、测试位移为50mm进行测试,测试结果记为隔膜与负极之间的粘接力N(单位N/m),新鲜电池(电池制备后未进行循环)测试的粘接力为N 1(单位N/m),循环100周电池测试的粘接力为N 2(单位N/m); Place the batteries obtained in the above examples and comparative examples in an environment of (25±2)°C, and let them stand for 2-3 hours. When the battery body reaches (25±2)°C, charge the battery at a constant current of 0.7C, and The current is 0.05C. When the battery terminal voltage reaches the charging limit voltage, change to constant voltage charging until the charging current ≤ cut-off current, stop charging and put it aside for 5 minutes, dissect the fully charged battery, and choose a length of 30mm along the direction of the tab* 15mm wide diaphragm and negative electrode as a whole sample, the separator and the negative electrode at an angle of 180 degrees are tested on a universal stretching machine at a speed of 100mm/min and a test displacement of 50mm, and the test result is recorded as the adhesion between the diaphragm and the negative electrode N (unit N/m), the adhesive force of fresh battery (not cycled after battery preparation) test is N 1 (unit N/m), the adhesive force of cycle 100 cycle battery test is N 2 (unit N/m );
其中用到的计算公式如下:The calculation formula used in it is as follows:
隔膜涂层与负极之间粘接力的变化率(%)=(N 1-N 2)/N 1×100% Change rate of adhesion between separator coating and negative electrode (%)=(N 1 -N 2 )/N 1 ×100%
表2 对比例1-5和实施例1-8所得电池实验测试结果Table 2 Comparative Examples 1-5 and Examples 1-8 Gained Battery Experimental Test Results
Figure PCTCN2022127500-appb-000002
Figure PCTCN2022127500-appb-000002
Figure PCTCN2022127500-appb-000003
Figure PCTCN2022127500-appb-000003
由表2结果可以看出:本公开通过隔膜与电解液的协同作用,并在正负极材料组合下联用后制备得到的锂离子电池,在有效提高电池循环寿命、降低电池循环膨胀的同时还能兼顾电池的低温性能。It can be seen from the results in Table 2 that the lithium-ion battery prepared by the present disclosure through the synergistic effect of the diaphragm and the electrolyte and the combination of positive and negative materials can effectively improve the battery cycle life and reduce battery cycle expansion. It can also take into account the low temperature performance of the battery.
以上,对本公开的实施方式进行了说明。但是,本公开不限定于上述实施方式。凡在本公开的精神和原则之内,所做的任何修改、等同替换、改进等,均应包含在本公开的保护范围之内。The embodiments of the present disclosure have been described above. However, the present disclosure is not limited to the above-mentioned embodiments. Any modifications, equivalent replacements, improvements, etc. made within the spirit and principles of the present disclosure shall be included within the protection scope of the present disclosure.

Claims (15)

  1. 一种电池,其特征在于,所述电池包括正极片、负极片、置于所述正极片和所述负极片之间的隔膜,以及非水电解液;A battery, characterized in that the battery comprises a positive electrode sheet, a negative electrode sheet, a separator placed between the positive electrode sheet and the negative electrode sheet, and a non-aqueous electrolyte;
    所述非水电解液包括非水有机溶剂和添加剂,其中所述非水有机溶剂至少包括丙酸乙酯;所述添加剂包括1,3-丙烷磺酸内酯和二氟草酸硼酸锂;The non-aqueous electrolytic solution includes a non-aqueous organic solvent and an additive, wherein the non-aqueous organic solvent includes at least ethyl propionate; the additive includes 1,3-propane sultone and lithium difluorooxalate borate;
    所述隔膜包括基材、耐热层和涂胶层,所述耐热层相对设置于所述基材的两面,所述涂胶层设置于所述耐热层上;所述涂胶层包括粘接剂,所述粘接剂中包括六氟丙烯-偏氟乙烯共聚物;The diaphragm includes a base material, a heat-resistant layer and a glue layer, the heat-resistant layer is relatively arranged on both sides of the base material, and the glue layer is arranged on the heat-resistant layer; the glue layer includes Adhesive, including hexafluoropropylene-vinylidene fluoride copolymer in the adhesive;
    所述非水电解液中丙酸乙酯的质量占比与六氟丙烯-偏氟乙烯共聚物中六氟丙烯的质量占比的比值为0.2~60。The ratio of the mass proportion of ethyl propionate in the non-aqueous electrolyte to the mass proportion of hexafluoropropylene in the hexafluoropropylene-vinylidene fluoride copolymer is 0.2-60.
  2. 根据权利要求1所述的电池,其特征在于,所述非水电解液中丙酸乙酯的质量百分含量与六氟丙烯-偏氟乙烯共聚物中六氟丙烯的质量占比的比值为0.5~35。The battery according to claim 1, wherein the ratio of the mass percentage of ethyl propionate in the non-aqueous electrolyte to the mass proportion of hexafluoropropylene in the hexafluoropropylene-vinylidene fluoride copolymer is 0.5~35.
  3. 根据权利要求1或2所述的电池,其特征在于,所述六氟丙烯-偏氟乙烯共聚物的数均分子量为50万Da~200万Da;The battery according to claim 1 or 2, characterized in that the number average molecular weight of the hexafluoropropylene-vinylidene fluoride copolymer is 500,000 Da to 2 million Da;
    优选地,在所述六氟丙烯-偏氟乙烯共聚物中,偏氟乙烯单元的分子量之和为50万Da~200万Da。Preferably, in the hexafluoropropylene-vinylidene fluoride copolymer, the sum of the molecular weights of the vinylidene fluoride units is 500,000 Da to 2 million Da.
  4. 根据权利要求1-3任一项所述的电池,其特征在于,所述六氟丙烯-偏氟乙烯共聚物中六氟丙烯的质量占比为1wt.%~25wt.%。The battery according to any one of claims 1-3, characterized in that the mass proportion of hexafluoropropylene in the hexafluoropropylene-vinylidene fluoride copolymer is 1wt.%-25wt.%.
  5. 根据权利要求1-4所述的电池,其特征在于,所述非水有机溶剂中,所述非水电解液中丙酸乙酯的质量占比为5wt.%~60wt.%。The battery according to claims 1-4, characterized in that, in the non-aqueous organic solvent, the mass proportion of ethyl propionate in the non-aqueous electrolyte is 5wt.%˜60wt.%.
  6. 根据权利要求1-5任一项所述的电池,其特征在于,在所述非水电解液中,所述1,3-丙烷磺酸内酯的质量占比为0.5wt.%~5wt.%;The battery according to any one of claims 1-5, characterized in that, in the non-aqueous electrolyte, the mass proportion of the 1,3-propane sultone is 0.5wt.%~5wt. %;
    优选地,在所述非水电解液中,所述二氟草酸硼酸锂的质量占比为0.01wt.%~2wt.%。Preferably, in the non-aqueous electrolytic solution, the mass proportion of lithium difluorooxalate borate is 0.01wt.%˜2wt.%.
  7. 根据权利要求1-6任一项所述的电池,其特征在于,所述添加剂还包括其他添加剂;The battery according to any one of claims 1-6, wherein the additives also include other additives;
    优选地,所述其他添加剂为三(三甲基硅烷)亚磷酸酯、三(三甲基甲硅烷基)硼酸酯、双三氟甲烷磺酰亚胺锂、双氟磺酰亚胺锂、1,3-丙 烯磺酸内酯、亚硫酸乙烯酯、硫酸乙烯酯、碳酸亚乙烯酯、二草酸硼酸锂、二氟草酸磷酸锂和乙烯基碳酸乙烯酯中的至少一种;Preferably, the other additives are tris(trimethylsilyl) phosphite, tris(trimethylsilyl) borate, lithium bistrifluoromethanesulfonyl imide, lithium bisfluorosulfonyl imide, At least one of 1,3-propene sultone, vinyl sulfite, vinyl sulfate, vinylene carbonate, lithium dioxalate borate, lithium difluorooxalate phosphate, and vinyl vinyl carbonate;
    优选地,在所述非水电解液中,所述其他添加剂的质量占比为0wt%-10wt%。Preferably, in the non-aqueous electrolyte, the mass proportion of the other additives is 0wt%-10wt%.
  8. 根据权利要求1-7任一项所述的电池,其特征在于,所述非水有机溶剂还包括碳酸乙烯酯、碳酸丙烯酯、碳酸二甲酯、碳酸二乙酯、碳酸甲乙酯、丙酸丙酯和乙酸丙酯中的至少一种。The battery according to any one of claims 1-7, wherein the non-aqueous organic solvent also includes ethylene carbonate, propylene carbonate, dimethyl carbonate, diethyl carbonate, ethyl methyl carbonate, propylene carbonate, at least one of propyl acetate and propyl acetate.
  9. 根据权利要求1-8任一项所述的电池,其特征在于,所述非水电解液中还包括锂盐;The battery according to any one of claims 1-8, wherein the non-aqueous electrolytic solution also includes a lithium salt;
    优选地,所述锂盐选自双三氟甲基磺酰亚胺锂、双氟磺酰亚胺锂和六氟磷酸锂中的至少一种;Preferably, the lithium salt is selected from at least one of lithium bistrifluoromethanesulfonimide, lithium bisfluorosulfonimide and lithium hexafluorophosphate;
    优选地,在所述非水电解液中,所述锂盐的质量占比为13wt.%~20wt.%。Preferably, in the non-aqueous electrolytic solution, the mass proportion of the lithium salt is 13wt.%˜20wt.%.
  10. 根据权利要求1-9任一项所述的电池,其特征在于,所述耐热层包括陶瓷和粘结剂;The battery according to any one of claims 1-9, wherein the heat-resistant layer comprises ceramics and a binder;
    优选地,所述耐热层中,所述陶瓷的质量占比为20wt.%~99wt.%;Preferably, in the heat-resistant layer, the mass proportion of the ceramic is 20wt.%-99wt.%;
    优选地,所述耐热层中,所述粘结剂的质量占比为1wt.%~80wt.%;Preferably, in the heat-resistant layer, the mass proportion of the binder is 1wt.%-80wt.%;
  11. 根据权利要求10任一项所述的电池,其特征在于,所述陶瓷选自氧化铝、勃姆石、氧化镁、氮化硼和氢氧化镁中的一种、两种或更多种;The battery according to any one of claim 10, wherein the ceramic is selected from one, two or more of alumina, boehmite, magnesium oxide, boron nitride and magnesium hydroxide;
    优选地,所述耐热层中的粘结剂选自聚四氟乙烯、聚偏氟乙烯、六氟丙烯-偏氟乙烯共聚物、聚酰亚胺、聚丙烯腈和聚甲基丙烯酸甲酯中的一种、两种或更多种;Preferably, the binder in the heat-resistant layer is selected from polytetrafluoroethylene, polyvinylidene fluoride, hexafluoropropylene-vinylidene fluoride copolymer, polyimide, polyacrylonitrile and polymethylmethacrylate one, two or more of
  12. 根据权利要求1-11任一项所述的电池,其特征在于,所述涂胶层的厚度为0.5μm~2μm。The battery according to any one of claims 1-11, characterized in that, the thickness of the adhesive layer is 0.5 μm˜2 μm.
  13. 根据权利要求1-12任一项所述的电池,其特征在于,所述正极片包括正极集流体和涂覆在正极集流体一侧或两侧表面的正极活性物质层,所述正极活性物质层包括正极活性物质、导电剂和粘结剂;The battery according to any one of claims 1-12, wherein the positive electrode sheet comprises a positive electrode current collector and a positive electrode active material layer coated on one or both sides of the positive electrode current collector, and the positive electrode active material The layer includes a positive electrode active material, a conductive agent and a binder;
    优选地,所述的正极活性物质选自钴酸锂或经过Al、Mg、Mn、Cr、Ti、Zr中两种或多种元素掺杂包覆处理的钴酸锂,所述经过Al、Mg、Mn、Cr、Ti、Zr中两种或多种元素掺杂包覆处理的钴酸锂的化学式为Li xCo 1-y1-y2-y3-y4 A y1B y2C y3D y4O 2;0.95≤x≤1.05,0.01≤y1≤0.1,0.01≤y2≤0.1,0≤y3≤0.1,0≤y4≤0.1,A、B、C、D选自Al、Mg、Mn、Cr、Ti、Zr中两种或多种元素; Preferably, the positive electrode active material is selected from lithium cobaltate or lithium cobaltate that has been doped with two or more elements of Al, Mg, Mn, Cr, Ti, and Zr. , Mn, Cr, Ti, Zr with two or more elements doped and coated with lithium cobalt oxide, the chemical formula is Li x Co 1-y1-y2-y3-y4 A y1 B y2 C y3 D y4 O 2 ; 0.95≤x≤1.05, 0.01≤y1≤0.1, 0.01≤y2≤0.1, 0≤y3≤0.1, 0≤y4≤0.1, A, B, C, D are selected from Al, Mg, Mn, Cr, Ti, Zr two or more elements in
  14. 根据权利要求1-13任一项所述的电池,其特征在于,所述负极片包括负极集流体和涂覆在负极集流体一侧或两侧表面的负极活性物质层,所述负极活性物质层包括负极活性物质、导电剂和粘结剂;The battery according to any one of claims 1-13, wherein the negative electrode sheet comprises a negative electrode current collector and a negative electrode active material layer coated on one or both sides of the negative electrode current collector, the negative electrode active material The layer includes a negative electrode active material, a conductive agent and a binder;
    优选地,所述的负极活性物质选自石墨。Preferably, the negative electrode active material is selected from graphite.
  15. 根据权利要求14所述的电池,其特征在于,所述负极活性物质还任选地含有SiO x/C或Si/C,其中0<x<2; The battery according to claim 14, wherein the negative electrode active material also optionally contains SiO x /C or Si/C, wherein 0<x<2;
    优选地,所述负极活性物质还含有1wt.%~15wt.%的SiO x/C或Si/C。 Preferably, the negative electrode active material further contains 1wt.%˜15wt.% of SiO x /C or Si/C.
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