WO2024066422A1 - Bab type block copolymer, preparation method, binder, positive electrode plate, secondary battery, and electric device - Google Patents

Bab type block copolymer, preparation method, binder, positive electrode plate, secondary battery, and electric device Download PDF

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WO2024066422A1
WO2024066422A1 PCT/CN2023/096928 CN2023096928W WO2024066422A1 WO 2024066422 A1 WO2024066422 A1 WO 2024066422A1 CN 2023096928 W CN2023096928 W CN 2023096928W WO 2024066422 A1 WO2024066422 A1 WO 2024066422A1
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block
block copolymer
positive electrode
type block
bab type
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PCT/CN2023/096928
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French (fr)
Chinese (zh)
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曾子鹏
李�诚
刘会会
孙成栋
王景明
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宁德时代新能源科技股份有限公司
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Publication of WO2024066422A1 publication Critical patent/WO2024066422A1/en

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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G81/00Macromolecular compounds obtained by interreacting polymers in the absence of monomers, e.g. block polymers
    • C08G81/02Macromolecular compounds obtained by interreacting polymers in the absence of monomers, e.g. block polymers at least one of the polymers being obtained by reactions involving only carbon-to-carbon unsaturated bonds
    • C08G81/024Block or graft polymers containing sequences of polymers of C08C or C08F and of polymers of C08G
    • 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
    • H01M10/054Accumulators with insertion or intercalation of metals other than lithium, e.g. with magnesium or aluminium
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/62Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • H01M4/621Binders
    • H01M4/622Binders being polymers
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/62Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • H01M4/621Binders
    • H01M4/622Binders being polymers
    • H01M4/623Binders being polymers fluorinated polymers
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/62Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • H01M4/628Inhibitors, e.g. gassing inhibitors, corrosion inhibitors
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

Definitions

  • the present application relates to the technical field of secondary batteries, and in particular to a BAB-type block copolymer, a preparation method, a binder, a positive electrode sheet, a secondary battery, a battery module, a battery pack and an electrical device.
  • secondary batteries have been widely used in energy storage power systems such as hydropower, thermal power, wind power and solar power stations, as well as in power tools, electric bicycles, electric motorcycles, electric vehicles, military equipment, aerospace and other fields. With the popularization of secondary battery applications, higher requirements have been put forward for their energy density and cycle performance.
  • Binders are commonly used materials in secondary batteries and are widely used in battery pole pieces, separators, packaging, etc. At present, the most widely used binder in the positive electrode of secondary batteries is polyvinylidene fluoride (PVDF), but it is expensive and has poor dispersibility. In addition, existing binders cannot meet the requirements of using and storing batteries under high voltage or extremely high temperature conditions. Therefore, existing binders still need to be improved.
  • PVDF polyvinylidene fluoride
  • the present application is made in view of the above-mentioned problems, and its purpose is to provide a BAB type block copolymer, which can reduce the membrane resistance of the electrode sheet, increase the liquid absorption rate of the electrode sheet, inhibit the dissolution of transition metals in the positive electrode active material, and thus improve the cycle performance and storage performance of the battery by using the block copolymer as a binder.
  • the first aspect of the present application provides a BAB type block copolymer comprising an A-block and B-block, B-block comprises the structural unit shown in formula I, A-block comprises one or more of the structural unit shown in formula II, the structural unit shown in formula III, and the structural unit shown in formula IV,
  • R1 , R2 , R3 are each independently selected from one or more of hydrogen, fluorine, and C1-3 alkyl containing at least one fluorine atom;
  • R4 is selected from substituted C6-25 aromatic groups;
  • R5 , R6 , R7 , R8 are each independently selected from substituted or unsubstituted C2-24 alkyl groups and substituted or unsubstituted C6-25 aromatic groups.
  • the binder prepared with the BAB type block copolymer can maximize the weight average molecular weight of the fluorine-containing block and the non-fluorine block, give full play to the respective advantages of the fluorine-containing binder and the non-fluorine binder, and achieve the role of complementary advantages.
  • the BAB type block copolymer can utilize the steric hindrance between the B-block and the A-block to reduce the agglomeration of the binder and improve the uniformity of the dispersion of the material in the pole piece.
  • the binder prepared with the above-mentioned BAB type block copolymer can reduce the membrane resistance of the pole piece, increase the liquid absorption rate of the pole piece, inhibit the dissolution of the transition metal in the positive electrode active material, and thus improve the cycle performance and storage performance of the battery. And compared with the simple blending of fluorine-containing polymers and non-fluorine polymers, the BAB type block copolymer can effectively inhibit the stratification of polymers of different structural units during the slurry preparation process through the interaction between the blocks.
  • the mass percentage of each of the B-blocks is 15% to 35%, and the mass percentage of the A-block is 30% to 70%, based on the total mass of the block copolymer.
  • the BAB type block copolymer with the mass percentage of B-block and A-block in a suitable range makes the electrode have excellent adhesion, good liquid absorption rate and low membrane resistance at the same time, and the battery has excellent cycle performance, high temperature storage performance and safety performance.
  • the block copolymer has a weight average molecular weight of 400,000 to 2,000,000.
  • the BAB-type block copolymer with a weight-average molecular weight within a suitable range enables the electrode to have excellent liquid absorption rate, good adhesion and low membrane resistance, and the battery has both excellent cycle performance and storage performance.
  • the A-block comprises a structural unit of Formula II containing a trifluoromethyl group.
  • the structural unit represented by formula II containing a trifluoromethyl group comprises
  • the structural unit represented by formula II containing trifluoromethyl in the A-block enables the BAB-type block copolymer to further improve the adhesion and liquid absorption rate of the electrode, reduce the membrane resistance of the electrode, effectively inhibit the dissolution of transition metals in the positive electrode active material, and improve the cycle performance, high temperature storage performance and safety performance of the battery.
  • the A-block comprises a structural unit of Formula II comprising a sulfone group.
  • the structural unit represented by formula II containing a sulfone group comprises
  • the structural unit shown in formula II containing a sulfone group in the A-block enables the BAB-type block copolymer to further improve the adhesion and liquid absorption rate of the electrode, reduce the membrane resistance of the electrode, inhibit the dissolution of transition metals in the positive electrode active material, and improve the cycle performance and high-temperature storage performance of the battery.
  • the structural unit represented by Formula I comprises one or more of a structural unit derived from vinylidene fluoride, a structural unit derived from tetrafluoroethylene, a structural unit derived from vinyl fluoride, a structural unit derived from trifluoroethylene, and a structural unit derived from hexafluoropropylene.
  • the structural unit shown in formula II comprises One or more of , wherein n is any integer between 6 and 12.
  • the second aspect of the present application also provides a method for preparing a BAB type block copolymer, characterized in that it comprises the following steps:
  • B-block polymerizing at least one monomer represented by formula V to prepare B-block,
  • a 1 , A 2 , and A 3 are each independently selected from one or more of hydrogen, fluorine, and a C 1-3 alkyl group containing at least one fluorine atom;
  • Preparing the A-block polymerizing at least one diamine and at least one dibasic anhydride or at least one dibasic acid to prepare the A-block, or ring-opening polymerizing a lactam monomer to prepare the A-block;
  • B-block and A-block are joined to prepare BAB type block copolymer.
  • this preparation method can maximize the weight average molecular weight of the fluorine-containing block and the non-fluorine block, give full play to the advantages of the fluorine-containing binder and the non-fluorine binder, and achieve the role of complementary advantages.
  • the preparation method has cheap raw materials, can reduce costs, reduce environmental pollution, and is conducive to the increase of binder production.
  • the BAB type block copolymer prepared by this method as a binder can make the electrode have excellent liquid absorption ability. The good adhesion, low membrane resistance and the cycle performance, high temperature storage performance and safety performance of the battery are improved.
  • the preparation of the B-block specifically comprises:
  • At least one monomer represented by formula V, a chain transfer agent and an initiator are subjected to reversible addition-fragmentation chain transfer polymerization at a reaction temperature of 70 to 90° C. for 5 to 8.5 hours to obtain a B-block having an azide group or an alkynyl group at one end.
  • Reversible addition-fragmentation chain transfer polymerization is used to achieve controlled polymerization, and the molecular weight distribution of the product is relatively narrow.
  • the B-block only has an alkynyl or azide group at the end, which is convenient for directing and bonding with the A-block in an efficient and mild manner to generate a BAB-type triblock copolymer.
  • the preparation of the A-block specifically comprises:
  • the catalyst, at least one diamine, at least one dibasic anhydride or at least one dibasic acid are stirred and reacted at room temperature for 4 to 10 hours, and the temperature is raised to 170 to 210° C. and reacted for 5 to 20 hours to obtain a product with both end groups being anhydride, carboxyl or amino groups;
  • the terminal groups of the product are subjected to functionalization reaction to obtain the A-block having alkynyl groups or azide groups at both ends.
  • the preparation of the A-block specifically comprises:
  • the terminal groups of the product are subjected to functionalization reaction to obtain the A-block having alkynyl groups or azide groups at both ends.
  • the A-block with azidation or alkyne at both ends prepared by the preparation method can be easily connected with the B-block in an efficient and mild manner to generate a BAB type block copolymer.
  • the preparation of the BAB type block copolymer specifically comprises:
  • the A-block having alkynyl or azide groups at both ends is mixed with the B-block having an azide or alkyne group at one end and subjected to a click reaction to prepare a BAB type block copolymer, wherein the end groups of the B-block and the A-block are different.
  • the above preparation method has the advantages of high yield, harmless by-products, simple and mild reaction conditions,
  • the advantage of readily available reaction raw materials can achieve controlled polymerization of block polymers, which is beneficial to improving the yield rate of products.
  • the chain transfer agent is a RAFT chain transfer agent containing a terminal alkynyl or azide group.
  • the end group modifier is a diamine or a dibasic acid.
  • the third aspect of the present application provides an application of a BAB type block copolymer in a secondary battery.
  • the secondary battery includes at least one of a lithium ion battery, a sodium ion battery, a magnesium ion battery, and a potassium ion battery.
  • the fourth aspect of the present application provides a positive electrode plate, including a positive electrode current collector and a positive electrode film layer arranged on at least one surface of the positive electrode current collector, wherein the positive electrode film layer includes a positive electrode active material, a conductive agent and a binder, and the binder is a BAB type block copolymer in any embodiment or a BAB type block copolymer prepared by the preparation method in any embodiment.
  • the positive electrode sheet has excellent liquid absorption rate and good bonding force, and has excellent membrane resistance and transition metal dissolution amount.
  • the binder has a mass percentage of 0.1% to 3% based on the total mass of the positive electrode active material.
  • Controlling the mass percentage of the binder within a suitable range can make the pole piece have excellent liquid absorption rate, good bonding force, and low membrane resistance.
  • the binder in the pole piece can inhibit the dissolution of transition metals in the active material, and improve the cycle performance, high temperature storage performance and safety performance of the battery.
  • the bonding force per unit length between the positive electrode film layer and the positive electrode current collector is not less than 11.5 N/m, and can be 11.5-15 N/m.
  • the positive electrode film layer of the pole piece has high bonding strength with the positive electrode current collector. During use, the positive electrode film layer is not easy to fall off from the positive electrode current collector, which helps to improve the cycle performance and safety of the battery.
  • the electrolyte absorption rate of the positive electrode plate is greater than 0.31 ⁇ g/s, and may be 0.32-0.5 ⁇ g/s, and the electrolyte has a density of 1.1-1.2 g/cm 3 .
  • the electrode has a high liquid absorption rate, which can improve the electrolyte infiltration efficiency of the electrode, improve the ion transmission path, reduce the interface resistance, and improve the battery performance.
  • a secondary battery comprising an electrode assembly and an The electrolyte is provided, and the electrode assembly comprises a separator, a negative electrode plate and a positive electrode plate according to the fourth aspect of the present application.
  • an electrical device comprising the secondary battery of the fifth aspect of the present application.
  • FIG1 is a schematic diagram of a method for preparing a BAB type block copolymer according to an embodiment of the present application
  • FIG2 is a schematic diagram of a secondary battery according to an embodiment of the present application.
  • FIG3 is an exploded view of the secondary battery of one embodiment of the present application shown in FIG2 ;
  • FIG4 is a schematic diagram of a battery module according to an embodiment of the present application.
  • FIG5 is a schematic diagram of a battery pack according to an embodiment of the present application.
  • FIG6 is an exploded view of the battery pack according to an embodiment of the present application shown in FIG5 ;
  • FIG. 7 is a schematic diagram of an electric device using a secondary battery as a power source according to an embodiment of the present application.
  • the "range” disclosed in this application is defined in the form of a lower limit and an upper limit. It is defined by selecting a lower limit and an upper limit, and the selected lower limit and upper limit define the boundary of a special range.
  • the scope defined in this way can include or exclude end values, and can be arbitrarily combined, that is, any lower limit can form a scope with any upper limit combination. For example, if the scope of 60-120 and 80-110 is listed for a specific parameter, it is understood that the scope of 60-110 and 80-120 is also expected. In addition, if the minimum range values 1 and 2 listed, and if the maximum range values 3, 4 and 5 are listed, the following scope can be all expected: 1-3, 1-4, 1-5, 2-3, 2-4 and 2-5.
  • the numerical range “ab” represents the abbreviation of any real number combination between a and b, wherein a and b are real numbers.
  • the numerical range "0-5" represents that all real numbers between "0-5" have been fully listed herein, and "0-5" is just the abbreviation of these numerical combinations.
  • a parameter is expressed as an integer ⁇ 2, it is equivalent to disclosing that the parameter is, for example, an integer of 2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12, etc.
  • the method includes steps (a) and (b), which means that the method may include steps (a) and (b) performed sequentially, or may include steps (b) and (a) performed sequentially.
  • the method may further include step (c), which means that step (c) may be added to the method in any order.
  • the method may include steps (a), (b) and (c), or may include steps (a), (c) and (b), or may include steps (c), (a) and (b), etc.
  • the “include” and “comprising” mentioned in this application represent open-ended or closed-ended expressions.
  • the “include” and “comprising” may represent that other components not listed may also be included or only the listed components may be included or only the listed components may be included.
  • the term "or” is inclusive.
  • the phrase “A or B” means “A, B, or both A and B”. More specifically, any of the following conditions satisfies the condition "A or B”: A is true (or exists) and B is false (or exists). A is false (or does not exist) and B is true (or exists); or both A and B are true (or exist).
  • PVDF polyvinylidene fluoride
  • the cost of PVDF binder is high and it cannot be recycled on a large scale due to restrictions of environmental protection policies.
  • PVDF binder is difficult to form an effective protective layer for the positive electrode active material, and cannot effectively inhibit the side reaction between the positive electrode active material and the electrolyte and the dissolution of transition metals in the positive electrode active material, resulting in problems such as gas generation, volume deformation, and deposition of transition metals at the negative electrode of the battery cell, which have a negative impact on the cycle performance and safety performance of the battery.
  • the present application provides a BAB type block copolymer, comprising an A-block and a B-block, wherein the B-block comprises a structural unit shown in formula I, and the A-block comprises one or more of a structural unit shown in formula II, a structural unit shown in formula III, and a structural unit shown in formula IV.
  • R1 , R2 , R3 are each independently selected from one or more of hydrogen, fluorine, and C1-3 alkyl containing at least one fluorine atom;
  • R4 is selected from substituted C6-25 aromatic groups;
  • R5 , R6 , R7 , R8 are each independently selected from substituted or unsubstituted C2-24 alkyl groups and substituted or unsubstituted C6-25 aromatic groups.
  • block copolymer refers to a special type of polymer made by linking two or more polymer segments with different properties. Block polymers with specific structures will exhibit different properties from simple linear polymers, many random copolymers, and even mixtures of homopolymers. Common types include AB and BAB types, in which A and B are both long chain segments; there are also (AB)n type multi-segment copolymers, in which A and B segments are relatively short.
  • the term "BAB type block copolymer” refers to a triblock copolymer with an A-block in the middle and B-blocks on both sides.
  • the B-block and the A-block are polymer segments with a predetermined degree of polymerization formed by polymerization of different monomers.
  • the B-block is a long sequence segment formed by polymerization of one or more fluorine-containing monomers
  • the A-block is a long sequence segment formed by polymerization of one or more fluorine-free monomers.
  • the B-block and the A-block are covalently bonded in an orderly manner to form a BAB type block copolymer.
  • the B-block is polyvinylidene fluoride, which is formed by the polymerization of vinylidene fluoride monomers, and has a weight average molecular weight of 100,000-500,000;
  • the A-block is polyimide, which is formed by the polymerization of dianhydride monomers and diamine monomers, and has a weight average molecular weight of 200,000-1,000,000; the end groups on both sides of the B-block and the A-block are bonded to obtain a polyvinylidene fluoride-polyimide-polyvinylidene fluoride block copolymer (BAB type block copolymer), and the weight average molecular weight of the block copolymer is 400,000-2,000,000.
  • BAB type block copolymer polyvinylidene fluoride-polyimide-polyvinylidene fluoride block copolymer
  • polymer includes, on the one hand, a collection of macromolecules that are chemically uniform but differ in degree of polymerization, molar mass and chain length, prepared by polymerization.
  • the term also includes, on the other hand, derivatives of such a collection of macromolecules formed by polymerization, i.e. compounds that can be obtained by reaction, for example addition or substitution, of functional groups in the above-mentioned macromolecules and can be chemically uniform or chemically heterogeneous.
  • C 1-3 alkyl refers to a straight or branched hydrocarbon chain radical consisting solely of carbon and hydrogen atoms, with no unsaturation in the radical, having from one to three carbon atoms, and attached to the remainder of the molecule by a single bond.
  • Examples of C 1-3 alkyl include, but are not limited to, methyl, ethyl, n-propyl, 1-methylethyl (isopropyl).
  • C 2 -C 24 alkyl should be interpreted accordingly.
  • C 1-3 alkyl containing at least one fluorine atom refers to an alkyl group containing 1 to 3 carbon atoms in which at least one H atom is replaced by a F atom.
  • the C 1-3 alkyl group containing one fluorine atom includes a -CF 3 group and a -C 2 F 6 group.
  • substituted means that at least one hydrogen atom of the compound or chemical moiety is replaced by another chemical moiety with a substituent, wherein the substituent is independently selected from: hydroxyl, thiol, amino, cyano, nitro, aldehyde, halogen atom, alkenyl, alkynyl, aryl, heteroaryl, C 1-6 alkyl, C 1-6 alkoxy.
  • C 6-25 aromatic group refers to an aromatic ring system in which at least one ring is aromatic, including but not limited to phenyl, biphenyl, indanyl, 1-naphthyl, 2-naphthyl and tetrahydronaphthyl.
  • the substituted C 6-25 aromatic group includes, but is not limited to, aralkyl, aralkyloxy, aryloxyalkyl, and a symmetrical or asymmetrical aromatic group linked via a carbonyl group or an ether group.
  • the structural unit represented by Formula I comprises one or more of a structural unit derived from vinylidene fluoride, a structural unit derived from tetrafluoroethylene, a structural unit derived from vinyl fluoride, a structural unit derived from trifluoroethylene, and a structural unit derived from hexafluoropropylene.
  • the structural unit shown in Formula II comprises One or more of , wherein n is any integer between 6 and 12.
  • the structural unit represented by formula III comprises
  • the structural unit represented by formula IV comprises
  • the BAB type block copolymer is used as a binder in a secondary battery. In some embodiments, the BAB type block copolymer is used as a pole piece binder in a secondary battery.
  • binder refers to a chemical compound, polymer or mixture that forms a colloidal solution or colloidal dispersion in a dispersion medium.
  • the dispersion medium of the binder is an aqueous solvent, such as water, that is, the binder is dissolved in the aqueous solvent.
  • the dispersion medium of the binder is an oily solvent
  • examples of the oily solvent include but are not limited to dimethylacetamide, N,N-dimethylformamide, N-methylpyrrolidone, acetone, dimethyl carbonate, ethyl cellulose, and polycarbonate. Soluble in oily solvents.
  • a binder is used to hold the electrode material and/or the conductive agent in place and adhere them to the conductive metal part to form an electrode.
  • the binder is used as a positive electrode binder to bind the positive electrode active material and/or the conductive agent to form an electrode.
  • the binder is used as a negative electrode binder to bind the negative electrode active material and/or the conductive agent to form an electrode.
  • the fluorine contained in the B-block forms hydrogen bonds with the hydroxyl and carboxyl groups on the surface of the positive electrode active material and the current collector, making the pole piece have excellent adhesion.
  • the A-block contains abundant carbonyl groups, which can form intermolecular hydrogen bonds. The hydrogen bonds interact with the hydroxyl groups on the surface of the positive electrode active material and the current collector, making the pole piece have excellent adhesion and improving the stability of the positive electrode.
  • the abundant carbonyl groups make the binder have excellent flexibility, reducing the shedding of active materials that occurs as the pole piece volume changes during the charge and discharge process, thereby improving the battery's cycle capacity retention rate.
  • the A-block comprises at least the structural unit represented by Formula II.
  • the imide bond contained in the A-block can improve the liquid absorption capacity of the electrode, improve the electrode's ability to infiltrate the electrolyte, help form a conductive network, and reduce the film resistance of the electrode.
  • the highly polar imide bond can improve the electrochemical stability and thermal stability of the binder, and effectively inhibit the physical expansion of the electrode caused by the insertion and extraction of ions during the electrochemical reaction.
  • the surface energy of the A-block containing the imide bond is relatively low, and the film-forming performance is good.
  • It can be evenly coated on the surface of the positive electrode active material, reducing the active sites on the surface of the positive electrode active material, reducing side reactions and the dissolution of transition metals, thereby improving the cycle performance and high-temperature storage performance of the electrode, and reducing the gas production of the battery at high temperature.
  • the A-block comprises at least a structural unit represented by Formula III or Formula IV.
  • the amide bond contained in the A-block can improve the liquid absorption capacity of the electrode, improve the electrode's ability to infiltrate the electrolyte, help form a conductive network, and reduce the film resistance of the electrode.
  • the strong polar amide bond can improve the electrochemical stability and thermal stability of the binder, and effectively inhibit the physical expansion of the electrode caused by the insertion and extraction of ions during the electrochemical reaction.
  • the binder when coated on the surface of the active material, it can reduce The side reaction between the low-activity material and the electrolyte inhibits the dissolution of transition metals in the active material, thereby improving the cycle performance, high-temperature storage performance and gas production performance of the electrode.
  • the binder prepared with the BAB type block copolymer can maximize the weight average molecular weight of the fluorine-containing block and the non-fluorine block, give full play to the respective advantages of the fluorine-containing binder and the non-fluorine binder, and achieve the role of complementary advantages.
  • the BAB type block copolymer can utilize the steric hindrance between the B-block and the A-block to reduce the agglomeration of the binder and improve the uniformity of the dispersion of the material in the pole piece.
  • the binder prepared with the above-mentioned BAB type block copolymer can reduce the membrane resistance of the pole piece, increase the liquid absorption rate of the pole piece, inhibit the dissolution of the transition metal in the positive electrode active material, and thus improve the cycle performance and storage performance of the battery. And compared with the simple blending of fluorine-containing polymers and non-fluorine polymers, the BAB type block copolymer can effectively inhibit the stratification of polymers of different structural units during the slurry preparation process through the interaction between the blocks.
  • the mass percentage of each B-block is 15% to 35%, and the mass percentage of the A-block is 30% to 70%, based on the total mass of the block copolymer.
  • the mass percentage of each B-block in the block copolymer can be selected as any one of 15%, 18%, 20%, 23%, 25%, 28%, 30%, 32%, and 35%, based on the total mass of the block copolymer.
  • the mass percentage of the A-block may be any one of 30%, 35%, 40%, 45%, 50%, 55%, 60%, 65%, and 70%, based on the total mass of the block copolymer.
  • the mass percentage of the B-block is too high and the mass percentage of the A-block is too low, the A-block cannot fully exert its role in increasing the liquid absorption rate, reducing the membrane resistance, and inhibiting the dissolution of transition metals in the active material, and the battery's cycle performance and safety performance cannot be effectively improved; if the mass percentage of the B-block is too low and the mass percentage of the A-block is too high, the bonding strength of the electrode and the cycle stability of the battery will be reduced.
  • the BAB type block copolymer with the mass percentage of B-block and A-block in a suitable range makes the electrode have excellent adhesion, good liquid absorption rate and low membrane resistance at the same time, and the battery has excellent cycle performance, high temperature storage performance and safety performance.
  • the weight average molecular weight of the BAB type block copolymer is 400,000 In some embodiments, the weight average molecular weight of the BAB type block copolymer can be selected from any one of 400,000 to 600,000, 600,000 to 800,000, 800,000 to 1,000,000, 1,000,000 to 1,200,000, 1,200,000 to 1,400,000, 1,400,000 to 1,600,000, 1,600,000 to 1,800,000, 1,800,000 to 2,000,000, 600,000 to 900,000, 900,000 to 1,200,000, 1,200,000 to 1,500,000, 1,500,000 to 1,800,000, and 1,200,000 to 2,000,000.
  • weight average molecular weight refers to the sum of the products of the weight fractions of molecules with different molecular weights in a polymer and their corresponding molecular weights.
  • the binder is difficult to dissolve and is easy to agglomerate with the conductive agent, resulting in excessive viscosity of the slurry, making it difficult to apply evenly, which is not conducive to the subsequent processing and production of the pole piece.
  • the weight average molecular weight of the BAB type block copolymer is too small, it is difficult to form a three-dimensional network bonding structure, and it cannot play an effective bonding and dispersion role, which is not conducive to the formation of a conductive network, resulting in an increase in the membrane resistance of the pole piece, and a decrease in the battery's cycle performance, high-temperature storage performance, and gas production performance.
  • the BAB-type block copolymer with a weight-average molecular weight within a suitable range enables the electrode to have excellent liquid absorption rate, good adhesion and low membrane resistance, and the battery has both excellent cycle performance and storage performance.
  • the A-block comprises a structural unit of Formula II containing a trifluoromethyl group.
  • the structural unit represented by formula II containing a trifluoromethyl group comprises
  • trifluoromethyl refers to a " -CF3 " group.
  • sulfone refers to a " -SO2- " group.
  • the structural unit shown in Formula II containing trifluoromethyl in the A-block can enhance the ion transfer ability of the binder, improve the liquid absorption rate of the pole piece, and reduce the membrane resistance of the pole piece.
  • the fluorine element in the trifluoromethyl group can form hydrogen bonds with the carboxyl and hydroxyl groups remaining on the surface of the active material and the current collector to further improve the bonding force of the binder.
  • the trifluoromethyl group in the A-block can improve the electrochemical stability and thermal stability of the binder, inhibit the dissolution of transition metals in the positive electrode active material, effectively inhibit the physical expansion of the pole piece caused by the insertion and removal of ions during the electrochemical reaction, and improve the battery's cycle performance, high-temperature storage performance and gas production performance.
  • the structural unit represented by formula II containing trifluoromethyl in the A-block enables the BAB-type block copolymer to further improve the adhesion and liquid absorption rate of the electrode, reduce the membrane resistance of the electrode, effectively inhibit the dissolution of transition metals in the positive electrode active material, and improve the cycle performance, high temperature storage performance and safety performance of the battery.
  • the A-block comprises a structural unit of Formula II containing a sulfone group. Yuan.
  • the structural unit represented by formula II containing a sulfone group comprises
  • the sulfone group has a strong electron-withdrawing effect, which can enhance the bonding ability between the electrode and the conductive ions in the active material, improve the bonding force of the electrode, and at the same time, the sulfone group can increase the electrolyte absorption rate of the electrode, so that the electrode has a lower membrane resistance.
  • the sulfone group can also enhance the stability of the imide bond structure and improve the structural stability of the binder during the electrode charge and discharge process, thereby improving the battery's cycle performance, high-temperature storage performance and safety performance.
  • the structural unit shown in formula II containing a sulfone group in the A-block enables the BAB-type block copolymer to further improve the adhesion and liquid absorption rate of the electrode, reduce the membrane resistance of the electrode, inhibit the dissolution of transition metals in the positive electrode active material, and improve the cycle performance and high-temperature storage performance of the battery.
  • the A-block comprises a structural unit of Formula II containing an ether bond.
  • the structural unit shown in Formula II contains an ether bond, which helps to improve the flexibility of the binder and improve the cycle performance and gas production performance of the battery.
  • One embodiment of the present application provides a method for preparing a BAB type block copolymer, comprising the following steps:
  • B-block polymerizing at least one monomer represented by formula V to prepare B-block,
  • a 1 , A 2 , and A 3 are each independently selected from one or more of hydrogen, fluorine, and a C 1-3 alkyl group containing at least one fluorine atom;
  • Preparing the A-block polymerizing at least one diamine and at least one dibasic anhydride or at least one dibasic acid to prepare the A-block, or ring-opening polymerizing a lactam monomer to prepare the A-block;
  • B-block and A-block are joined to prepare BAB type Block copolymers.
  • FIG1 a schematic diagram of a method for preparing a BAB-type block copolymer 6 is shown in FIG1 , wherein the end groups 611 of an A-block 61 comprising a structural unit 612 shown in Formula II, Formula III or Formula IV are active groups, and the terminal groups 621 of a B-block 62 comprising a structural unit 622 shown in Formula I are active groups, and the end groups 611 of the A-block react with the terminal groups 621 of the B-block to achieve bonding of polymer segments, thereby preparing a BAB-type block copolymer 6.
  • diamine refers to an amine containing two amino groups.
  • the diamine is an aliphatic diamine or an aromatic diamine, comprising
  • n is any integer between 6 and 12.
  • dianhydride refers to a monomer containing two anhydrides.
  • the dibasic anhydride is an aromatic dianhydride, comprising One or more of .
  • diacid refers to a monomer containing two carboxyl groups.
  • the dibasic acid can be selected from aromatic dibasic acids or aliphatic dibasic acids, such as one or more of adipic acid, sebacic acid, terephthalic acid, and isophthalic acid.
  • the preparation method has cheap raw materials, can reduce costs, reduce environmental pollution, and is conducive to the improvement of binder production.
  • the BAB type block copolymer prepared by this method as a binder can make the pole piece have excellent liquid absorption capacity, good adhesion, and low membrane resistance, so that the battery's cycle performance, high temperature storage performance and safety performance are improved. to improvement.
  • the preparation of the B-block specifically comprises:
  • At least one monomer represented by formula V, a chain transfer agent and an initiator are polymerized by reversible addition-fragmentation chain transfer to obtain a B-block having an azide group or an alkynyl group at one end.
  • the reaction temperature of the reversible addition-fragmentation chain transfer polymerization is 70 to 90° C., and the reaction time is 5 to 8.5 hours.
  • the preparation of the B-block specifically comprises:
  • At least one monomer represented by formula V, a chain transfer agent and an initiator are subjected to reversible addition-fragmentation chain transfer polymerization at a reaction temperature of 70 to 90° C. for 5 to 8.5 hours to obtain a B-block having an azide group or an alkynyl group at one end.
  • azide group refers to a -N3 group.
  • alkynyl refers to a -C ⁇ CH group.
  • RAFT polymerization is a type of reversibly deactivated free radical polymerization, also known as a "living/controlled free radical polymerization method".
  • the main principle of RAFT polymerization is to add a RAFT agent as a chain transfer agent to the free radical polymerization, and protect the easily terminated free radicals through chain transfer, so that most of the free radicals in the polymerization reaction are converted into dormant free radicals.
  • dormant segments and active segments exist at the same time and are constantly and rapidly switched to each other through dynamic reversible reactions, resulting in only a few polymer chains existing in the form of active chains and growing at any one time, and finally making the growth probability of each polymer segment roughly equal, thus showing the characteristics of living polymerization.
  • the monomer represented by formula V is one or more of vinylidene fluoride, tetrafluoroethylene, and vinyl fluoride.
  • the synthesis route of the B-block is shown in the figure below, wherein the chain transfer agent is trithiocarbonate, Z' is an active group having an alkynyl or azide group at the end, and R is an alkyl group.
  • the B-block having an alkynyl or azide group at the end is prepared by the following reaction.
  • the reversible addition-fragmentation chain transfer polymerization can achieve controllable polymerization, and the molecular weight distribution of the product is relatively narrow.
  • the B-block only has an alkynyl or azide group at the end, which is convenient for directing and bonding with the A-block in an efficient and mild manner to generate a BAB-type triblock copolymer.
  • controllable polymerization can be achieved, and the molecular weight distribution of the product is relatively narrow.
  • the preparation of the A-block specifically comprises:
  • the terminal groups of the product are subjected to functionalization reaction to obtain the A-block having alkynyl groups or azide groups at both ends.
  • the polymerization conditions of at least one diamine and at least one dibasic anhydride or at least one dibasic acid are stirring the reaction at room temperature for 4 to 10 hours, and then heating to 170 to 210° C. for 5 to 20 hours.
  • the preparation of the A-block specifically comprises:
  • the catalyst, at least one diamine and at least one dibasic anhydride or at least one dibasic acid are stirred and reacted at room temperature for 4 to 10 hours, and the temperature is raised to 170 to 210° C. and reacted for 5 to 20 hours to obtain a product having end groups at both ends being anhydride, carboxyl or amino groups;
  • the terminal groups of the product are subjected to functionalization reaction to obtain the A-block having alkynyl groups or azide groups at both ends.
  • the synthesis route of the A-block is that at least one diamine and at least one dibasic anhydride undergo a polymerization reaction under the action of a catalyst to generate a polyimide, so that the diamine or dibasic anhydride is in excess, and a polyimide with amino groups or acid anhydrides at both ends is obtained, and the amino groups or acid anhydrides at both ends are functionalized with an active monomer containing an azide group or an alkynyl group to prepare an A-block with an azide group or an alkynyl group at both ends.
  • the active monomer containing an azide group or an alkynyl group refers to a monomer containing an azide group or an alkynyl group and containing an azide group or an alkynyl group.
  • the monomer having an active functional group that reacts with the amino group or acid anhydride at both ends of the polyimide, the active functional group that reacts with the amino group can be any one of epoxy, carboxyl, acid anhydride, isocyanate, and carbonyl chloride.
  • the active functional group that reacts with the acid anhydride can be an amino group.
  • amino refers to a -NH2 group.
  • anhydride refers to a -CO-O-CO- group.
  • epoxy refers to a -CH-O-CH- group.
  • carboxyl refers to a -COOH group.
  • isocyanate refers to an -NCO group.
  • carbonyl chloride refers to a -COCl group.
  • amino refers to a "-NH-" group.
  • the synthesis route of the A-block is that at least one diamine and at least one dibasic acid undergo a polycondensation reaction to generate polyamide under the action of a catalyst, so that the diamine or dibasic acid is excessive, and the end groups at both ends are amino or carboxyl polyamides, and the amino or carboxyl groups at both ends are functionalized with active monomers containing azide groups or alkynyl groups to prepare A-blocks with azide groups or alkynyl groups at both ends.
  • the active monomer containing azide groups or alkynyl groups refers to a monomer containing azide groups or alkynyl groups and containing active functional groups that can react with amino groups or carboxyl groups at both ends of the polyamide, and the active functional groups that react with amino groups can be selected from any one of epoxy groups, carboxyl groups, acid anhydrides, isocyanate groups, and carbonyl chloride.
  • the active functional group that reacts with carboxyl groups can be selected from amino groups or imino groups.
  • the catalyst may be any one of quinoline, isoquinoline, and tertiary amine.
  • the preparation of the A-block specifically comprises:
  • a terminal group regulator, water and at least one lactam monomer are polymerized to obtain a product having terminal groups at both ends being carboxyl groups or amino groups;
  • the terminal groups of the product are functionalized to obtain an A-block having alkynyl or azide groups at both ends.
  • the polymerization reaction conditions of the terminal group regulator, water and at least one lactam monomer are 250° C. to 280° C. for 12 to 24 hours.
  • the preparation of the A-block specifically comprises:
  • the end group regulator, water and at least one lactam monomer are reacted at 250°C to 280°C.
  • the polymerization reaction is carried out at a temperature of 12 to 24 hours to obtain a product having carboxyl or amino groups at both ends;
  • the terminal groups of the product are functionalized to obtain an A-block having alkynyl or azide groups at both ends.
  • the synthesis route of the A-block is as follows, under the catalysis of water, the lactam monomer undergoes a ring-opening polymerization reaction to obtain a polyamide with an amino group at one end and a carboxyl group at the other end, and then an end group regulator is added to react with the polyamide to obtain a polyamide with amino or carboxyl groups at both ends, and the amino or carboxyl groups at both ends are functionalized with an active monomer containing an azide group or an alkynyl group to prepare an A-block with an azide group or an alkynyl group at both ends.
  • the active monomer containing an azide group or an alkynyl group refers to a monomer containing an azide group or an alkynyl group and containing an active functional group that can react with the amino or carboxyl groups at both ends of the polyamide, and the active functional group that reacts with the amino group can be selected from any one of an epoxy group, a carboxyl group, an anhydride group, an isocyanate group, and a carbonyl chloride group.
  • the active functional group that reacts with the carboxyl group can be selected from an amino group or an imino group.
  • the lactam monomer may be selected from one or more of caprolactam, capryllactam, decanolactam, and laurolactam.
  • the A-block with azidation or alkyne at both ends prepared by the preparation method can be easily connected with the B-block in an efficient and mild manner to generate a BAB type block copolymer.
  • the preparation of the BAB type block copolymer specifically comprises:
  • the A-block having alkynyl or azide groups at both ends is mixed with the B-block having an azide or alkyne group at one end and subjected to a click reaction to prepare a BAB type block copolymer, wherein the end groups of the B-block and the A-block are different.
  • click reaction refers to a cycloaddition reaction between an alkynyl group and an azide group, so that the A-block is connected to the B-block.
  • the click reaction is carried out in the presence of a Cu(I) catalyst at room temperature and pressure.
  • the terminal group of the B-block is an azide group and the terminal group of the A-block is an alkynyl group.
  • the terminal group of the B-block is an alkynyl group and the terminal group of the A-block is an azide group.
  • the above preparation method has the advantages of high yield, harmless by-products, simple and mild reaction conditions, and readily available reaction raw materials. It can achieve controlled polymerization of block polymers, which is beneficial to improving the yield rate of products.
  • the chain transfer agent is a RAFT chain transfer agent containing a terminal alkynyl or azide group. In some embodiments, the chain transfer agent is a trithiocarbonate containing a terminal alkynyl or azide group. In some embodiments, the structural formula of the chain transfer agent is selected from the following formula,
  • the RAFT chain transfer agent containing a terminal alkynyl or azide group allows the terminal of the B-block to carry an alkynyl or azide group during the synthesis of the B-block, providing a basis for the click reaction between the A-block and the B-block, avoiding complex post-processing steps, and improving the reaction efficiency.
  • the end group modifier is a diamine or a dibasic acid.
  • the end group regulator of the diamine or dibasic acid can react with the end group of the product to obtain a product with both end groups being amino or carboxyl, which is convenient for subsequent conversion and can prepare A-blocks with both end groups being azido or alkynyl in a simple and efficient manner.
  • the BAB type block copolymer may be used in a secondary battery.
  • the secondary battery includes at least one of a lithium ion battery, a sodium ion battery, a magnesium ion battery, and a potassium ion battery.
  • the positive electrode plate includes a positive electrode current collector and a positive electrode film layer arranged on at least one surface of the positive electrode current collector, wherein the positive electrode film layer includes a positive electrode active material, a conductive agent and a binder, and the binder is a BAB type block copolymer in some embodiments or a BAB type block copolymer prepared by the preparation method in some embodiments.
  • the positive electrode sheet has excellent liquid absorption rate and good bonding force, low membrane resistance and transition metal dissolution amount.
  • the mass percentage of the binder is 0.1% to 3%, based on the total mass of the positive electrode active material. In some embodiments, the mass percentage of the binder can be selected from any one of 0.1% to 0.2%, 0.2% to 1%, 0.2% to 1.03%, 1% to 3%, and 1.03% to 3%.
  • the binder content When the binder content is too low, the binder cannot fully exert its bonding and dispersion effects, resulting in insufficient bonding force of the pole piece and increased membrane resistance, which has a negative impact on the battery's cycle performance and high-temperature storage performance.
  • the binder content is too high, the viscosity of the slurry is too high, which will cause the binder coating layer on the surface of the positive electrode active material to be too thick, affecting the transmission of electrons and ions during the battery cycle, increasing the internal resistance of the pole piece membrane, and affecting the battery's cycle performance and high-temperature storage performance.
  • Controlling the mass percentage of the binder within a suitable range can make the pole piece have excellent liquid absorption rate, good bonding force, and low membrane resistance.
  • the binder in the pole piece can inhibit the dissolution of transition metals in the active material, and improve the cycle performance, high temperature storage performance and safety performance of the battery.
  • the bonding force per unit length between the positive electrode film layer and the positive electrode current collector is not less than 11.5 N/m, and can be 11.5-15 N/m. In some embodiments, the bonding force per unit length between the positive electrode film layer and the positive electrode current collector can be 11.5 N/m, 12 N/m, 12.5 N/m, 13 N/m, 13.5 N/m, 14 N/m, 14.5 N/m, or 15 N/m.
  • the bonding force per unit length between the positive electrode film layer and the positive electrode current collector can be tested by any means known in the art, such as testing with reference to GB-T2790-1995 national standard "Adhesive 180° Peel Strength Test Method".
  • the positive electrode plate is cut into a test specimen of 20* 100mm2 size for use; the electrode is bonded to one side of the positive electrode film layer with double-sided tape, and compacted with a pressure roller to make the double-sided tape and the electrode completely fit; the other side of the double-sided tape is adhered to the stainless steel surface, and one end of the sample is bent in the opposite direction with a bending angle of 180°; the high-speed rail tensile machine is used for testing, one end of the stainless steel is fixed to the lower fixture of the tensile machine, and the bent end of the sample is fixed to the upper fixture, the angle of the sample is adjusted to ensure that the upper and lower ends are in a vertical position, and then the sample is stretched at a speed of 50mm/min until the positive
  • the layers are peeled off, and the displacement and force in the process are recorded.
  • the force when the force is balanced is divided by the width of the electrode attached to the double-sided adhesive (the width direction of the electrode is perpendicular to the peeling direction) as the bonding force of the electrode per unit length. In this test, the width of the electrode is 20mm.
  • the positive electrode film layer of the pole piece has high bonding strength with the positive electrode current collector. During use, the positive electrode film layer is not easy to fall off from the positive electrode current collector, which helps to improve the cycle performance and safety of the battery.
  • the electrolyte absorption rate of the positive electrode plate is greater than 0.31 ⁇ g/s, and may be 0.32-0.5 ⁇ g/s, and the electrolyte has a density of 1.1-1.2 g/cm 3 .
  • the liquid absorption rate of the positive electrode plate to the electrolyte can be selected as 0.32 ⁇ g/s, 0.33 ⁇ g/s, 0.34 ⁇ g/s, 0.35 ⁇ g/s, 0.36 ⁇ g/s, 0.37 ⁇ g/s, 0.38 ⁇ g/s, 0.39 ⁇ g/s, 0.40 ⁇ g/s, 0.41 ⁇ g/s, 0.42 ⁇ g/s, 0.43 ⁇ g/s, 0.44 ⁇ g/s, 0.45 ⁇ g/s, 0.46 ⁇ g/s, 0.47 ⁇ g/s, 0.484 ⁇ g/s, 0.49 ⁇ g/s, 0.50 ⁇ g/s, and the density of the electrolyte is 1.1-1.2g/ cm3 .
  • the liquid absorption rate of the electrode can reflect the ability of the electrode to wet in the electrolyte.
  • the electrolyte can be prepared by dissolving lithium hexafluorophosphate in a mixed solvent of ethylene carbonate and ethyl methyl carbonate, the mass content of the lithium hexafluorophosphate solution is 12.5%, and the volume ratio of ethylene carbonate to ethyl methyl carbonate in the solution is 3:7.
  • the electrode has a high liquid absorption rate, which can improve the electrolyte infiltration efficiency of the electrode, improve the ion transmission path, reduce the interface resistance, and improve the battery performance.
  • the positive electrode current collector has two surfaces opposite to each other in its thickness direction, and the positive electrode film layer is disposed on any one or both of the two opposite surfaces of the positive electrode current collector.
  • the positive electrode current collector may be a metal foil or a composite current collector.
  • aluminum foil may 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 may be formed by forming a metal material (aluminum, aluminum alloy, nickel, nickel alloy, titanium, titanium alloy, silver and silver alloy, etc.) on a polymer material substrate (such as a substrate of polypropylene (PP), polyethylene terephthalate (PET), polybutylene terephthalate (PBT), polystyrene (PS), polyethylene (PE), etc.).
  • PP polypropylene
  • PET polyethylene terephthalate
  • PBT polybutylene terephthalate
  • PS polystyrene
  • PE polyethylene
  • the positive electrode active material may be a positive electrode active material for a battery known in the art.
  • the positive electrode active material may include at least one of the following materials: an olivine-structured lithium-containing phosphate, a lithium transition metal oxide, and their respective modified compounds.
  • the present application is not limited to these materials, and other traditional materials that can be used as positive electrode active materials for batteries may 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 oxide (such as LiCoO2 ), lithium nickel oxide (such as LiNiO2 ), lithium manganese oxide (such as LiMnO2 , LiMn2O4 ), lithium nickel cobalt oxide, lithium manganese cobalt oxide, lithium nickel manganese oxide, lithium nickel cobalt manganese oxide (such as LiNi1 / 3Co1 / 3Mn1 / 3O2 (also referred to as NCM333 ), LiNi0.5Co0.2Mn0.3O2 (also referred to as NCM523 ) , LiNi0.5Co0.25Mn0.25O2 (also referred to as NCM211 ) , LiNi0.6Co0.2Mn0.2O2 (also referred to as NCM622 ), LiNi0.8Co0.1Mn0.1O2 (also referred to as NCM811 ), lithium nickel cobalt aluminum oxide (such as LiNi 0.85 Co 0.15 Al 0.05
  • lithium-containing phosphates with an olivine structure may include, but are not limited to, at least one of lithium iron phosphate (such as LiFePO 4 (also referred to as LFP)), a composite material of lithium iron phosphate and carbon, lithium manganese phosphate (such as LiMnPO 4 ), a composite material of lithium manganese phosphate and carbon, lithium iron manganese phosphate, and a composite material of lithium iron manganese phosphate and carbon.
  • lithium iron phosphate such as LiFePO 4 (also referred to as LFP)
  • LiMnPO 4 lithium manganese phosphate
  • LiMnPO 4 lithium manganese phosphate
  • LiMnPO 4 lithium manganese phosphate and carbon
  • the positive electrode film layer may further include a conductive agent, which may include, for example, at least one of superconducting carbon, acetylene black, carbon black, Ketjen black, carbon dots, carbon nanotubes, graphene, and carbon nanofibers.
  • a conductive agent which may include, for example, at least one of superconducting carbon, acetylene black, carbon black, Ketjen black, carbon dots, carbon nanotubes, graphene, and carbon nanofibers.
  • the positive electrode sheet can be prepared by the following method: the components for preparing the positive electrode sheet, such as the positive electrode active material, the conductive agent, the binder and Any other components are dispersed in a solvent (such as N-methylpyrrolidone) to form a positive electrode slurry; the positive electrode slurry is coated on the positive electrode collector, and after drying, cold pressing and other processes, a positive electrode sheet can be obtained.
  • a solvent such as N-methylpyrrolidone
  • the negative electrode sheet includes a negative electrode current collector and a negative electrode film layer disposed on at least one surface of the negative electrode current collector, wherein the negative electrode film layer includes a negative electrode active material.
  • the negative electrode current collector has two surfaces opposite to each other in its thickness direction, and the negative electrode film layer is disposed on any one or both of the two opposite surfaces of the negative electrode current collector.
  • the negative electrode current collector may be a metal foil or a composite current collector.
  • the metal foil copper foil may be used.
  • the composite current collector may include a polymer material base layer and a metal layer formed on at least one surface of the polymer material substrate.
  • the composite current collector may be formed by forming a metal material (copper, copper alloy, nickel, nickel alloy, titanium, titanium alloy, silver and silver alloy, etc.) on a polymer material substrate (such as a substrate of polypropylene (PP), polyethylene terephthalate (PET), polybutylene terephthalate (PBT), polystyrene (PS), polyethylene (PE), etc.).
  • PP polypropylene
  • PET polyethylene terephthalate
  • PBT polybutylene terephthalate
  • PS polystyrene
  • PE polyethylene
  • the negative electrode active material may adopt the negative electrode active material for the battery known in the art.
  • the negative electrode active material may include at least one of the following materials: artificial graphite, natural graphite, soft carbon, hard carbon, silicon-based materials, tin-based materials, lithium titanate, etc.
  • the silicon-based material may be selected from at least one of elemental silicon, silicon oxide compounds, silicon-carbon composites, silicon-nitrogen composites, and silicon alloys.
  • the tin-based material may be selected from at least one of elemental tin, tin oxide compounds, and tin alloys.
  • the present application is not limited to these materials, and other traditional materials that can be used as negative electrode active materials for batteries may also be used. These negative electrode active materials may be used alone or in combination of two or more.
  • the negative electrode film layer may further include a binder.
  • the binder may be selected from at least one of styrene-butadiene rubber (SBR), polyacrylic acid (PAA), sodium polyacrylate (PAAS), polyacrylamide (PAM), polyvinyl alcohol (PVA), sodium alginate (SA), polymethacrylic acid (PMAA) and carboxymethyl chitosan (CMCS).
  • the negative electrode film layer may also optionally include a conductive agent.
  • the conductive agent may At least one selected from superconducting carbon, acetylene black, carbon black, Ketjen black, carbon dots, carbon nanotubes, graphene and carbon nanofibers.
  • the negative electrode film layer may optionally include other additives, such as a thickener (eg, sodium carboxymethyl cellulose (CMC-Na)).
  • a thickener eg, sodium carboxymethyl cellulose (CMC-Na)
  • the negative electrode sheet can be prepared in the following manner: the components for preparing the negative electrode sheet, such as the negative electrode active material, the conductive agent, the binder and any other components are dispersed in a solvent (such as deionized water) to form a negative electrode slurry; the negative electrode slurry is coated on the negative electrode collector, and after drying, cold pressing and other processes, the negative electrode sheet can be obtained.
  • a solvent such as deionized water
  • the electrolyte plays the role of conducting ions between the positive electrode and the negative electrode.
  • the present application has no specific restrictions on the type of electrolyte, which can be selected according to needs.
  • the electrolyte can be liquid, gel or all-solid.
  • the electrolyte is an electrolyte solution, which includes an electrolyte salt and a solvent.
  • the electrolyte salt can be selected from at least one of lithium hexafluorophosphate, lithium tetrafluoroborate, lithium perchlorate, lithium hexafluoroarsenate, lithium bis(fluorosulfonyl)imide, lithium bis(trifluoromethanesulfonyl)imide, lithium trifluoromethanesulfonate, lithium difluorophosphate, lithium difluorooxalatoborate, lithium dioxalatoborate, lithium difluorodioxalatophosphate, and lithium tetrafluorooxalatophosphate.
  • the solvent can be selected from at least one of 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, 1,4-butyrolactone, cyclopentane sulfone, dimethyl sulfone, methyl ethyl sulfone and diethyl sulfone.
  • the electrolyte may further include additives, such as negative electrode film-forming additives, positive electrode film-forming additives, and additives that can improve certain battery properties, such as additives that improve battery overcharge performance, additives that improve battery high or low temperature performance, etc.
  • additives such as negative electrode film-forming additives, positive electrode film-forming additives, and additives that can improve certain battery properties, such as additives that improve battery overcharge performance, additives that improve battery high or low temperature performance, etc.
  • the secondary battery further includes a separator.
  • the present application has no particular limitation on the type of separator, and any known porous separator with good chemical stability and mechanical stability can be selected.
  • the material of the isolation membrane can be selected from at least one of glass fiber, non-woven fabric, polyethylene, polypropylene and polyvinylidene fluoride.
  • the isolation membrane can be a single-layer film or a multi-layer composite film, without particular limitation.
  • the materials of each layer can be the same or different, without particular limitation.
  • the positive electrode sheet, the negative electrode sheet, and the separator may be formed into an electrode assembly by a winding process or a lamination process.
  • the secondary battery may include an outer package, which may be used to encapsulate the electrode assembly and the electrolyte.
  • the outer packaging of the secondary battery may be a hard shell, such as a hard plastic shell, an aluminum shell, a steel shell, etc.
  • the outer packaging of the secondary battery may also be a soft package, such as a bag-type soft package.
  • the material of the soft package may be plastic, and examples of the plastic include polypropylene, polybutylene terephthalate, and polybutylene succinate.
  • FIG2 is a secondary battery 5 of a square structure as an example.
  • the secondary battery may also be a sodium ion battery, a magnesium ion battery, or a potassium ion battery.
  • the outer package may include a shell 51 and a cover plate 53.
  • the shell 51 may include a bottom plate and a side plate connected to the bottom plate, and the bottom plate and the side plate enclose a receiving cavity.
  • the shell 51 has an opening connected to the receiving cavity, and the cover plate 53 can be covered on the opening to close the receiving cavity.
  • the positive electrode sheet, the negative electrode sheet and the isolation film can form an electrode assembly 52 through a winding process or a lamination process.
  • the electrode assembly 52 is encapsulated in the receiving cavity.
  • the 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 batteries can be assembled into battery modules.
  • the number of the secondary batteries included may 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.
  • FIG4 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. Of course, they may also be arranged in any other manner. Further, the plurality of secondary batteries 5 may be fixed by fasteners.
  • the battery module 4 may further include a housing having a housing space, and the plurality of secondary batteries 5 are housed in the housing space.
  • an electric device comprising at least one of a secondary battery of any embodiment, a battery module of any embodiment, or a battery pack of any embodiment.
  • the electrical device 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 for the electrical device, and can also be used as an energy storage unit for the electrical device.
  • the electrical device may include mobile devices (such as mobile phones, laptops, etc.), electric vehicles (such as pure electric vehicles, hybrid electric vehicles, plug-in hybrid electric vehicles, electric bicycles, electric scooters, electric golf carts, electric trucks, etc.), electric trains, ships and satellites, energy storage systems, etc., but are not limited thereto.
  • a secondary battery, a battery module or a battery pack may be selected according to its usage requirements.
  • FIG7 is an example of an electric 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 mobile phone, a tablet computer, a notebook computer, etc. Such a device is usually required to be thin and light, and a secondary battery may be used as a power source.
  • A4 is the residue of diamine
  • A5 is the residue of dianhydride
  • x is the degree of polymerization of A - block.
  • RAFT chain transfer agent CTA-alkyne
  • azobisisobutyronitrile in a molar ratio of 700:1:0.1
  • the mixture was subjected to at least three freeze-thaw cycles and placed in an oil bath preheated to 80 ° C. After 6 hours of reaction, the reaction was terminated by cooling in liquid nitrogen and the solution was precipitated in a large excess of methanol. The polymer was collected by filtration and reprecipitated twice from chloroform with methanol. The resulting product was dried under vacuum at room temperature overnight to remove all traces of residual solvent to obtain polyvinylidene fluoride with alkynyl groups at the end, i.e., B-block polymer.
  • Polyvinylidene fluoride with an alkynyl group at the end, polyimide with an azide group at both ends, and CuBr were added to a dry Schlenk tube in a molar ratio of 1:2.5:4. After degassing, 4 ml of anhydrous N,N-dimethylformamide (DMF) and 0.14 mmol N,N,N',N,'N"-pentamethyldiethylenetriamine (PMDETA) were added. The reaction was stirred at 60°C for 3 days and terminated by exposure to air.
  • DMF N,N-dimethylformamide
  • PMDETA 0.14 mmol N,N,N',N,'N"-pentamethyldiethylenetriamine
  • the reaction mixture was filtered through a neutral alumina column to remove the copper catalyst, the solution was concentrated under reduced pressure and precipitated in a 20-fold excess of a mixed solvent (the volume ratio of methanol to water was 1:1), the product was collected by filtration, and vacuum dried to obtain a BAB-type block copolymer, which was used as a battery binder.
  • NCM Lithium nickel cobalt manganese
  • conductive agent carbon black conductive agent carbon black
  • binder conductive agent carbon black
  • NMP N-methylpyrrolidone
  • the active material artificial graphite, the conductive agent carbon black, the binder styrene-butadiene rubber (SBR), and the thickener sodium hydroxymethyl cellulose (CMC) are dissolved in the solvent deionized water in a weight ratio of 96.2:0.8:0.8:1.2, and the negative electrode slurry is prepared after being evenly mixed; the negative electrode slurry is evenly coated on the negative electrode collector copper foil once or multiple times, and the negative electrode sheet is obtained after drying, cold pressing, and slitting.
  • Polypropylene film is used as the isolation film.
  • the positive electrode sheet, the separator, and the negative electrode sheet of Example 1 are stacked in order, so that the separator is between the positive and negative electrode sheets to play an isolating role, and then wound to obtain a bare cell, and the bare cell is welded with a pole ear, and the bare cell is placed in an aluminum shell, and baked at 80°C to remove water, and then the electrolyte is injected and sealed to obtain an uncharged battery.
  • the uncharged battery is then subjected to the processes of static, hot and cold pressing, formation, shaping, and capacity testing in sequence to obtain the lithium-ion battery product of Example 1.
  • the battery of Example 2 is prepared in a similar manner to the battery of Example 1, but the polymerization reaction temperature and reaction time of the B-block, the molar amounts of the dianhydride and diamine of the A-block, the polymerization degrees of the B-block and the A-block, and the weight average molecular weights of the B-block and the A-block are adjusted.
  • the specific adjustment parameters are shown in Table 1.
  • the preparation methods of the batteries of Examples 12 to 15 are similar to those of the battery of Example 1, but the mass percentage of the binder is adjusted.
  • the specific parameters are shown in Table 1 based on the mass of the positive electrode active material.
  • the battery of Example 16 is prepared in a similar manner to the battery of Example 4, except that the diamine
  • the monomer was adjusted to 9.5 mmol of 1,4-bis(4-aminophenylsulfone)benzene, so that the prepared A-block was polyimide-2 containing only sulfone groups and having azide groups at both ends.
  • the specific parameters are shown in Table 1.
  • the preparation method of the battery of Example 17 is similar to that of the battery of Example 4, but the diamine is adjusted to 9.5 mmol of 1,4-bis(2-trifluoromethyl-4-aminophenoxy)benzene, so that the prepared A-block is a polyimide containing only trifluoromethyl groups and having azide groups at both ends.
  • the specific parameters are shown in Table 1.
  • the preparation method of the battery of Example 18 is similar to that of the battery of Example 4, but the A-block is replaced with polyamide-6 having azide groups at both ends.
  • the specific parameters are shown in Table 1, and the preparation method is as follows:
  • the preparation method of the battery of Example 19 is similar to that of the battery of Example 4, but the diamine is adjusted to 1,4-bis(4-aminophenoxy)benzene.
  • the specific parameters are shown in Table 1.
  • the preparation method of the battery of Example 20 is similar to that of the battery of Example 4, but the dianhydride is adjusted to 2,2'-bis(trifluoromethyl)-3,3',4,4'-diphenyl ether tetracarboxylic dianhydride, and the diamine is adjusted to 4,4'-diaminodiphenyl ether.
  • the specific parameters are shown in Table 1.
  • the preparation method of the battery of Example 21 is similar to that of the battery of Example 4, but the dianhydride is adjusted to 2,2'-bis(trifluoromethyl)-3,3',4,4'-diphenylethertetracarboxylic dianhydride, and the diamine is adjusted to 1,4-(bis-2-trifluoromethyl-4-aminophenoxy)benzene.
  • the specific parameters are shown in Table 1.
  • the preparation method of the battery of Example 22 is similar to that of the battery of Example 4, but the diamine is adjusted to 4,4'-diaminodiphenyl sulfone.
  • the specific parameters are shown in Table 1.
  • the preparation method of the battery of Example 23 is similar to that of the battery of Example 4, but the dianhydride is adjusted to 3,3',4,4'-diphenylsulfone tetracarboxylic dianhydride, and the diamine is adjusted to 1,4-bis(2-trifluoro methyl-4-aminophenone)benzene, the specific parameters are shown in Table 1.
  • the preparation method of the battery of Example 24 is similar to that of the battery of Example 4, but the dianhydride is adjusted to 2,2'-bis(trifluoromethyl)-3,3',4,4'-diphenylethertetracarboxylic dianhydride, and the diamine is adjusted to 4,4'-diaminodiphenyl sulfone.
  • the specific parameters are shown in Table 1.
  • the preparation method of the battery of Example 25 is similar to that of the battery of Example 4, but the A-block is replaced with polyamide-66 having azide groups at both ends.
  • the specific parameters are shown in Table 1, and the preparation method is as follows:
  • the preparation method of the battery of Comparative Example 1 is similar to that of the battery of Example 1, but the binder is polyvinylidene fluoride with a weight average molecular weight of 1.2 million.
  • the specific parameters are shown in Table 1 and are purchased from Solvay Group's 5130.
  • the preparation method of the battery in Comparative Example 2 is similar to that of the battery in Example 1, but the binder is polyimide-1 with a weight average molecular weight of 1.2 million.
  • the specific parameters are shown in Table 1.
  • the preparation method is similar to that of the polyimide-1 in Example 1, except that the diamine content is adjusted to 24 mmol; the dianhydride content is adjusted to 24.5 mmol, wherein the solid content in the reaction system is 15%, and stirring is carried out at room temperature for 12 hours under a nitrogen atmosphere. After stirring at room temperature, the temperature is raised to 180°C, and stirring is continued for 20 hours under a nitrogen atmosphere.
  • the polyimide containing trifluoromethyl and sulfone groups is purified and dried, and the weight average molecular weight thereof is 1.2 million.
  • the preparation method of the battery of Comparative Example 3 is similar to that of the battery of Example 1, but the binder is a blend of polyvinylidene fluoride and polyimide.
  • the specific parameters are shown in Table 1.
  • the preparation method is as follows:
  • Blending The polyimide-1 in comparative example 2 and the polyvinylidene fluoride in comparative example 1 were blended in a mass ratio of 6:4 to obtain a polyvinylidene fluoride and polyimide-1 blend adhesive. dose.
  • the prepared lithium-ion battery was charged and discharged for the first time with a current of 0.5C (i.e., the current value that completely discharges the theoretical capacity within 2 hours).
  • the charging was constant current and constant voltage charging, the termination voltage was 4.2V, the cut-off current was 0.05C, and the discharge termination voltage was 2.8V.
  • the battery was left for 24 hours, it was charged to 4.2V with a constant current and constant voltage of 0.5C, and then the fully charged battery was discharged with a current of 1C.
  • the discharge termination voltage was 2.8V.
  • the battery cell was disassembled, the negative electrode plate was taken out, and the ICP (inductively coupled plasma) method was used to test the deposition of metal Co and Mn.
  • the battery capacity retention rate data corresponding to the embodiments or comparative examples in Table 1 are the data measured after 500 cycles under the above test conditions, that is, the value of P500.
  • Lithium ion secondary battery storage capacity retention rate (%) CAP 2 /CAP 1 * 100%.
  • Full batteries with 100% state of charge (SOC) are stored at 70°C.
  • the open circuit voltage (OCV) and AC internal resistance (IMP) of the battery cells are measured before, during and after storage to monitor the SOC, and the volume of the battery cells is measured.
  • the full battery is taken out after every 48 hours of storage, and the OCV and IMP are tested after standing for 1 hour.
  • the volume of the battery cells is measured by the water displacement method after cooling to room temperature.
  • the water displacement method is to first use a balance that automatically converts units using dial data to measure the gravity F1 of the battery cell separately, and then place the battery cell completely in deionized water (density is known to be 1g/ cm3 ), and measure the gravity F2 of the battery cell at this time.
  • the battery cell After each volume test, the battery cell is recharged at a constant current of 1C to 4.25V, and then charged at a constant voltage of 4.25V until the current drops to 0.05C. After the recharging is completed, the battery cell is put into the furnace to continue testing.
  • the volume of the battery cells was measured, and the increase in the volume of the battery cells after storage relative to the volume of the battery cells before storage, i.e. the gas production, was calculated.
  • the gas production/initial volume of the battery cells gave the battery volume expansion rate.
  • a Waters 2695 Isocratic HPLC gel chromatograph (differential refractive index detector 2141) was used.
  • a 3.0% polystyrene solution sample was used as a reference, and a matching chromatographic column (oily: Styragel HT5 DMF7.8*300mm+Styragel HT4) was selected.
  • a 3.0% polymer solution was prepared with purified N-methylpyrrolidone (NMP) solvent, and the prepared solution was allowed to stand for one day for use.
  • NMP N-methylpyrrolidone
  • tetrahydrofuran was first drawn with a syringe and rinsed, and repeated several times. Then 5 ml of the experimental solution was drawn, the air in the syringe was removed, and the needle tip was wiped dry. Finally, the sample solution was slowly injected into the injection port. Data was obtained after the indication stabilized.
  • the binders in Examples 1 to 25 all include BAB type block copolymers, wherein the B-blocks all include structural units derived from vinylidene fluoride, and the A-blocks include imide or amide structural units.
  • the binders prepared with the above polyvinylidene fluoride-polyimide-polyvinylidene fluoride block copolymers or polyvinylidene fluoride-polyamide-polyvinylidene fluoride block copolymers can reduce the film resistance of the pole piece, increase the liquid absorption rate of the pole piece, inhibit the dissolution of transition metals in the positive electrode active material, and thus improve the cycle performance and storage performance of the battery.
  • the BAB-type block copolymer can reduce the diaphragm resistance of the electrode, effectively inhibit the dissolution of transition metals in the positive electrode active material, improve the cycle performance and high-temperature storage performance of the battery, and reduce the gas production of the battery at high temperature.
  • the BAB-type block copolymer can reduce the diaphragm resistance of the electrode, improve the cycle performance and high-temperature storage performance of the battery, while further taking into account the adhesion and liquid absorption rate of the electrode, thereby improving the overall performance of the battery.
  • the BAB-type block copolymer can further improve the adhesion and liquid absorption rate of the electrode, reduce the dissolution amount of transition metals, and improve the cycle performance and high-temperature storage performance of the battery.
  • the BAB-type block copolymer can further improve the adhesion and liquid absorption rate of the electrode, reduce the dissolution amount of transition metals, and improve the cycle performance and high-temperature storage performance of the battery.
  • the BAB-type block copolymer can further improve the adhesion and liquid absorption rate of the electrode, reduce the dissolution amount of transition metals, and improve the cycle performance and high-temperature storage performance of the battery.

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Abstract

The present application provides a BAB type block copolymer, a preparation method, a binder, a positive electrode plate, a secondary battery, and an electric device. The BAB type block copolymer comprises an A-block and a B-block. The B-block comprises a structural unit represented by formula I, and the A-block comprises one or more of structural units represented by formula II, formula III and formula IV, wherein R1, R2 and R3 are each independently selected from one or more of hydrogen, fluorine, and C1-3 alkyl containing at least one fluorine atom, R4 is each independently selected from a substituted C6-25 aromatic group, and R5, R6, R7, and R8 are each independently selected from substituted or unsubstituted C2-24 alkyl, and a substituted or unsubstituted C6-25 aromatic group. The block copolymer is used as a binder, such that the film resistance of the electrode plate can be reduced, the liquid absorption rate of the electrode plate is increased, and the dissolution of transition metal in a positive electrode active material is inhibited, thereby improving the cycle performance and the storage performance of the battery.

Description

BAB型嵌段共聚物、制备方法、粘结剂、正极极片、二次电池及用电装置BAB type block copolymer, preparation method, binder, positive electrode sheet, secondary battery and electrical device
交叉引用cross reference
本申请引用于2022年9月30日递交的名称为“BAB型嵌段共聚物、制备方法、粘结剂、正极极片、二次电池及用电装置”的第202211205884.5号中国专利申请,其通过引用被全部并入本申请。This application refers to Chinese Patent Application No. 202211205884.5 filed on September 30, 2022, entitled “BAB-type block copolymer, preparation method, binder, positive electrode plate, secondary battery and electrical device”, which is incorporated into this application in its entirety by reference.
技术领域Technical Field
本申请涉及二次电池技术领域,尤其涉及一种BAB型嵌段共聚物、制备方法、粘结剂、正极极片、二次电池、电池模块、电池包和用电装置。The present application relates to the technical field of secondary batteries, and in particular to a BAB-type block copolymer, a preparation method, a binder, a positive electrode sheet, a secondary battery, a battery module, a battery pack and an electrical device.
背景技术Background technique
近年来,二次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。随着二次电池应用的普及,对其能量密度、循环性能等也提出了更高的要求。In recent years, secondary batteries have been widely used in energy storage power systems such as hydropower, thermal power, wind power and solar power stations, as well as in power tools, electric bicycles, electric motorcycles, electric vehicles, military equipment, aerospace and other fields. With the popularization of secondary battery applications, higher requirements have been put forward for their energy density and cycle performance.
粘结剂是二次电池中的常用材料,广泛应用于电池极片、隔离膜、封装处等。目前,二次电池正极中使用最广泛的粘结剂是聚偏二氟乙烯(PVDF),但其价格昂贵、分散性差,另外现有的粘结剂无法满足电池在高电压下或极端高温条件下使用、储存的需求。因此,现有的粘结剂仍有待改进。Binders are commonly used materials in secondary batteries and are widely used in battery pole pieces, separators, packaging, etc. At present, the most widely used binder in the positive electrode of secondary batteries is polyvinylidene fluoride (PVDF), but it is expensive and has poor dispersibility. In addition, existing binders cannot meet the requirements of using and storing batteries under high voltage or extremely high temperature conditions. Therefore, existing binders still need to be improved.
发明内容Summary of the invention
本申请是鉴于上述课题而进行的,其目的在于,提供一种BAB型嵌段共聚物,以该嵌段共聚物作为粘结剂能够降低极片的膜片电阻,提高极片的吸液速率,抑制正极活性材料中过渡金属的溶出,进而提高电池的循环性能和存储性能。The present application is made in view of the above-mentioned problems, and its purpose is to provide a BAB type block copolymer, which can reduce the membrane resistance of the electrode sheet, increase the liquid absorption rate of the electrode sheet, inhibit the dissolution of transition metals in the positive electrode active material, and thus improve the cycle performance and storage performance of the battery by using the block copolymer as a binder.
本申请的第一方面提供一种BAB型嵌段共聚物,包含A-嵌段和 B-嵌段,B-嵌段包含式I所示的结构单元,A-嵌段包含式II所示的结构单元、式Ⅲ所示的结构单元、式Ⅳ所示的结构单元中的一种或多种,
The first aspect of the present application provides a BAB type block copolymer comprising an A-block and B-block, B-block comprises the structural unit shown in formula I, A-block comprises one or more of the structural unit shown in formula II, the structural unit shown in formula III, and the structural unit shown in formula IV,
其中R1、R2、R3各自独立地选自氢、氟、至少含有一个氟原子的C1-3烷基中的一种或多种,R4选自取代的C6-25的芳香基,R5、R6、R7、R8各自独立地选自取代或未取代的C2-24烷基、取代或未取代的C6-25的芳香基。 R1 , R2 , R3 are each independently selected from one or more of hydrogen, fluorine, and C1-3 alkyl containing at least one fluorine atom; R4 is selected from substituted C6-25 aromatic groups; and R5 , R6 , R7 , R8 are each independently selected from substituted or unsubstituted C2-24 alkyl groups and substituted or unsubstituted C6-25 aromatic groups.
以BAB型嵌段共聚物制备的粘结剂,可以将含氟嵌段和非氟嵌段的重均分子量最大化,充分发挥含氟粘结剂和非氟粘结剂各自的优势,实现优势互补的作用。同时BAB型嵌段共聚物可以利用B-嵌段与A-嵌段间的空间位阻作用,减少粘结剂的团聚,提高极片中物质分散的均匀性。以上述BAB型嵌段共聚物制备的粘结剂能够降低极片的膜片电阻,提高极片的吸液速率,抑制正极活性材料中过渡金属的溶出,进而提高电池的循环性能和存储性能。且BAB型嵌段共聚物相比于含氟聚合物与非氟聚合物的简单共混,可以通过嵌段间的相互作用有效抑制在浆料制备过程中不同结构单元的聚合物的分层现象。 The binder prepared with the BAB type block copolymer can maximize the weight average molecular weight of the fluorine-containing block and the non-fluorine block, give full play to the respective advantages of the fluorine-containing binder and the non-fluorine binder, and achieve the role of complementary advantages. At the same time, the BAB type block copolymer can utilize the steric hindrance between the B-block and the A-block to reduce the agglomeration of the binder and improve the uniformity of the dispersion of the material in the pole piece. The binder prepared with the above-mentioned BAB type block copolymer can reduce the membrane resistance of the pole piece, increase the liquid absorption rate of the pole piece, inhibit the dissolution of the transition metal in the positive electrode active material, and thus improve the cycle performance and storage performance of the battery. And compared with the simple blending of fluorine-containing polymers and non-fluorine polymers, the BAB type block copolymer can effectively inhibit the stratification of polymers of different structural units during the slurry preparation process through the interaction between the blocks.
在任意实施方式中,所述嵌段共聚物中,每个所述B-嵌段的质量百分比为15%~35%,所述A-嵌段的质量百分比为30%~70%,基于所述嵌段共聚物的总质量计。In any embodiment, in the block copolymer, the mass percentage of each of the B-blocks is 15% to 35%, and the mass percentage of the A-block is 30% to 70%, based on the total mass of the block copolymer.
B-嵌段和A-嵌段的质量百分比在合适范围内的BAB型嵌段共聚物使得极片同时具有优异的粘结力、良好的吸液速率和较低的膜片电阻,电池具有优异的循环性能、高温存储性能和安全性能。The BAB type block copolymer with the mass percentage of B-block and A-block in a suitable range makes the electrode have excellent adhesion, good liquid absorption rate and low membrane resistance at the same time, and the battery has excellent cycle performance, high temperature storage performance and safety performance.
在任意实施方式中,所述嵌段共聚物的重均分子量为40万~200万。In any embodiment, the block copolymer has a weight average molecular weight of 400,000 to 2,000,000.
重均分子量在合适范围内的BAB型嵌段共聚物使得极片同时具有优异的吸液速率、良好的粘结力和较低的膜片电阻,电池兼具优秀的循环性能和存储性能。The BAB-type block copolymer with a weight-average molecular weight within a suitable range enables the electrode to have excellent liquid absorption rate, good adhesion and low membrane resistance, and the battery has both excellent cycle performance and storage performance.
在任意实施方式中,A-嵌段包含含有三氟甲基的式II所示的结构单元。In any embodiment, the A-block comprises a structural unit of Formula II containing a trifluoromethyl group.
在任意实施方式中,所述含有三氟甲基的式II所示的结构单元包含

In any embodiment, the structural unit represented by formula II containing a trifluoromethyl group comprises

中的一种或多种。One or more of .
A-嵌段中包含含有三氟甲基的式II所示的结构单元使得BAB型嵌段共聚物能够进一步提高极片的粘结力和吸液速率,降低极片的膜片电阻,有效抑制正极活性材料中过渡金属的溶出,提高电池的循环性能、高温存储性能和安全性能。The structural unit represented by formula II containing trifluoromethyl in the A-block enables the BAB-type block copolymer to further improve the adhesion and liquid absorption rate of the electrode, reduce the membrane resistance of the electrode, effectively inhibit the dissolution of transition metals in the positive electrode active material, and improve the cycle performance, high temperature storage performance and safety performance of the battery.
在任意实施方式中,A-嵌段包含含有砜基的式II所示的结构单元。In any embodiment, the A-block comprises a structural unit of Formula II comprising a sulfone group.
在任意实施方式中,所述含有砜基的式II所示的结构单元包含

In any embodiment, the structural unit represented by formula II containing a sulfone group comprises

中的一种或多种。One or more of .
A-嵌段中包含含有砜基的式II所示的结构单元使得BAB型嵌段共聚物能够进一步提高极片的粘结力和吸液速率,降低极片的膜片电阻,抑制正极活性材料中过渡金属的溶出,提高电池的循环性能和高温存储性能。The structural unit shown in formula II containing a sulfone group in the A-block enables the BAB-type block copolymer to further improve the adhesion and liquid absorption rate of the electrode, reduce the membrane resistance of the electrode, inhibit the dissolution of transition metals in the positive electrode active material, and improve the cycle performance and high-temperature storage performance of the battery.
在任意实施方式中,式I所示的结构单元包含衍生自偏二氟乙烯的结构单元、衍生自四氟乙烯的结构单元、衍生自氟乙烯的结构单元、衍生自三氟乙烯的结构单元、衍生自六氟丙烯的结构单元中的一种或多种。In any embodiment, the structural unit represented by Formula I comprises one or more of a structural unit derived from vinylidene fluoride, a structural unit derived from tetrafluoroethylene, a structural unit derived from vinyl fluoride, a structural unit derived from trifluoroethylene, and a structural unit derived from hexafluoropropylene.
在任意实施方式中,式II所示的结构单元包括



中的一种或多种,其中n为6-12之间的任意整数。
In any embodiment, the structural unit shown in formula II comprises



One or more of , wherein n is any integer between 6 and 12.
本申请的第二方面还提供一种BAB型嵌段共聚物的制备方法,其特征在于,包括以下步骤:The second aspect of the present application also provides a method for preparing a BAB type block copolymer, characterized in that it comprises the following steps:
制备B-嵌段:将至少一种式Ⅴ所示单体聚合制备B-嵌段,
Preparation of B-block: polymerizing at least one monomer represented by formula V to prepare B-block,
其中A1、A2、A3各自独立地选自氢、氟、至少含有一个氟原子的C1-3烷基中的一种或多种;wherein A 1 , A 2 , and A 3 are each independently selected from one or more of hydrogen, fluorine, and a C 1-3 alkyl group containing at least one fluorine atom;
制备A-嵌段:将至少一种二元胺和至少一种二元酐或至少一种二元酸聚合制备A-嵌段,或者将内酰胺单体开环聚合制备A-嵌段;Preparing the A-block: polymerizing at least one diamine and at least one dibasic anhydride or at least one dibasic acid to prepare the A-block, or ring-opening polymerizing a lactam monomer to prepare the A-block;
制备BAB型嵌段共聚物:将B-嵌段和A-嵌段接合制备BAB型嵌段共聚物。Preparation of BAB type block copolymer: B-block and A-block are joined to prepare BAB type block copolymer.
该制备方法相对于传统的共聚方法可以将含氟嵌段和非氟嵌段的重均分子量最大化,充分发挥含氟粘结剂和非氟粘结剂各自的优势,实现优势互补的作用。该制备方法原料便宜,可以降低成本,减少对环境的污染,有利于粘结剂产量的提升。同时以该方法制备的BAB型嵌段共聚物作为粘结剂,能够使得极片具有优秀的吸液能 力、良好的粘结力,较低的膜片电阻,使得电池的循环性能、高温存储性能和安全性能得到改善。Compared with the traditional copolymerization method, this preparation method can maximize the weight average molecular weight of the fluorine-containing block and the non-fluorine block, give full play to the advantages of the fluorine-containing binder and the non-fluorine binder, and achieve the role of complementary advantages. The preparation method has cheap raw materials, can reduce costs, reduce environmental pollution, and is conducive to the increase of binder production. At the same time, the BAB type block copolymer prepared by this method as a binder can make the electrode have excellent liquid absorption ability. The good adhesion, low membrane resistance and the cycle performance, high temperature storage performance and safety performance of the battery are improved.
在任意实施方式中,所述制备B-嵌段具体包括:In any embodiment, the preparation of the B-block specifically comprises:
将至少一种式Ⅴ所示单体、链转移剂和引发剂在70~90℃的反应温度下通过可逆加成-裂解链转移聚合,反应5~8.5小时得到单端具有叠氮基团或炔基的B-嵌段。At least one monomer represented by formula V, a chain transfer agent and an initiator are subjected to reversible addition-fragmentation chain transfer polymerization at a reaction temperature of 70 to 90° C. for 5 to 8.5 hours to obtain a B-block having an azide group or an alkynyl group at one end.
采用可逆加成-裂解链转移聚合实现可控聚合,且产物分子量分布较窄。而且通过上述反应,B-嵌段只在末端具有炔基或叠氮基团,方便以高效温和的方式定向地与A-嵌段发生接合,生成BAB型三嵌段共聚物。Reversible addition-fragmentation chain transfer polymerization is used to achieve controlled polymerization, and the molecular weight distribution of the product is relatively narrow. Moreover, through the above reaction, the B-block only has an alkynyl or azide group at the end, which is convenient for directing and bonding with the A-block in an efficient and mild manner to generate a BAB-type triblock copolymer.
在任意实施方式中,所述制备A-嵌段具体包括:In any embodiment, the preparation of the A-block specifically comprises:
将催化剂、至少一种二元胺、至少一种二元酐或至少一种二元酸在室温下搅拌反应4~10小时,升温至170~210℃反应5~20小时,得到两端的端基均为酸酐、羧基或氨基的产物;The catalyst, at least one diamine, at least one dibasic anhydride or at least one dibasic acid are stirred and reacted at room temperature for 4 to 10 hours, and the temperature is raised to 170 to 210° C. and reacted for 5 to 20 hours to obtain a product with both end groups being anhydride, carboxyl or amino groups;
对产物的端基进行官能化反应,得到两端均具有炔基或叠氮基团的所述A-嵌段。The terminal groups of the product are subjected to functionalization reaction to obtain the A-block having alkynyl groups or azide groups at both ends.
在任意实施方式中,所述制备A-嵌段具体包括:In any embodiment, the preparation of the A-block specifically comprises:
将端基调节剂、水和至少一种内酰胺单体在250℃~280℃的反应温度下聚合反应12~24小时,得到两端的端基均为羧基或氨基的产物;Polymerizing an end group regulator, water and at least one lactam monomer at a reaction temperature of 250° C. to 280° C. for 12 to 24 hours to obtain a product having end groups at both ends being carboxyl groups or amino groups;
对产物的端基进行官能化反应,得到两端均具有炔基或叠氮基团的所述A-嵌段。The terminal groups of the product are subjected to functionalization reaction to obtain the A-block having alkynyl groups or azide groups at both ends.
采用该制备方法制备出的两侧末端叠氮化或炔基化的A-嵌段,便于以高效温和的方式与B-嵌段发生嵌段间的连接,生成BAB型嵌段共聚物。The A-block with azidation or alkyne at both ends prepared by the preparation method can be easily connected with the B-block in an efficient and mild manner to generate a BAB type block copolymer.
在任意实施方式中,所述制备BAB型嵌段共聚物具体包括:In any embodiment, the preparation of the BAB type block copolymer specifically comprises:
将两端均具有炔基或叠氮基团的A-嵌段与单端具有叠氮基团或炔基的B-嵌段混合,进行点击反应,制备BAB型嵌段共聚物,其中B-嵌段和A-嵌段的端基不同。The A-block having alkynyl or azide groups at both ends is mixed with the B-block having an azide or alkyne group at one end and subjected to a click reaction to prepare a BAB type block copolymer, wherein the end groups of the B-block and the A-block are different.
上述制备方法,具有产率高、副产物无害、反应条件简单温和、 反应原料易得的优点,能够实现嵌段聚合物的可控聚合,有利于提高产品的良品率。The above preparation method has the advantages of high yield, harmless by-products, simple and mild reaction conditions, The advantage of readily available reaction raw materials can achieve controlled polymerization of block polymers, which is beneficial to improving the yield rate of products.
在任意实施方式中,链转移剂为含末端炔基或叠氮基团的RAFT链转移剂。In any embodiment, the chain transfer agent is a RAFT chain transfer agent containing a terminal alkynyl or azide group.
在任意实施方式中,端基调节剂为二元胺或二元酸。In any embodiment, the end group modifier is a diamine or a dibasic acid.
本申请的第三方面,提供一种BAB型嵌段共聚物在二次电池中的应用,可选地,二次电池包括锂离子电池、钠离子电池、镁离子电池、钾离子电池中的至少一种。The third aspect of the present application provides an application of a BAB type block copolymer in a secondary battery. Optionally, the secondary battery includes at least one of a lithium ion battery, a sodium ion battery, a magnesium ion battery, and a potassium ion battery.
本申请的第四方面提供一种正极极片,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,所述正极膜层包括正极活性材料、导电剂和粘结剂,该粘结剂为任意实施方式中的BAB型嵌段共聚物或任意实施方式中的制备方法制备的BAB型嵌段共聚物。The fourth aspect of the present application provides a positive electrode plate, including a positive electrode current collector and a positive electrode film layer arranged on at least one surface of the positive electrode current collector, wherein the positive electrode film layer includes a positive electrode active material, a conductive agent and a binder, and the binder is a BAB type block copolymer in any embodiment or a BAB type block copolymer prepared by the preparation method in any embodiment.
该正极极片具有优异的吸液速率和良好的粘结力,具有优异的膜片电阻和过渡金属溶出量。The positive electrode sheet has excellent liquid absorption rate and good bonding force, and has excellent membrane resistance and transition metal dissolution amount.
在任意实施方式中,粘结剂的质量百分比为0.1%~3%,基于正极活性材料的总质量计。In any embodiment, the binder has a mass percentage of 0.1% to 3% based on the total mass of the positive electrode active material.
控制粘结剂的质量百分比在合适范围内,可以使得极片具有优异的吸液速率、良好的粘结力、较低的膜片电阻。另外极片中的粘结剂能够抑制活性材料中过渡金属的溶出,提高电池的循环性能、高温存储性能和安全性能。Controlling the mass percentage of the binder within a suitable range can make the pole piece have excellent liquid absorption rate, good bonding force, and low membrane resistance. In addition, the binder in the pole piece can inhibit the dissolution of transition metals in the active material, and improve the cycle performance, high temperature storage performance and safety performance of the battery.
在任意实施方式中,所述正极膜层与所述正极集流体间单位长度的粘结力不小于11.5N/m,可选为11.5-15N/m。In any embodiment, the bonding force per unit length between the positive electrode film layer and the positive electrode current collector is not less than 11.5 N/m, and can be 11.5-15 N/m.
该极片的正极膜层与正极集流体之间具有高的粘结强度,在使用过程中,正极膜层不容易从正极集流体上脱落,有助于提高电池的循环性能和安全性。The positive electrode film layer of the pole piece has high bonding strength with the positive electrode current collector. During use, the positive electrode film layer is not easy to fall off from the positive electrode current collector, which helps to improve the cycle performance and safety of the battery.
在任意实施方式中,所述正极极片对电解液的吸液速率大于0.31μg/s,可选为0.32-0.5μg/s,所述电解液的密度为1.1-1.2g/cm3In any embodiment, the electrolyte absorption rate of the positive electrode plate is greater than 0.31 μg/s, and may be 0.32-0.5 μg/s, and the electrolyte has a density of 1.1-1.2 g/cm 3 .
该极片具有较高的吸液速率,能够提高电解液对极片的浸润效率,改善离子传输路径,降低界面电阻,提高电池性能。The electrode has a high liquid absorption rate, which can improve the electrolyte infiltration efficiency of the electrode, improve the ion transmission path, reduce the interface resistance, and improve the battery performance.
在本申请的第五方面,提供一种二次电池,包括电极组件和电 解液,所述电极组件包括隔离膜、负极极片和本申请第四方面的正极极片。In a fifth aspect of the present application, a secondary battery is provided, comprising an electrode assembly and an The electrolyte is provided, and the electrode assembly comprises a separator, a negative electrode plate and a positive electrode plate according to the fourth aspect of the present application.
在本申请的第六方面,提供一种用电装置,包括本申请第五方面的二次电池。In a sixth aspect of the present application, an electrical device is provided, comprising the secondary battery of the fifth aspect of the present application.
附图说明BRIEF DESCRIPTION OF THE DRAWINGS
图1是本申请一实施方式的BAB型嵌段共聚物的制备方法示意图;FIG1 is a schematic diagram of a method for preparing a BAB type block copolymer according to an embodiment of the present application;
图2是本申请一实施方式的二次电池的示意图;FIG2 is a schematic diagram of a secondary battery according to an embodiment of the present application;
图3是图2所示的本申请一实施方式的二次电池的分解图;FIG3 is an exploded view of the secondary battery of one embodiment of the present application shown in FIG2 ;
图4是本申请一实施方式的电池模块的示意图;FIG4 is a schematic diagram of a battery module according to an embodiment of the present application;
图5是本申请一实施方式的电池包的示意图;FIG5 is a schematic diagram of a battery pack according to an embodiment of the present application;
图6是图5所示的本申请一实施方式的电池包的分解图;FIG6 is an exploded view of the battery pack according to an embodiment of the present application shown in FIG5 ;
图7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。FIG. 7 is a schematic diagram of an electric device using a secondary battery as a power source according to an embodiment of the present application.
附图标记说明:Description of reference numerals:
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盖板;6BAB型嵌段共聚物;61A-嵌段;611A-嵌段的两端基团;612式II、式III或式IV所示结构单元;62B-嵌段;621B-嵌段的末端基团;622式I所示结构单元。1 battery pack; 2 upper box; 3 lower box; 4 battery module; 5 secondary battery; 51 shell; 52 electrode assembly; 53 cover plate; 6BAB type block copolymer; 61A-block; 611A-terminal groups of the block; 612 structural unit shown in formula II, formula III or formula IV; 62B-block; 621B-terminal groups of the block; 622 structural unit shown in formula I.
具体实施方式Detailed ways
以下,适当地参照附图详细说明具体公开了本申请的正极活性材料及其制造方法、正极极片、二次电池、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。Below, the embodiments of the positive electrode active material and its manufacturing method, positive electrode sheet, secondary battery, battery module, battery pack and electrical device of the present application are specifically disclosed with appropriate reference to the drawings. However, there are cases where unnecessary detailed descriptions are omitted. For example, there are cases where detailed descriptions of well-known matters and repeated descriptions of actually the same structure are omitted. This is to avoid the following description from becoming unnecessarily lengthy and to facilitate the understanding of those skilled in the art. In addition, the drawings and the following descriptions are provided for those skilled in the art to fully understand the present application and are not intended to limit the subject matter described in the claims.
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。The "range" disclosed in this application is defined in the form of a lower limit and an upper limit. It is defined by selecting a lower limit and an upper limit, and the selected lower limit and upper limit define the boundary of a special range. The scope defined in this way can include or exclude end values, and can be arbitrarily combined, that is, any lower limit can form a scope with any upper limit combination. For example, if the scope of 60-120 and 80-110 is listed for a specific parameter, it is understood that the scope of 60-110 and 80-120 is also expected. In addition, if the minimum range values 1 and 2 listed, and if the maximum range values 3, 4 and 5 are listed, the following scope can be all expected: 1-3, 1-4, 1-5, 2-3, 2-4 and 2-5. In this application, unless otherwise specified, the numerical range "ab" represents the abbreviation of any real number combination between a and b, wherein a and b are real numbers. For example, the numerical range "0-5" represents that all real numbers between "0-5" have been fully listed herein, and "0-5" is just the abbreviation of these numerical combinations. In addition, when a parameter is expressed as an integer ≥ 2, it is equivalent to disclosing that the parameter is, for example, an integer of 2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12, etc.
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。Unless otherwise specified, all embodiments and optional embodiments of the present application can be combined with each other to form a new technical solution.
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。Unless otherwise specified, all technical features and optional technical features of this application can be combined with each other to form a new technical solution.
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。If there is no special explanation, all steps of the present application can be performed sequentially or randomly, preferably sequentially. For example, the method includes steps (a) and (b), which means that the method may include steps (a) and (b) performed sequentially, or may include steps (b) and (a) performed sequentially. For example, the method may further include step (c), which means that step (c) may be added to the method in any order. For example, the method may include steps (a), (b) and (c), or may include steps (a), (c) and (b), or may include steps (c), (a) and (b), etc.
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。If there is no special explanation, the "include" and "comprising" mentioned in this application represent open-ended or closed-ended expressions. For example, the "include" and "comprising" may represent that other components not listed may also be included or only the listed components may be included or only the listed components may be included.
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)。If not specifically stated, in this application, the term "or" is inclusive. For example, the phrase "A or B" means "A, B, or both A and B". More specifically, any of the following conditions satisfies the condition "A or B": A is true (or exists) and B is false (or exists). A is false (or does not exist) and B is true (or exists); or both A and B are true (or exist).
现有技术中常以聚偏氟乙烯(PVDF)作为极片粘结剂,然而PVDF粘结剂的成本高,受环保政策的限制无法大规模回收利用。而且PVDF粘结剂难以对正极活性材料形成有效的保护层,无法有效抑制正极活性材料与电解液的副反应以及正极活性材料中过渡金属的溶出,导致电芯产气、体积变形、过渡金属在负极沉积等问题,对电池的循环性能和安全性能均产生负面影响,In the prior art, polyvinylidene fluoride (PVDF) is often used as a pole piece binder. However, the cost of PVDF binder is high and it cannot be recycled on a large scale due to restrictions of environmental protection policies. Moreover, PVDF binder is difficult to form an effective protective layer for the positive electrode active material, and cannot effectively inhibit the side reaction between the positive electrode active material and the electrolyte and the dissolution of transition metals in the positive electrode active material, resulting in problems such as gas generation, volume deformation, and deposition of transition metals at the negative electrode of the battery cell, which have a negative impact on the cycle performance and safety performance of the battery.
[粘结剂][Binder]
基于此,本申请提供了一种BAB型嵌段共聚物,包含A-嵌段和B-嵌段,B-嵌段包含式I所示的结构单元,A-嵌段包含式II所示的结构单元、式Ⅲ所示的结构单元、式Ⅳ所示的结构单元中的一种或多种,
Based on this, the present application provides a BAB type block copolymer, comprising an A-block and a B-block, wherein the B-block comprises a structural unit shown in formula I, and the A-block comprises one or more of a structural unit shown in formula II, a structural unit shown in formula III, and a structural unit shown in formula IV.
其中R1、R2、R3各自独立地选自氢、氟、至少含有一个氟原子的C1-3烷基中的一种或多种,R4选自取代的C6-25的芳香基,R5、R6、R7、R8各自独立地选自取代或未取代的C2-24烷基、取代或未取代的C6-25的芳香基。 R1 , R2 , R3 are each independently selected from one or more of hydrogen, fluorine, and C1-3 alkyl containing at least one fluorine atom; R4 is selected from substituted C6-25 aromatic groups; and R5 , R6 , R7 , R8 are each independently selected from substituted or unsubstituted C2-24 alkyl groups and substituted or unsubstituted C6-25 aromatic groups.
在本文中,术语“嵌段共聚物”是将两种或两种以上性质不同的聚合物链段连在一起制备而成的一种特殊聚合物。具有特定结构的嵌段聚合物会表现出与简单线形聚合物,以及许多无规共聚物甚至均聚物的混合物不同的性质。常见的有AB型和BAB型,其中A、B都是长链段;也有(AB)n型多段共聚物,其中A、B链段相对较短。In this article, the term "block copolymer" refers to a special type of polymer made by linking two or more polymer segments with different properties. Block polymers with specific structures will exhibit different properties from simple linear polymers, many random copolymers, and even mixtures of homopolymers. Common types include AB and BAB types, in which A and B are both long chain segments; there are also (AB)n type multi-segment copolymers, in which A and B segments are relatively short.
在本文中,术语“BAB型嵌段共聚物”是指中间为A-嵌段,两侧为B-嵌段的三嵌段共聚物。其中,B-嵌段和A-嵌段分别是由不同的单体聚合形成的具有预定聚合度的聚合物链段。在一些实施方式中,B-嵌段是由一种或多种含氟单体聚合形成的长序列链段,A-嵌段是由一种或多种不含氟单体聚合形成的长序列链段。B-嵌段和A-嵌段以有序的方式经共价键结合形成BAB型嵌段共聚物。作为示例,BAB型嵌段聚合物中B-嵌段为聚偏二氟乙烯,由偏氟乙烯单体聚合形成,重均分子量为10万-50万;A-嵌段为聚酰亚胺,由二酐单体和二胺单体聚合形成,重均分子量为20万-100万;B-嵌段和A-嵌段嵌段两侧的端基键合得到聚偏氟乙烯-聚酰亚胺-聚偏氟乙烯嵌段共聚物(BAB型嵌段共聚物),该嵌段共聚物的重均分子量为40万-200万。In this article, the term "BAB type block copolymer" refers to a triblock copolymer with an A-block in the middle and B-blocks on both sides. Wherein, the B-block and the A-block are polymer segments with a predetermined degree of polymerization formed by polymerization of different monomers. In some embodiments, the B-block is a long sequence segment formed by polymerization of one or more fluorine-containing monomers, and the A-block is a long sequence segment formed by polymerization of one or more fluorine-free monomers. The B-block and the A-block are covalently bonded in an orderly manner to form a BAB type block copolymer. As an example, in the BAB type block polymer, the B-block is polyvinylidene fluoride, which is formed by the polymerization of vinylidene fluoride monomers, and has a weight average molecular weight of 100,000-500,000; the A-block is polyimide, which is formed by the polymerization of dianhydride monomers and diamine monomers, and has a weight average molecular weight of 200,000-1,000,000; the end groups on both sides of the B-block and the A-block are bonded to obtain a polyvinylidene fluoride-polyimide-polyvinylidene fluoride block copolymer (BAB type block copolymer), and the weight average molecular weight of the block copolymer is 400,000-2,000,000.
在本文中,术语“聚合物”一方面包括通过聚合反应制备的化学上均一的、但在聚合度、摩尔质量和链长方面不同的大分子的集合体。该术语另一方面也包括由聚合反应形成的这样的大分子集合体的衍生物,即可以通过上述大分子中的官能团的反应,例如加成或取代获得的并且可以是化学上均一的或化学上不均一的化合物。In this context, the term "polymer" includes, on the one hand, a collection of macromolecules that are chemically uniform but differ in degree of polymerization, molar mass and chain length, prepared by polymerization. The term also includes, on the other hand, derivatives of such a collection of macromolecules formed by polymerization, i.e. compounds that can be obtained by reaction, for example addition or substitution, of functional groups in the above-mentioned macromolecules and can be chemically uniform or chemically heterogeneous.
在本文中,术语“C1-3烷基”是指仅由碳和氢原子组成的直链或支链烃链基团,基团中不存在不饱和,具有从一至三个碳原子,并且通过单键附接到分子的其余部分。C1-3烷基的示例包括但不限于:甲基、乙基、正丙基、1-甲基乙基(异丙基)。术语“C2-C24烷基”应作相应解释。As used herein, the term "C 1-3 alkyl" refers to a straight or branched hydrocarbon chain radical consisting solely of carbon and hydrogen atoms, with no unsaturation in the radical, having from one to three carbon atoms, and attached to the remainder of the molecule by a single bond. Examples of C 1-3 alkyl include, but are not limited to, methyl, ethyl, n-propyl, 1-methylethyl (isopropyl). The term "C 2 -C 24 alkyl" should be interpreted accordingly.
在本文中,术语“至少含有一个氟原子的C1-3烷基”是指至少有一个H原子被F原子取代的含有1-3个碳原子的烷基。在一些实 施方式中,含有一个氟原子的C1-3烷基包括-CF3基团、-C2F6基团。In this context, the term "C 1-3 alkyl containing at least one fluorine atom" refers to an alkyl group containing 1 to 3 carbon atoms in which at least one H atom is replaced by a F atom. In the embodiment, the C 1-3 alkyl group containing one fluorine atom includes a -CF 3 group and a -C 2 F 6 group.
在本文中,术语“取代的”是指该化合物或化学部分的至少一个氢原子被另一种化学部分被取代基取代,其中的取代基各自独立地选自:羟基、巯基、氨基、氰基、硝基、醛基、卤素原子、烯基、炔基、芳基、杂芳基、C1-6烷基、C1-6烷氧基。As used herein, the term "substituted" means that at least one hydrogen atom of the compound or chemical moiety is replaced by another chemical moiety with a substituent, wherein the substituent is independently selected from: hydroxyl, thiol, amino, cyano, nitro, aldehyde, halogen atom, alkenyl, alkynyl, aryl, heteroaryl, C 1-6 alkyl, C 1-6 alkoxy.
在本文中,术语“C6-25的芳香基”,指至少一个环为芳族的芳族环系统,其包括但不限于苯基、联苯基、茚满基、1-萘基、2-萘基和四氢萘基。As used herein, the term "C 6-25 aromatic group" refers to an aromatic ring system in which at least one ring is aromatic, including but not limited to phenyl, biphenyl, indanyl, 1-naphthyl, 2-naphthyl and tetrahydronaphthyl.
在本文中,取代的C6-25的芳香基包括但不限于芳烷基、芳烷氧基、芳基氧基烷基、通过羰基或醚基连接的对称或不对称芳基基团。Herein, the substituted C 6-25 aromatic group includes, but is not limited to, aralkyl, aralkyloxy, aryloxyalkyl, and a symmetrical or asymmetrical aromatic group linked via a carbonyl group or an ether group.
在一些实施方式中,式I所示的结构单元包含衍生自偏二氟乙烯的结构单元、衍生自四氟乙烯的结构单元、衍生自氟乙烯的结构单元、衍生自三氟乙烯的结构单元、衍生自六氟丙烯的结构单元中的一种或多种。In some embodiments, the structural unit represented by Formula I comprises one or more of a structural unit derived from vinylidene fluoride, a structural unit derived from tetrafluoroethylene, a structural unit derived from vinyl fluoride, a structural unit derived from trifluoroethylene, and a structural unit derived from hexafluoropropylene.
在一些实施方式中,式II所示的结构单元包含



中的一种或多种,其中n为6-12之间的任意整数。
In some embodiments, the structural unit shown in Formula II comprises



One or more of , wherein n is any integer between 6 and 12.
在一些实施方式中,式Ⅲ所示的结构单元包含

In some embodiments, the structural unit represented by formula III comprises

在一些实施方式中,式Ⅳ所示结构单元包含
In some embodiments, the structural unit represented by formula IV comprises
在一些实施方式中,BAB型嵌段共聚物在二次电池中作为粘结剂。在一些实施方式中,BAB型嵌段共聚物在二次电池中作为极片粘结剂。In some embodiments, the BAB type block copolymer is used as a binder in a secondary battery. In some embodiments, the BAB type block copolymer is used as a pole piece binder in a secondary battery.
在本文中,术语“粘结剂”是指在分散介质中形成胶体溶液或胶体分散液的化学化合物、聚合物或混合物。As used herein, the term "binder" refers to a chemical compound, polymer or mixture that forms a colloidal solution or colloidal dispersion in a dispersion medium.
在一些实施方式中,粘结剂的分散介质是水性溶剂,如水。即粘结剂溶解于水性溶剂中。In some embodiments, the dispersion medium of the binder is an aqueous solvent, such as water, that is, the binder is dissolved in the aqueous solvent.
在一些实施方式中,粘结剂的分散介质是油性溶剂,油性溶剂的示例包括但不限于二甲基乙酰胺、N,N-二甲基甲酰胺、N-甲基吡咯烷酮、丙酮、碳酸二甲酯、乙基纤维素、聚碳酸酯。即,粘结剂 溶解于油性溶剂中。In some embodiments, the dispersion medium of the binder is an oily solvent, and examples of the oily solvent include but are not limited to dimethylacetamide, N,N-dimethylformamide, N-methylpyrrolidone, acetone, dimethyl carbonate, ethyl cellulose, and polycarbonate. Soluble in oily solvents.
在一些实施方式中,粘结剂用于将电极材料及/或导电剂固定在合适位置并将它们粘附在导电金属部件以形成电极。In some embodiments, a binder is used to hold the electrode material and/or the conductive agent in place and adhere them to the conductive metal part to form an electrode.
在一些实施方式中,粘结剂作为正极粘结剂,用于粘结正极活性材料及/或导电剂以形成电极。In some embodiments, the binder is used as a positive electrode binder to bind the positive electrode active material and/or the conductive agent to form an electrode.
在一些实施方式中,粘结剂作为负极粘结剂,用于粘结负极活性材料及/或导电剂以形成电极。In some embodiments, the binder is used as a negative electrode binder to bind the negative electrode active material and/or the conductive agent to form an electrode.
B-嵌段含有的氟元素与正极活性材料表面及集流体表面的羟基和羧基形成氢键作用,使得极片具有优异的粘结力。A-嵌段中含有丰富的羰基,可以形成分子间氢键,氢键与正极活性材料表面及集流体表面的羟基形成相互作用,使得极片具有优异的粘结力,提高正极极片的稳定性,另外丰富的羰基使得粘结剂具有优异的柔韧性,减轻在充放电过程中随着极片体积变化而发生的活性物质的脱落情况,从而提高电池的循环容量保持率。The fluorine contained in the B-block forms hydrogen bonds with the hydroxyl and carboxyl groups on the surface of the positive electrode active material and the current collector, making the pole piece have excellent adhesion. The A-block contains abundant carbonyl groups, which can form intermolecular hydrogen bonds. The hydrogen bonds interact with the hydroxyl groups on the surface of the positive electrode active material and the current collector, making the pole piece have excellent adhesion and improving the stability of the positive electrode. In addition, the abundant carbonyl groups make the binder have excellent flexibility, reducing the shedding of active materials that occurs as the pole piece volume changes during the charge and discharge process, thereby improving the battery's cycle capacity retention rate.
在一些实施方式中,A-嵌段至少包含式II所示的结构单元。In some embodiments, the A-block comprises at least the structural unit represented by Formula II.
A-嵌段中含有的酰亚胺键,能够提高极片的吸液能力,改善极片对电解液的浸润能力,有助于导电网络的形成,降低极片的膜片电阻。另外强极性的酰亚胺键,可以提高粘结剂的电化学稳定性和热稳定性,有效地抑制极片由于电化学反应过程中离子的嵌入和脱出所引发的物理膨胀。同时含有酰亚胺键的A-嵌段的表面能相对较低,成膜性能好,能够均匀地包覆在正极活性材料表面,减少正极活性材料表面的活性位点,降低副反应和过渡金属的溶出,从而提高电极的循环性能、高温存储性能,减少电池在高温下的产气量。The imide bond contained in the A-block can improve the liquid absorption capacity of the electrode, improve the electrode's ability to infiltrate the electrolyte, help form a conductive network, and reduce the film resistance of the electrode. In addition, the highly polar imide bond can improve the electrochemical stability and thermal stability of the binder, and effectively inhibit the physical expansion of the electrode caused by the insertion and extraction of ions during the electrochemical reaction. At the same time, the surface energy of the A-block containing the imide bond is relatively low, and the film-forming performance is good. It can be evenly coated on the surface of the positive electrode active material, reducing the active sites on the surface of the positive electrode active material, reducing side reactions and the dissolution of transition metals, thereby improving the cycle performance and high-temperature storage performance of the electrode, and reducing the gas production of the battery at high temperature.
在一些实施方式中,A-嵌段至少包含式III或式IV所示的结构单元。In some embodiments, the A-block comprises at least a structural unit represented by Formula III or Formula IV.
A-嵌段中含有的酰胺键,能够提高极片的吸液能力,改善极片对电解液的浸润能力,有助于导电网络的形成,降低极片的膜片电阻,另外强极性的酰胺键,可以提高粘结剂的电化学稳定性和热稳定性,有效地抑制极片由于电化学反应过程中离子的嵌入和脱出所引发的物理膨胀。同时当粘结剂包覆在活性材料的表面时,能够降 低活性材料与电解液的副反应,抑制活性材料中过渡金属的溶出,从而提高电极的循环性能、高温存储性能和产气性能。The amide bond contained in the A-block can improve the liquid absorption capacity of the electrode, improve the electrode's ability to infiltrate the electrolyte, help form a conductive network, and reduce the film resistance of the electrode. In addition, the strong polar amide bond can improve the electrochemical stability and thermal stability of the binder, and effectively inhibit the physical expansion of the electrode caused by the insertion and extraction of ions during the electrochemical reaction. At the same time, when the binder is coated on the surface of the active material, it can reduce The side reaction between the low-activity material and the electrolyte inhibits the dissolution of transition metals in the active material, thereby improving the cycle performance, high-temperature storage performance and gas production performance of the electrode.
以BAB型嵌段共聚物制备的粘结剂,可以将含氟嵌段和非氟嵌段的重均分子量最大化,充分发挥含氟粘结剂和非氟粘结剂各自的优势,实现优势互补的作用。同时BAB型嵌段共聚物可以利用B-嵌段与A-嵌段间的空间位阻作用,减少粘结剂的团聚,提高极片中物质分散的均匀性。以上述BAB型嵌段共聚物制备的粘结剂能够降低极片的膜片电阻,提高极片的吸液速率,抑制正极活性材料中过渡金属的溶出,进而提高电池的循环性能和存储性能。且BAB型嵌段共聚物相比于含氟聚合物与非氟聚合物的简单共混,可以通过嵌段间的相互作用有效抑制在浆料制备过程中不同结构单元的聚合物的分层现象。The binder prepared with the BAB type block copolymer can maximize the weight average molecular weight of the fluorine-containing block and the non-fluorine block, give full play to the respective advantages of the fluorine-containing binder and the non-fluorine binder, and achieve the role of complementary advantages. At the same time, the BAB type block copolymer can utilize the steric hindrance between the B-block and the A-block to reduce the agglomeration of the binder and improve the uniformity of the dispersion of the material in the pole piece. The binder prepared with the above-mentioned BAB type block copolymer can reduce the membrane resistance of the pole piece, increase the liquid absorption rate of the pole piece, inhibit the dissolution of the transition metal in the positive electrode active material, and thus improve the cycle performance and storage performance of the battery. And compared with the simple blending of fluorine-containing polymers and non-fluorine polymers, the BAB type block copolymer can effectively inhibit the stratification of polymers of different structural units during the slurry preparation process through the interaction between the blocks.
在一些实施方式中,嵌段共聚物中,每个B-嵌段的质量百分比为15%~35%,A-嵌段的质量百分比为30%~70%,基于嵌段共聚物的总质量计。In some embodiments, in the block copolymer, the mass percentage of each B-block is 15% to 35%, and the mass percentage of the A-block is 30% to 70%, based on the total mass of the block copolymer.
在一些实施方式中,嵌段共聚物中,每个B-嵌段的质量百分比可选为15%、18%、20%、23%、25%、28%、30%、32%、35%中的任意一种,基于嵌段共聚物的总质量计。In some embodiments, the mass percentage of each B-block in the block copolymer can be selected as any one of 15%, 18%, 20%, 23%, 25%, 28%, 30%, 32%, and 35%, based on the total mass of the block copolymer.
在一些实施方式中,嵌段共聚物中,A-嵌段的质量百分比可选为30%、35%、40%、45%、50%、55%、60%、65%、70%中的任意一种,基于嵌段共聚物的总质量计。In some embodiments, in the block copolymer, the mass percentage of the A-block may be any one of 30%, 35%, 40%, 45%, 50%, 55%, 60%, 65%, and 70%, based on the total mass of the block copolymer.
若B-嵌段的质量百分比过高,A-嵌段的质量百分比过低,无法充分发挥A-嵌段提高吸液速率、降低膜片电阻、抑制活性材料中过渡金属溶出的作用,无法有效提高电池的循环性能和安全性能;若B-嵌段的质量百分比过低,A-嵌段的质量百分比过高,极片的粘结力和电池的循环稳定性会有所下降。If the mass percentage of the B-block is too high and the mass percentage of the A-block is too low, the A-block cannot fully exert its role in increasing the liquid absorption rate, reducing the membrane resistance, and inhibiting the dissolution of transition metals in the active material, and the battery's cycle performance and safety performance cannot be effectively improved; if the mass percentage of the B-block is too low and the mass percentage of the A-block is too high, the bonding strength of the electrode and the cycle stability of the battery will be reduced.
B-嵌段和A-嵌段的质量百分比在合适范围内的BAB型嵌段共聚物使得极片同时具有优异的粘结力、良好的吸液速率和较低的膜片电阻,电池具有优异的循环性能、高温存储性能和安全性能。The BAB type block copolymer with the mass percentage of B-block and A-block in a suitable range makes the electrode have excellent adhesion, good liquid absorption rate and low membrane resistance at the same time, and the battery has excellent cycle performance, high temperature storage performance and safety performance.
在一些实施方式中,BAB型嵌段共聚物的重均分子量为40万 ~200万。在一些实施方式中,BAB型嵌段共聚物的重均分子量可选为40万~60万、60万~80万、80万~100万、100万~120万、120万~140万、140万~160万、160万~180万、180万~200万、60万~90万、90万~120万、120万~150万、150万~180万、120万~200万中的任意一种。In some embodiments, the weight average molecular weight of the BAB type block copolymer is 400,000 In some embodiments, the weight average molecular weight of the BAB type block copolymer can be selected from any one of 400,000 to 600,000, 600,000 to 800,000, 800,000 to 1,000,000, 1,000,000 to 1,200,000, 1,200,000 to 1,400,000, 1,400,000 to 1,600,000, 1,600,000 to 1,800,000, 1,800,000 to 2,000,000, 600,000 to 900,000, 900,000 to 1,200,000, 1,200,000 to 1,500,000, 1,500,000 to 1,800,000, and 1,200,000 to 2,000,000.
在本文中,术语“重均分子量”是指聚合物中用不同分子量的分子所占的重量分数与其对应的分子量乘积的总和。As used herein, the term "weight average molecular weight" refers to the sum of the products of the weight fractions of molecules with different molecular weights in a polymer and their corresponding molecular weights.
若BAB型嵌段共聚物的重均分子量过大,粘结剂溶解困难,易与导电剂团聚,导致浆料的粘度过大,难以涂布均匀,不利于后续极片的加工生产。若BAB型嵌段共聚物的重均分子量过小,难以形成三维网状粘结结构,无法起到有效的粘结和分散作用,不利于导电网络的形成,导致极片的膜片电阻增大,电池的循环性能、高温存储性能和产气性能下降。If the weight average molecular weight of the BAB type block copolymer is too large, the binder is difficult to dissolve and is easy to agglomerate with the conductive agent, resulting in excessive viscosity of the slurry, making it difficult to apply evenly, which is not conducive to the subsequent processing and production of the pole piece. If the weight average molecular weight of the BAB type block copolymer is too small, it is difficult to form a three-dimensional network bonding structure, and it cannot play an effective bonding and dispersion role, which is not conducive to the formation of a conductive network, resulting in an increase in the membrane resistance of the pole piece, and a decrease in the battery's cycle performance, high-temperature storage performance, and gas production performance.
重均分子量在合适范围内的BAB型嵌段共聚物使得极片同时具有优异的吸液速率、良好的粘结力和较低的膜片电阻,电池兼具优秀的循环性能和存储性能。The BAB-type block copolymer with a weight-average molecular weight within a suitable range enables the electrode to have excellent liquid absorption rate, good adhesion and low membrane resistance, and the battery has both excellent cycle performance and storage performance.
在一些实施方式中,A-嵌段包含含有三氟甲基的式II所示的结构单元。In some embodiments, the A-block comprises a structural unit of Formula II containing a trifluoromethyl group.
在一些实施方式中,所述含有三氟甲基的式II所示的结构单元包含

In some embodiments, the structural unit represented by formula II containing a trifluoromethyl group comprises

中的一种或多种。One or more of .
在本文中,术语“三氟甲基”指的是“-CF3”基团。As used herein, the term "trifluoromethyl" refers to a " -CF3 " group.
在本文中,术语“砜基”指的是“-SO2-”基团。As used herein, the term "sulfone" refers to a " -SO2- " group.
在本文中,术语“醚键”是指“-O-”。As used herein, the term "ether bond" refers to "-O-".
A-嵌段中包含含有三氟甲基的式II所示的结构单元可以增强粘结剂的离子转移能力,改善极片的吸液速率,降低极片的膜片电阻,同时三氟甲基中的氟元素可以与活性材料及集流体表面残留的羧基、羟基形成氢键以进一步提高粘结剂的粘结力。另外A-嵌段中包含三氟甲基基团可以提高粘结剂的电化学稳定性、热稳定性,抑制正极活性材料中过渡金属的溶出,有效地抑制极片由于电化学反应过程中离子的嵌入和脱出所引发的物理膨胀,提高电池的循环性能、高温存储性能和产气性能。The structural unit shown in Formula II containing trifluoromethyl in the A-block can enhance the ion transfer ability of the binder, improve the liquid absorption rate of the pole piece, and reduce the membrane resistance of the pole piece. At the same time, the fluorine element in the trifluoromethyl group can form hydrogen bonds with the carboxyl and hydroxyl groups remaining on the surface of the active material and the current collector to further improve the bonding force of the binder. In addition, the trifluoromethyl group in the A-block can improve the electrochemical stability and thermal stability of the binder, inhibit the dissolution of transition metals in the positive electrode active material, effectively inhibit the physical expansion of the pole piece caused by the insertion and removal of ions during the electrochemical reaction, and improve the battery's cycle performance, high-temperature storage performance and gas production performance.
A-嵌段中包含含有三氟甲基的式II所示的结构单元使得BAB型嵌段共聚物能够进一步提高极片的粘结力和吸液速率,降低极片的膜片电阻,有效抑制正极活性材料中过渡金属的溶出,提高电池的循环性能、高温存储性能和安全性能。The structural unit represented by formula II containing trifluoromethyl in the A-block enables the BAB-type block copolymer to further improve the adhesion and liquid absorption rate of the electrode, reduce the membrane resistance of the electrode, effectively inhibit the dissolution of transition metals in the positive electrode active material, and improve the cycle performance, high temperature storage performance and safety performance of the battery.
在一些实施方式中,A-嵌段包含含有砜基的式II所示的结构单 元。In some embodiments, the A-block comprises a structural unit of Formula II containing a sulfone group. Yuan.
在一些实施方式中,所述含有砜基的式II所示的结构单元包含

In some embodiments, the structural unit represented by formula II containing a sulfone group comprises

中的一种或多种。One or more of .
砜基基团具有强吸电子作用,能够增强极片与活性材料中导电离子的结合能力,提高极片的粘结力,同时砜基能够提高极片对电解液的吸液速率,使得极片具有较低的膜片电阻。砜基还可以增强酰亚胺键结构的稳定性,提高粘结剂在电极充放电过程中的结构稳定性,进而提高电池的循环性能、高温存储性能和安全性能。The sulfone group has a strong electron-withdrawing effect, which can enhance the bonding ability between the electrode and the conductive ions in the active material, improve the bonding force of the electrode, and at the same time, the sulfone group can increase the electrolyte absorption rate of the electrode, so that the electrode has a lower membrane resistance. The sulfone group can also enhance the stability of the imide bond structure and improve the structural stability of the binder during the electrode charge and discharge process, thereby improving the battery's cycle performance, high-temperature storage performance and safety performance.
A-嵌段中包含含有砜基的式II所示的结构单元使得BAB型嵌段共聚物能够进一步提高极片的粘结力和吸液速率,降低极片的膜片电阻,抑制正极活性材料中过渡金属的溶出,提高电池的循环性能和高温存储性能。The structural unit shown in formula II containing a sulfone group in the A-block enables the BAB-type block copolymer to further improve the adhesion and liquid absorption rate of the electrode, reduce the membrane resistance of the electrode, inhibit the dissolution of transition metals in the positive electrode active material, and improve the cycle performance and high-temperature storage performance of the battery.
在一些实施方式中,A-嵌段包含含有醚键的式II所示的结构单元。In some embodiments, the A-block comprises a structural unit of Formula II containing an ether bond.
式II所示的结构单元中含有醚键,有助于提高粘结剂的柔韧性,提高电池的循环性能和产气性能。The structural unit shown in Formula II contains an ether bond, which helps to improve the flexibility of the binder and improve the cycle performance and gas production performance of the battery.
本申请的一个实施方式提供一种BAB型嵌段共聚物的制备方法,包括以下步骤:One embodiment of the present application provides a method for preparing a BAB type block copolymer, comprising the following steps:
制备B-嵌段:将至少一种式Ⅴ所示单体聚合制备B-嵌段,
Preparation of B-block: polymerizing at least one monomer represented by formula V to prepare B-block,
其中A1、A2、A3各自独立地选自氢、氟、至少含有一个氟原子的C1-3烷基中的一种或多种;wherein A 1 , A 2 , and A 3 are each independently selected from one or more of hydrogen, fluorine, and a C 1-3 alkyl group containing at least one fluorine atom;
制备A-嵌段:将至少一种二元胺和至少一种二元酐或至少一种二元酸聚合制备A-嵌段,或者将内酰胺单体开环聚合制备A-嵌段;Preparing the A-block: polymerizing at least one diamine and at least one dibasic anhydride or at least one dibasic acid to prepare the A-block, or ring-opening polymerizing a lactam monomer to prepare the A-block;
制备BAB型嵌段共聚物:将B-嵌段和A-嵌段接合制备BAB型 嵌段共聚物。Preparation of BAB type block copolymers: B-block and A-block are joined to prepare BAB type Block copolymers.
在一些实施方式中,BAB型嵌段共聚物6的制备方法示意图如图1所示,其中,包含式II、式III或式IV所示结构单元612的A-嵌段61的两端基团611为活性基团,包含式I所示结构单元622的B-嵌段62的末端基团621为活性基团,A-嵌段的两端基团611与B-嵌段的末端基团621反应实现聚合物链段的接合,从而制备BAB型嵌段共聚物6。In some embodiments, a schematic diagram of a method for preparing a BAB-type block copolymer 6 is shown in FIG1 , wherein the end groups 611 of an A-block 61 comprising a structural unit 612 shown in Formula II, Formula III or Formula IV are active groups, and the terminal groups 621 of a B-block 62 comprising a structural unit 622 shown in Formula I are active groups, and the end groups 611 of the A-block react with the terminal groups 621 of the B-block to achieve bonding of polymer segments, thereby preparing a BAB-type block copolymer 6.
在本文中,术语“二元胺”是指含有两个氨基的胺。As used herein, the term "diamine" refers to an amine containing two amino groups.
在一些实施方式中,二元胺为脂肪族二元胺或芳香族二元胺,包含

In some embodiments, the diamine is an aliphatic diamine or an aromatic diamine, comprising

中的一种或多种,其中n为6-12之间的任意整数。 One or more of , wherein n is any integer between 6 and 12.
在本文中,术语“二元酐”是指含有两个酸酐的单体。As used herein, the term "dianhydride" refers to a monomer containing two anhydrides.
在一些实施方式中,二元酐为芳二酐,包含
中的一种或多种。
In some embodiments, the dibasic anhydride is an aromatic dianhydride, comprising
One or more of .
在本文中,术语“二元酸”是指含有两个羧基的单体。二元酸可选自芳族二元酸或脂肪族二元酸,如己二酸、癸二酸、对苯二甲酸、间苯二甲酸中的一种或者多种。In this document, the term "diacid" refers to a monomer containing two carboxyl groups. The dibasic acid can be selected from aromatic dibasic acids or aliphatic dibasic acids, such as one or more of adipic acid, sebacic acid, terephthalic acid, and isophthalic acid.
该制备方法原料便宜,可以降低成本,减少对环境的污染,有利于粘结剂产量的提升。同时以该方法制备的BAB型嵌段共聚物作为粘结剂,能够使得极片具有优秀的吸液能力、良好的粘结力、较低的膜片电阻,使得电池的循环性能、高温存储性能和安全性能得 到改善。The preparation method has cheap raw materials, can reduce costs, reduce environmental pollution, and is conducive to the improvement of binder production. At the same time, the BAB type block copolymer prepared by this method as a binder can make the pole piece have excellent liquid absorption capacity, good adhesion, and low membrane resistance, so that the battery's cycle performance, high temperature storage performance and safety performance are improved. to improvement.
在一些实施方式中,所述制备B-嵌段具体包括:In some embodiments, the preparation of the B-block specifically comprises:
将至少一种式Ⅴ所示单体、链转移剂和引发剂通过可逆加成-裂解链转移聚合得到单端具有叠氮基团或炔基的B-嵌段。At least one monomer represented by formula V, a chain transfer agent and an initiator are polymerized by reversible addition-fragmentation chain transfer to obtain a B-block having an azide group or an alkynyl group at one end.
在一些实施方式中,可逆加成-裂解链转移聚合的反应温度为70~90℃,反应时间为5~8.5小时。In some embodiments, the reaction temperature of the reversible addition-fragmentation chain transfer polymerization is 70 to 90° C., and the reaction time is 5 to 8.5 hours.
在一些实施方式中,所述制备B-嵌段具体包括:In some embodiments, the preparation of the B-block specifically comprises:
将至少一种式Ⅴ所示单体、链转移剂和引发剂在70~90℃的反应温度下通过可逆加成-裂解链转移聚合,反应5~8.5小时得到单端具有叠氮基团或炔基的B-嵌段。At least one monomer represented by formula V, a chain transfer agent and an initiator are subjected to reversible addition-fragmentation chain transfer polymerization at a reaction temperature of 70 to 90° C. for 5 to 8.5 hours to obtain a B-block having an azide group or an alkynyl group at one end.
在本文中,术语“叠氮基团”是指-N3基团。As used herein, the term "azide group" refers to a -N3 group.
在本文中,术语“炔基”是指-C≡CH基团。As used herein, the term "alkynyl" refers to a -C≡CH group.
在本文中,术语“可逆加成-裂解链转移聚合”(RAFT聚合)是一种可逆失活自由基聚合,也被称为“活性/可控自由基聚合方法”。RAFT聚合的主要原理是通过在自由基聚合中加入作为链转移试剂的RAFT试剂,将易终止的自由基通过链转移的方式保护起来使得聚合反应中大多数自由基转变为休眠种自由基,在反应过程中休眠链段与活性链段同时存在并通过动态可逆的反应不断进行快速的相互切换,从而导致在任一时刻只有少数的聚合物链以活性链形式存在并进行增长最终使得每条聚合物链段的增长几率大致相等进而表现出活性聚合的特征。In this article, the term "reversible addition-fragmentation chain transfer polymerization" (RAFT polymerization) is a type of reversibly deactivated free radical polymerization, also known as a "living/controlled free radical polymerization method". The main principle of RAFT polymerization is to add a RAFT agent as a chain transfer agent to the free radical polymerization, and protect the easily terminated free radicals through chain transfer, so that most of the free radicals in the polymerization reaction are converted into dormant free radicals. During the reaction, dormant segments and active segments exist at the same time and are constantly and rapidly switched to each other through dynamic reversible reactions, resulting in only a few polymer chains existing in the form of active chains and growing at any one time, and finally making the growth probability of each polymer segment roughly equal, thus showing the characteristics of living polymerization.
在一些实施方式中,式Ⅴ所示单体为偏二氟乙烯、四氟乙烯、氟乙烯中的一种或多种。In some embodiments, the monomer represented by formula V is one or more of vinylidene fluoride, tetrafluoroethylene, and vinyl fluoride.
在一些实施方式中,B-嵌段的合成路线示意图如下图所示,其中,链转移剂为三硫代碳酸酯,Z’为末端含有炔基或叠氮基团的活性基团,R为烷基。通过下述反应,制备了末端具有炔基或叠氮基团的B-嵌段。
In some embodiments, the synthesis route of the B-block is shown in the figure below, wherein the chain transfer agent is trithiocarbonate, Z' is an active group having an alkynyl or azide group at the end, and R is an alkyl group. The B-block having an alkynyl or azide group at the end is prepared by the following reaction.
采用可逆加成-裂解链转移聚合,可实现可控聚合,且产物分子量分布较窄。而且通过上述反应,B-嵌段只在末端具有炔基或叠氮基团,方便以高效温和的方式定向的与A-嵌段发生接合,生成BAB型三嵌段共聚物。The reversible addition-fragmentation chain transfer polymerization can achieve controllable polymerization, and the molecular weight distribution of the product is relatively narrow. Moreover, through the above reaction, the B-block only has an alkynyl or azide group at the end, which is convenient for directing and bonding with the A-block in an efficient and mild manner to generate a BAB-type triblock copolymer.
采用该制备方法,可实现可控聚合,且产物分子量分布较窄。By adopting the preparation method, controllable polymerization can be achieved, and the molecular weight distribution of the product is relatively narrow.
在一些实施方式中,所述制备A-嵌段具体包括:In some embodiments, the preparation of the A-block specifically comprises:
将至少一种二元胺和至少一种二元酐或至少一种二元酸进行聚合,得到两端的端基均为酸酐、羧基或氨基的产物;Polymerizing at least one diamine and at least one dibasic anhydride or at least one dibasic acid to obtain a product having end groups at both ends being anhydride, carboxyl or amino groups;
对产物的端基进行官能化反应,得到两端均具有炔基或叠氮基团的所述A-嵌段。The terminal groups of the product are subjected to functionalization reaction to obtain the A-block having alkynyl groups or azide groups at both ends.
在一些实施方式中,至少一种二元胺和至少一种二元酐或至少一种二元酸的聚合条件为在室温下搅拌反应4~10小时,继续升温至170~210℃反应5~20小时。In some embodiments, the polymerization conditions of at least one diamine and at least one dibasic anhydride or at least one dibasic acid are stirring the reaction at room temperature for 4 to 10 hours, and then heating to 170 to 210° C. for 5 to 20 hours.
在一些实施方式中,所述制备A-嵌段具体包括:In some embodiments, the preparation of the A-block specifically comprises:
将催化剂、至少一种二元胺和至少一种二元酐或至少一种二元酸在室温下搅拌反应4~10小时,升温至170~210℃反应5~20小时,得到两端的端基均为酸酐、羧基或氨基的产物;The catalyst, at least one diamine and at least one dibasic anhydride or at least one dibasic acid are stirred and reacted at room temperature for 4 to 10 hours, and the temperature is raised to 170 to 210° C. and reacted for 5 to 20 hours to obtain a product having end groups at both ends being anhydride, carboxyl or amino groups;
对产物的端基进行官能化反应,得到两端均具有炔基或叠氮基团的所述A-嵌段。The terminal groups of the product are subjected to functionalization reaction to obtain the A-block having alkynyl groups or azide groups at both ends.
在一些实施方式中,A-嵌段的合成路线为在催化剂的作用下,至少一种二元胺和至少一种二元酐发生聚合反应生成聚酰亚胺,使得二元胺或二元酐过量,得到两端的端基均为氨基或酸酐的聚酰亚胺,两端的氨基或酸酐与包含叠氮基团或炔基的活性单体进行官能化反应,制备两端均具有叠氮基团或炔基的A-嵌段。可以理解,包含叠氮基团或炔基的活性单体是指包含叠氮基团或炔基且包含能够 与聚酰亚胺两端的氨基或酸酐反应的活性官能团的单体,与氨基发生反应的活性官能团可选为环氧基、羧基、酸酐、异氰酸酯基、羰基氯中的任意一种。与酸酐反应的活性官能团可选为氨基。In some embodiments, the synthesis route of the A-block is that at least one diamine and at least one dibasic anhydride undergo a polymerization reaction under the action of a catalyst to generate a polyimide, so that the diamine or dibasic anhydride is in excess, and a polyimide with amino groups or acid anhydrides at both ends is obtained, and the amino groups or acid anhydrides at both ends are functionalized with an active monomer containing an azide group or an alkynyl group to prepare an A-block with an azide group or an alkynyl group at both ends. It is understood that the active monomer containing an azide group or an alkynyl group refers to a monomer containing an azide group or an alkynyl group and containing an azide group or an alkynyl group. The monomer having an active functional group that reacts with the amino group or acid anhydride at both ends of the polyimide, the active functional group that reacts with the amino group can be any one of epoxy, carboxyl, acid anhydride, isocyanate, and carbonyl chloride. The active functional group that reacts with the acid anhydride can be an amino group.
在本文中,术语“氨基”指的是-NH2基团。As used herein, the term "amino" refers to a -NH2 group.
在本文中,术语“酸酐”指的是-CO-O-CO-基团。As used herein, the term "anhydride" refers to a -CO-O-CO- group.
在本文中,术语“环氧基”指的是-CH-O-CH-基团。As used herein, the term "epoxy" refers to a -CH-O-CH- group.
在本文中,术语“羧基”指的是-COOH基团。As used herein, the term "carboxyl" refers to a -COOH group.
在本文中,术语“异氰酸酯基”指的是-NCO基团。As used herein, the term "isocyanate" refers to an -NCO group.
在本文中,术语“羰基氯”指的是-COCl基团。As used herein, the term "carbonyl chloride" refers to a -COCl group.
在本文中,术语“亚氨基”是指“-NH-”基团。As used herein, the term "imino" refers to a "-NH-" group.
在一些实施方式中,A-嵌段的合成路线为在催化剂的作用下,至少一种二元胺和至少一种二元酸发生缩聚反应生成聚酰胺,使得二元胺或二元酸过量,得到两端的端基均为氨基或羧基的聚酰胺,两端的氨基或羧基与包含叠氮基团或炔基的活性单体进行官能化反应,制备两端均具有叠氮基团或炔基的A-嵌段。可以理解,包含叠氮基团或炔基的活性单体是指包含叠氮基团或炔基且包含能够与聚酰胺两端的氨基或羧基反应的活性官能团的单体,与氨基发生反应的活性官能团可选为环氧基、羧基、酸酐、异氰酸酯基、羰基氯中的任意一种。与羧基反应的活性官能团可选为氨基或亚氨基。In some embodiments, the synthesis route of the A-block is that at least one diamine and at least one dibasic acid undergo a polycondensation reaction to generate polyamide under the action of a catalyst, so that the diamine or dibasic acid is excessive, and the end groups at both ends are amino or carboxyl polyamides, and the amino or carboxyl groups at both ends are functionalized with active monomers containing azide groups or alkynyl groups to prepare A-blocks with azide groups or alkynyl groups at both ends. It is understood that the active monomer containing azide groups or alkynyl groups refers to a monomer containing azide groups or alkynyl groups and containing active functional groups that can react with amino groups or carboxyl groups at both ends of the polyamide, and the active functional groups that react with amino groups can be selected from any one of epoxy groups, carboxyl groups, acid anhydrides, isocyanate groups, and carbonyl chloride. The active functional group that reacts with carboxyl groups can be selected from amino groups or imino groups.
在一些实施方式中,催化剂可选为喹啉、异喹啉、叔胺中的任意一种。In some embodiments, the catalyst may be any one of quinoline, isoquinoline, and tertiary amine.
在一些实施方式中,所述制备A-嵌段具体包括:In some embodiments, the preparation of the A-block specifically comprises:
将端基调节剂、水和至少一种内酰胺单体进行聚合反应,得到两端的端基均为羧基或氨基的产物;A terminal group regulator, water and at least one lactam monomer are polymerized to obtain a product having terminal groups at both ends being carboxyl groups or amino groups;
对产物的端基进行官能化反应,得到两端均具有炔基或叠氮基团的A-嵌段。The terminal groups of the product are functionalized to obtain an A-block having alkynyl or azide groups at both ends.
在一些实施方式中,端基调节剂、水和至少一种内酰胺单体聚合反应的条件为在250℃~280℃的反应温度下聚合12~24小时。In some embodiments, the polymerization reaction conditions of the terminal group regulator, water and at least one lactam monomer are 250° C. to 280° C. for 12 to 24 hours.
在一些实施方式中,所述制备A-嵌段具体包括:In some embodiments, the preparation of the A-block specifically comprises:
将端基调节剂、水和至少一种内酰胺单体在250℃~280℃的反 应温度下聚合反应12~24小时,得到两端的端基均为羧基或氨基的产物;The end group regulator, water and at least one lactam monomer are reacted at 250°C to 280°C. The polymerization reaction is carried out at a temperature of 12 to 24 hours to obtain a product having carboxyl or amino groups at both ends;
对产物的端基进行官能化反应,得到两端均具有炔基或叠氮基团的A-嵌段。The terminal groups of the product are functionalized to obtain an A-block having alkynyl or azide groups at both ends.
在一些实施方式中,A-嵌段的合成路线如下所示,在水的催化下,内酰胺单体发生开环聚合反应,得到一端为氨基、一端为羧基的聚酰胺,再加入端基调节剂与聚酰胺进行反应,得到两端的端基均为氨基或羧基的聚酰胺,两端的氨基或羧基与包含叠氮基团或炔基的活性单体进行官能化反应,制备两端均具有叠氮基团或炔基的A-嵌段。可以理解,包含叠氮基团或炔基的活性单体是指包含叠氮基团或炔基且包含能够与聚酰胺两端的氨基或羧基反应的活性官能团的单体,与氨基发生反应的活性官能团可选为环氧基、羧基、酸酐、异氰酸酯基、羰基氯中的任意一种。与羧基反应的活性官能团可选为氨基或亚氨基。In some embodiments, the synthesis route of the A-block is as follows, under the catalysis of water, the lactam monomer undergoes a ring-opening polymerization reaction to obtain a polyamide with an amino group at one end and a carboxyl group at the other end, and then an end group regulator is added to react with the polyamide to obtain a polyamide with amino or carboxyl groups at both ends, and the amino or carboxyl groups at both ends are functionalized with an active monomer containing an azide group or an alkynyl group to prepare an A-block with an azide group or an alkynyl group at both ends. It is understood that the active monomer containing an azide group or an alkynyl group refers to a monomer containing an azide group or an alkynyl group and containing an active functional group that can react with the amino or carboxyl groups at both ends of the polyamide, and the active functional group that reacts with the amino group can be selected from any one of an epoxy group, a carboxyl group, an anhydride group, an isocyanate group, and a carbonyl chloride group. The active functional group that reacts with the carboxyl group can be selected from an amino group or an imino group.
在一些实施方式中,内酰胺单体可选为己内酰胺、辛内酰胺、癸内酰胺、十二内酰胺中的一种或多种。In some embodiments, the lactam monomer may be selected from one or more of caprolactam, capryllactam, decanolactam, and laurolactam.
采用该制备方法制备出的两侧末端叠氮化或炔基化的A-嵌段,便于以高效温和的方式与B-嵌段发生嵌段间的连接,生成BAB型嵌段共聚物。The A-block with azidation or alkyne at both ends prepared by the preparation method can be easily connected with the B-block in an efficient and mild manner to generate a BAB type block copolymer.
在一些实施方式中,所述制备BAB型嵌段共聚物具体包括:In some embodiments, the preparation of the BAB type block copolymer specifically comprises:
将两端均具有炔基或叠氮基团的A-嵌段与单端具有叠氮基团或炔基的B-嵌段混合,进行点击反应,制备BAB型嵌段共聚物,其中B-嵌段和A-嵌段的端基不同。The A-block having alkynyl or azide groups at both ends is mixed with the B-block having an azide or alkyne group at one end and subjected to a click reaction to prepare a BAB type block copolymer, wherein the end groups of the B-block and the A-block are different.
在本文中,术语“点击反应”是指炔基与叠氮基发生环加成反应,使得A-嵌段与B-嵌段相连的反应。在一些实施方式中,点击反应在Cu(I)催化剂的存在下,常温常压下进行。Herein, the term "click reaction" refers to a cycloaddition reaction between an alkynyl group and an azide group, so that the A-block is connected to the B-block. In some embodiments, the click reaction is carried out in the presence of a Cu(I) catalyst at room temperature and pressure.
在一些实施方式中,B-嵌段的端基为叠氮基团,A-嵌段的端基为炔基。In some embodiments, the terminal group of the B-block is an azide group and the terminal group of the A-block is an alkynyl group.
在一些实施方式中,B-嵌段的端基为炔基,A-嵌段的端基为叠氮基团。 In some embodiments, the terminal group of the B-block is an alkynyl group and the terminal group of the A-block is an azide group.
上述制备方法,具有产率高、副产物无害、反应条件简单温和、反应原料易得的优点,能够实现嵌段聚合物的可控聚合,有利于提高产品的良品率。The above preparation method has the advantages of high yield, harmless by-products, simple and mild reaction conditions, and readily available reaction raw materials. It can achieve controlled polymerization of block polymers, which is beneficial to improving the yield rate of products.
在一些实施方式中,链转移剂为含末端炔基或叠氮基团的RAFT链转移剂。在一些实施方式中,链转移剂为含末端炔基或叠氮基团的三硫代碳酸酯。在一些实施方式中,链转移剂的结构式选自下式,
In some embodiments, the chain transfer agent is a RAFT chain transfer agent containing a terminal alkynyl or azide group. In some embodiments, the chain transfer agent is a trithiocarbonate containing a terminal alkynyl or azide group. In some embodiments, the structural formula of the chain transfer agent is selected from the following formula,
含末端炔基或叠氮基团的RAFT链转移剂在B-嵌段合成的同时使得B-嵌段的末端带有炔基或叠氮基团,为A-嵌段与B-嵌段发生点击反应提供了基础,避免了复杂的后处理步骤,能够提高反应效率。The RAFT chain transfer agent containing a terminal alkynyl or azide group allows the terminal of the B-block to carry an alkynyl or azide group during the synthesis of the B-block, providing a basis for the click reaction between the A-block and the B-block, avoiding complex post-processing steps, and improving the reaction efficiency.
在一些实施方式中,端基调节剂为二元胺或二元酸。In some embodiments, the end group modifier is a diamine or a dibasic acid.
二元胺或二元酸的端基调节剂能够与产物的端基反应,得到两端的端基均为氨基或羧基的产物,便于后续转化的发生,能够以简单高效的方式制备两端的端基均为叠氮基或炔基的A-嵌段。The end group regulator of the diamine or dibasic acid can react with the end group of the product to obtain a product with both end groups being amino or carboxyl, which is convenient for subsequent conversion and can prepare A-blocks with both end groups being azido or alkynyl in a simple and efficient manner.
在一些实施方式中,BAB型嵌段共聚物可以应用在二次电池中,可选地,二次电池包括锂离子电池、钠离子电池、镁离子电池、钾离子电池中的至少一种。In some embodiments, the BAB type block copolymer may be used in a secondary battery. Optionally, the secondary battery includes at least one of a lithium ion battery, a sodium ion battery, a magnesium ion battery, and a potassium ion battery.
[正极极片][Positive electrode]
正极极片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,所述正极膜层包括正极活性材料、导电剂和粘结剂,该粘结剂为一些实施方式中的BAB型嵌段共聚物或一些实施方式中的制备方法制备的BAB型嵌段共聚物。 The positive electrode plate includes a positive electrode current collector and a positive electrode film layer arranged on at least one surface of the positive electrode current collector, wherein the positive electrode film layer includes a positive electrode active material, a conductive agent and a binder, and the binder is a BAB type block copolymer in some embodiments or a BAB type block copolymer prepared by the preparation method in some embodiments.
该正极极片具有优异的吸液速率和良好的粘结力,低的膜片电阻和过渡金属溶出量。The positive electrode sheet has excellent liquid absorption rate and good bonding force, low membrane resistance and transition metal dissolution amount.
在一些实施方式中,粘结剂的质量百分比为0.1%~3%,基于正极活性材料的总质量计。在一些实施方式中,粘结剂的质量百分比可选为0.1%~0.2%、0.2%~1%、0.2%~1.03%、1%~3%、1.03%~3%中的任意一种。In some embodiments, the mass percentage of the binder is 0.1% to 3%, based on the total mass of the positive electrode active material. In some embodiments, the mass percentage of the binder can be selected from any one of 0.1% to 0.2%, 0.2% to 1%, 0.2% to 1.03%, 1% to 3%, and 1.03% to 3%.
当粘结剂含量过低时,粘结剂无法充分发挥粘结作用和分散作用,导致极片的粘结力不足、膜片电阻升高,对电池的循环性能和高温存储性能产生负面影响。当粘结剂含量过高时,浆料的粘度过大,会导致包覆于正极活性材料表面的粘结剂包覆层过厚,在电池循环过程中影响电子和离子的传输,使得极片的膜片内阻增大,影响电池的循环性能和高温存储性能。When the binder content is too low, the binder cannot fully exert its bonding and dispersion effects, resulting in insufficient bonding force of the pole piece and increased membrane resistance, which has a negative impact on the battery's cycle performance and high-temperature storage performance. When the binder content is too high, the viscosity of the slurry is too high, which will cause the binder coating layer on the surface of the positive electrode active material to be too thick, affecting the transmission of electrons and ions during the battery cycle, increasing the internal resistance of the pole piece membrane, and affecting the battery's cycle performance and high-temperature storage performance.
控制粘结剂的质量百分比在合适范围内,可以使得极片具有优异的吸液速率、良好的粘结力、较低的膜片电阻。另外极片中的粘结剂能够抑制活性材料中过渡金属的溶出,提高电池的循环性能、高温存储性能和安全性能。Controlling the mass percentage of the binder within a suitable range can make the pole piece have excellent liquid absorption rate, good bonding force, and low membrane resistance. In addition, the binder in the pole piece can inhibit the dissolution of transition metals in the active material, and improve the cycle performance, high temperature storage performance and safety performance of the battery.
在一些实施方式中,所述正极膜层与所述正极集流体间单位长度的粘结力不小于11.5N/m,可选为11.5-15N/m。在一些实施方式中,所述正极膜层与所述正极集流体间单位长度的粘结力可选为11.5N/m、12N/m、12.5N/m、13N/m、13.5N/m、14N/m、14.5N/m、15N/m。In some embodiments, the bonding force per unit length between the positive electrode film layer and the positive electrode current collector is not less than 11.5 N/m, and can be 11.5-15 N/m. In some embodiments, the bonding force per unit length between the positive electrode film layer and the positive electrode current collector can be 11.5 N/m, 12 N/m, 12.5 N/m, 13 N/m, 13.5 N/m, 14 N/m, 14.5 N/m, or 15 N/m.
正极膜层与正极集流体间单位长度的粘结力可以采用本领域公知的任意手段进行测试,如参照GB-T2790-1995国标《胶粘剂180°剥离强度实验方法》进行测试。作为示例,将正极极片裁剪为20*100mm2尺寸的测试试样,备用;极片用双面胶粘接正极膜层一面,并用压辊压实,使双面胶与极片完全贴合;双面胶的另外一面粘贴于不锈钢表面,将试样一端反向弯曲,弯曲角度为180°;采用高铁拉力机测试,将不锈钢一端固定于拉力机下方夹具,试样弯曲末端固定于上方夹具,调整试样角度,保证上下端位于垂直位置,然后以50mm/min的速度拉伸试样,直到正极集流体全部从正极膜 层剥离,记录过程中的位移和作用力。以受力平衡时的力除以与双面胶贴合的极片的宽度(极片的宽度方向垂直于剥离方向)做为单位长度的极片的粘结力,本测试中极片的宽度为20mm。The bonding force per unit length between the positive electrode film layer and the positive electrode current collector can be tested by any means known in the art, such as testing with reference to GB-T2790-1995 national standard "Adhesive 180° Peel Strength Test Method". As an example, the positive electrode plate is cut into a test specimen of 20* 100mm2 size for use; the electrode is bonded to one side of the positive electrode film layer with double-sided tape, and compacted with a pressure roller to make the double-sided tape and the electrode completely fit; the other side of the double-sided tape is adhered to the stainless steel surface, and one end of the sample is bent in the opposite direction with a bending angle of 180°; the high-speed rail tensile machine is used for testing, one end of the stainless steel is fixed to the lower fixture of the tensile machine, and the bent end of the sample is fixed to the upper fixture, the angle of the sample is adjusted to ensure that the upper and lower ends are in a vertical position, and then the sample is stretched at a speed of 50mm/min until the positive current collector is completely removed from the positive electrode film. The layers are peeled off, and the displacement and force in the process are recorded. The force when the force is balanced is divided by the width of the electrode attached to the double-sided adhesive (the width direction of the electrode is perpendicular to the peeling direction) as the bonding force of the electrode per unit length. In this test, the width of the electrode is 20mm.
该极片的正极膜层与正极集流体之间具有高的粘结强度,在使用过程中,正极膜层不容易从正极集流体上脱落,有助于提高电池的循环性能和安全性。The positive electrode film layer of the pole piece has high bonding strength with the positive electrode current collector. During use, the positive electrode film layer is not easy to fall off from the positive electrode current collector, which helps to improve the cycle performance and safety of the battery.
在一些实施方式中,所述正极极片对电解液的吸液速率大于0.31μg/s,可选为0.32-0.5μg/s,所述电解液的密度为1.1-1.2g/cm3。在一些实施方式中,正极极片对电解液的吸液速率,可选为0.32μg/s、0.33μg/s、0.34μg/s、0.35μg/s、0.36μg/s、0.37μg/s、0.38μg/s、0.39μg/s、0.40μg/s、0.41μg/s、0.42μg/s、0.43μg/s、0.44μg/s、0.45μg/s、0.46μg/s、0.47μg/s、0.484μg/s、0.49μg/s、0.50μg/s,所述电解液的密度为1.1-1.2g/cm3In some embodiments, the electrolyte absorption rate of the positive electrode plate is greater than 0.31 μg/s, and may be 0.32-0.5 μg/s, and the electrolyte has a density of 1.1-1.2 g/cm 3 . In some embodiments, the liquid absorption rate of the positive electrode plate to the electrolyte can be selected as 0.32μg/s, 0.33μg/s, 0.34μg/s, 0.35μg/s, 0.36μg/s, 0.37μg/s, 0.38μg/s, 0.39μg/s, 0.40μg/s, 0.41μg/s, 0.42μg/s, 0.43μg/s, 0.44μg/s, 0.45μg/s, 0.46μg/s, 0.47μg/s, 0.484μg/s, 0.49μg/s, 0.50μg/s, and the density of the electrolyte is 1.1-1.2g/ cm3 .
极片的吸液速率可以反映极片在电解液中润湿的能力。该测试可以采用本领域公知的任意手段进行。作为示例,将冷压后的正极极片裁剪为5*5cm2尺寸的测试样品;首先,将样品在80℃下干燥4h,测试极片厚度后,固定在样品台上,然后挑选d=200μm的毛细管,用5000目砂纸打磨端面至平整,利用显微镜观察毛细管与极片间状态;用毛细管吸取电解液,控制电解液高度h=3mm,下降毛细管与极片接触,同时用秒表计时,当液面下降完毕后,停止计时,读取吸液时间t,记录数据;利用公式计算极片的平均吸液速率v,v=π×(d/2)2×h×ρ/t。本测试中,选用的电解液的密度为1.1-1.2g/cm3。作为示例,电解液可以通过六氟磷酸锂溶解于碳酸乙烯酯和碳酸甲乙酯的混合溶剂中配置,六氟磷酸锂溶液的质量含量为12.5%,溶液中碳酸乙烯酯和碳酸甲乙酯的体积比为3:7。The liquid absorption rate of the electrode can reflect the ability of the electrode to wet in the electrolyte. The test can be performed by any means known in the art. As an example, the cold-pressed positive electrode is cut into a test sample of 5* 5cm2 ; first, the sample is dried at 80℃ for 4h, and after the thickness of the electrode is tested, it is fixed on the sample table, and then a capillary with d=200μm is selected, and the end face is polished with 5000 mesh sandpaper to be flat, and the state between the capillary and the electrode is observed under a microscope; the electrolyte is absorbed by the capillary, and the electrolyte height is controlled to h=3mm, and the capillary is lowered to contact the electrode, and a stopwatch is used to time. When the liquid level drops, the timing is stopped, the liquid absorption time t is read, and the data is recorded; the average liquid absorption rate v of the electrode is calculated using the formula, v=π×(d/2) 2 ×h×ρ/t. In this test, the density of the selected electrolyte is 1.1-1.2g/ cm3 . As an example, the electrolyte can be prepared by dissolving lithium hexafluorophosphate in a mixed solvent of ethylene carbonate and ethyl methyl carbonate, the mass content of the lithium hexafluorophosphate solution is 12.5%, and the volume ratio of ethylene carbonate to ethyl methyl carbonate in the solution is 3:7.
该极片具有较高的吸液速率,能够提高电解液对极片的浸润效率,改善离子传输路径,降低界面电阻,提高电池性能。The electrode has a high liquid absorption rate, which can improve the electrolyte infiltration efficiency of the electrode, improve the ion transmission path, reduce the interface resistance, and improve the battery performance.
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。 As an example, the positive electrode current collector has two surfaces opposite to each other in its thickness direction, and the positive electrode film layer is disposed on any one or both of the two opposite surfaces of the positive electrode current collector.
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。In some embodiments, the positive electrode current collector may be a metal foil or a composite current collector. For example, aluminum foil may 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 may be formed by forming a metal material (aluminum, aluminum alloy, nickel, nickel alloy, titanium, titanium alloy, silver and silver alloy, etc.) on a polymer material substrate (such as a substrate of polypropylene (PP), polyethylene terephthalate (PET), polybutylene terephthalate (PBT), polystyrene (PS), polyethylene (PE), etc.).
在一些实施方式中,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LiCoO2)、锂镍氧化物(如LiNiO2)、锂锰氧化物(如LiMnO2、LiMn2O4)、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LiNi1/3Co1/3Mn1/3O2(也可以简称为NCM333)、LiNi0.5Co0.2Mn0.3O2(也可以简称为NCM523)、LiNi0.5Co0.25Mn0.25O2(也可以简称为NCM211)、LiNi0.6Co0.2Mn0.2O2(也可以简称为NCM622)、LiNi0.8Co0.1Mn0.1O2(也可以简称为NCM811)、锂镍钴铝氧化物(如LiNi0.85Co0.15Al0.05O2)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LiFePO4(也可以简称为LFP))、磷酸铁锂与碳的复合材料、磷酸锰锂(如LiMnPO4)、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。In some embodiments, the positive electrode active material may be a positive electrode active material for a battery known in the art. As an example, the positive electrode active material may include at least one of the following materials: an olivine-structured lithium-containing phosphate, a lithium transition metal oxide, and their respective modified compounds. However, the present application is not limited to these materials, and other traditional materials that can be used as positive electrode active materials for batteries may also be used. These positive electrode active materials may be used alone or in combination of two or more. Among them, examples of lithium transition metal oxides may include, but are not limited to , lithium cobalt oxide (such as LiCoO2 ), lithium nickel oxide (such as LiNiO2 ), lithium manganese oxide (such as LiMnO2 , LiMn2O4 ), lithium nickel cobalt oxide, lithium manganese cobalt oxide, lithium nickel manganese oxide, lithium nickel cobalt manganese oxide (such as LiNi1 / 3Co1 / 3Mn1 / 3O2 (also referred to as NCM333 ), LiNi0.5Co0.2Mn0.3O2 (also referred to as NCM523 ) , LiNi0.5Co0.25Mn0.25O2 (also referred to as NCM211 ) , LiNi0.6Co0.2Mn0.2O2 (also referred to as NCM622 ), LiNi0.8Co0.1Mn0.1O2 (also referred to as NCM811 ), lithium nickel cobalt aluminum oxide ( such as LiNi 0.85 Co 0.15 Al 0.05 O 2 ) and at least one of modified compounds thereof. Examples of lithium-containing phosphates with an olivine structure may include, but are not limited to, at least one of lithium iron phosphate (such as LiFePO 4 (also referred to as LFP)), a composite material of lithium iron phosphate and carbon, lithium manganese phosphate (such as LiMnPO 4 ), a composite material of lithium manganese phosphate and carbon, lithium iron manganese phosphate, and a composite material of lithium iron manganese phosphate and carbon.
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。In some embodiments, the positive electrode film layer may further include a conductive agent, which may include, for example, at least one of superconducting carbon, acetylene black, carbon black, Ketjen black, carbon dots, carbon nanotubes, graphene, and carbon nanofibers.
在一些实施方式中,可以通过以下方式制备正极极片:将上述用于制备正极极片的组分,例如正极活性材料、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,即可得到正极极片。In some embodiments, the positive electrode sheet can be prepared by the following method: the components for preparing the positive electrode sheet, such as the positive electrode active material, the conductive agent, the binder and Any other components are dispersed in a solvent (such as N-methylpyrrolidone) to form a positive electrode slurry; the positive electrode slurry is coated on the positive electrode collector, and after drying, cold pressing and other processes, a positive electrode sheet can be obtained.
[负极极片][Negative electrode]
负极极片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材料。The negative electrode sheet includes a negative electrode current collector and a negative electrode film layer disposed on at least one surface of the negative electrode current collector, wherein the negative electrode film layer includes a negative electrode active material.
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。As an example, the negative electrode current collector has two surfaces opposite to each other in its thickness direction, and the negative electrode film layer is disposed on any one or both of the two opposite surfaces of the negative electrode current collector.
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。In some embodiments, the negative electrode current collector may be a metal foil or a composite current collector. For example, as the metal foil, copper foil may be used. The composite current collector may include a polymer material base layer and a metal layer formed on at least one surface of the polymer material substrate. The composite current collector may be formed by forming a metal material (copper, copper alloy, nickel, nickel alloy, titanium, titanium alloy, silver and silver alloy, etc.) on a polymer material substrate (such as a substrate of polypropylene (PP), polyethylene terephthalate (PET), polybutylene terephthalate (PBT), polystyrene (PS), polyethylene (PE), etc.).
在一些实施方式中,负极活性材料可采用本领域公知的用于电池的负极活性材料。作为示例,负极活性材料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、硅碳复合物、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材料的传统材料。这些负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。In some embodiments, the negative electrode active material may adopt the negative electrode active material for the battery known in the art. As an example, the negative electrode active material may include at least one of the following materials: artificial graphite, natural graphite, soft carbon, hard carbon, silicon-based materials, tin-based materials, lithium titanate, etc. The silicon-based material may be selected from at least one of elemental silicon, silicon oxide compounds, silicon-carbon composites, silicon-nitrogen composites, and silicon alloys. The tin-based material may be selected from at least one of elemental tin, tin oxide compounds, and tin alloys. However, the present application is not limited to these materials, and other traditional materials that can be used as negative electrode active materials for batteries may also be used. These negative electrode active materials may be used alone or in combination of two or more.
在一些实施方式中,负极膜层还可选地包括粘结剂。所述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。In some embodiments, the negative electrode film layer may further include a binder. The binder may be selected from at least one of styrene-butadiene rubber (SBR), polyacrylic acid (PAA), sodium polyacrylate (PAAS), polyacrylamide (PAM), polyvinyl alcohol (PVA), sodium alginate (SA), polymethacrylic acid (PMAA) and carboxymethyl chitosan (CMCS).
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。In some embodiments, the negative electrode film layer may also optionally include a conductive agent. The conductive agent may At least one selected from superconducting carbon, acetylene black, carbon black, Ketjen black, carbon dots, carbon nanotubes, graphene and carbon nanofibers.
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。In some embodiments, the negative electrode film layer may optionally include other additives, such as a thickener (eg, sodium carboxymethyl cellulose (CMC-Na)).
在一些实施方式中,可以通过以下方式制备负极极片:将上述用于制备负极极片的组分,例如负极活性材料、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,即可得到负极极片。In some embodiments, the negative electrode sheet can be prepared in the following manner: the components for preparing the negative electrode sheet, such as the negative electrode active material, the conductive agent, the binder and any other components are dispersed in a solvent (such as deionized water) to form a negative electrode slurry; the negative electrode slurry is coated on the negative electrode collector, and after drying, cold pressing and other processes, the negative electrode sheet can be obtained.
[电解质][Electrolytes]
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。The electrolyte plays the role of conducting ions between the positive electrode and the negative electrode. The present application has no specific restrictions on the type of electrolyte, which can be selected according to needs. For example, the electrolyte can be liquid, gel or all-solid.
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。In some embodiments, the electrolyte is an electrolyte solution, which includes an electrolyte salt and a solvent.
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。In some embodiments, the electrolyte salt can be selected from at least one of lithium hexafluorophosphate, lithium tetrafluoroborate, lithium perchlorate, lithium hexafluoroarsenate, lithium bis(fluorosulfonyl)imide, lithium bis(trifluoromethanesulfonyl)imide, lithium trifluoromethanesulfonate, lithium difluorophosphate, lithium difluorooxalatoborate, lithium dioxalatoborate, lithium difluorodioxalatophosphate, and lithium tetrafluorooxalatophosphate.
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。In some embodiments, the solvent can be selected from at least one of 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, 1,4-butyrolactone, cyclopentane sulfone, dimethyl sulfone, methyl ethyl sulfone and diethyl sulfone.
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。In some embodiments, the electrolyte may further include additives, such as negative electrode film-forming additives, positive electrode film-forming additives, and additives that can improve certain battery properties, such as additives that improve battery overcharge performance, additives that improve battery high or low temperature performance, etc.
[隔离膜] [Isolation film]
在一些实施方式中,二次电池中还包括隔离膜。本申请对隔离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隔离膜。In some embodiments, the secondary battery further includes a separator. The present application has no particular limitation on the type of separator, and any known porous separator with good chemical stability and mechanical stability can be selected.
在一些实施方式中,隔离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。隔离膜可以是单层薄膜,也可以是多层复合薄膜,没有特别限制。在隔离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。In some embodiments, the material of the isolation membrane can be selected from at least one of glass fiber, non-woven fabric, polyethylene, polypropylene and polyvinylidene fluoride. The isolation membrane can be a single-layer film or a multi-layer composite film, without particular limitation. When the isolation membrane is a multi-layer composite film, the materials of each layer can be the same or different, without particular limitation.
在一些实施方式中,正极极片、负极极片和隔离膜可通过卷绕工艺或叠片工艺制成电极组件。In some embodiments, the positive electrode sheet, the negative electrode sheet, and the separator may be formed into an electrode assembly by a winding process or a lamination process.
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。In some embodiments, the secondary battery may include an outer package, which may be used to encapsulate the electrode assembly and the electrolyte.
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。In some embodiments, the outer packaging of the secondary battery may be a hard shell, such as a hard plastic shell, an aluminum shell, a steel shell, etc. The outer packaging of the secondary battery may also be a soft package, such as a bag-type soft package. The material of the soft package may be plastic, and examples of the plastic include polypropylene, polybutylene terephthalate, and polybutylene succinate.
[二次电池][Secondary battery]
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2是作为一个示例的方形结构的二次电池5。所述二次电池也可以为钠离子电池、镁离子电池、钾离子电池。The present application has no particular restrictions on the shape of the secondary battery, which may be cylindrical, square or any other shape. For example, FIG2 is a secondary battery 5 of a square structure as an example. The secondary battery may also be a sodium ion battery, a magnesium ion battery, or a potassium ion battery.
在一些实施方式中,参照图3,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。In some embodiments, referring to FIG. 3 , the outer package may include a shell 51 and a cover plate 53. Among them, the shell 51 may include a bottom plate and a side plate connected to the bottom plate, and the bottom plate and the side plate enclose a receiving cavity. The shell 51 has an opening connected to the receiving cavity, and the cover plate 53 can be covered on the opening to close the receiving cavity. The positive electrode sheet, the negative electrode sheet and the isolation film can form an electrode assembly 52 through a winding process or a lamination process. The electrode assembly 52 is encapsulated in the receiving cavity. The 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.
[电池模板][Battery Template]
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。In some embodiments, the secondary batteries can be assembled into battery modules. The number of the secondary batteries included may 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.
图4是作为一个示例的电池模块4。参照图4,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。FIG4 is a battery module 4 as an example. Referring to FIG4 , in the battery module 4, a plurality of secondary batteries 5 may be arranged in sequence along the length direction of the battery module 4. Of course, they may also be arranged in any other manner. Further, the plurality of secondary batteries 5 may be fixed by fasteners.
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。Optionally, the battery module 4 may further include a housing having a housing space, and the plurality of secondary batteries 5 are housed in the housing space.
[用电装置][Electrical devices]
本申请的一个实施方式中,提供一种用电装置,包括任意实施方式的二次电池、任意实施方式的电池模块或任意实施方式的电池包中的至少一种。In one embodiment of the present application, there is provided an electric device, comprising at least one of a secondary battery of any embodiment, a battery module of any embodiment, or a battery pack of any embodiment.
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。The electrical device 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 for the electrical device, and can also be used as an energy storage unit for the electrical device. The electrical device may include mobile devices (such as mobile phones, laptops, etc.), electric vehicles (such as pure electric vehicles, hybrid electric vehicles, plug-in hybrid electric vehicles, electric bicycles, electric scooters, electric golf carts, electric trucks, etc.), electric trains, ships and satellites, energy storage systems, etc., but are not limited thereto.
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。As the electrical device, a secondary battery, a battery module or a battery pack may be selected according to its usage requirements.
图7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。FIG7 is an example of an electric device. The electric device is a pure electric vehicle, a hybrid electric vehicle, or a plug-in hybrid electric vehicle. In order to meet the electric device's requirements for high power and high energy density of secondary batteries, a battery pack or a battery module may be used.
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。Another example of a device may be a mobile phone, a tablet computer, a notebook computer, etc. Such a device is usually required to be thin and light, and a secondary battery may be used as a power source.
实施例Example
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。The following are examples of the present application. The examples described below are exemplary and are only used to explain the present application, and should not be construed as limiting the present application. If the specific technology or conditions are not specified, the technology or conditions described in the literature in this field or the product instructions shall be followed. If the manufacturer of the reagents or instruments is not specified, they are all conventional products that can be purchased from the market.
一、制备方法1. Preparation method
实施例1Example 1
1)粘结剂的制备1) Preparation of binder
制备A-嵌段:Preparation of A-block:
将10.5mmol的1,4-双(2-三氟甲基-4-氨基苯砜基)苯加入到500ml的三口烧瓶中,加入250ml的间甲酚,搅拌一段时间使其完全溶解后,再加入溶剂体积3%的催化剂异喹啉;将10mmol的3,3',4,4'-二苯甲酮四羧酸二酐分批次缓慢加入上述溶液中,反应体系中固含量为15%,氮气氛围下常温搅拌6小时;常温搅拌结束后,升温至180°C,氮气氛围下继续搅拌8小时;加入5mmol 2-叠氮-2-甲基丙酸,在氮气氛围下搅拌3小时后,提纯干燥,得到两端均具有叠氮基的聚酰亚胺-1,即A-嵌段。10.5 mmol of 1,4-bis(2-trifluoromethyl-4-aminophenylsulfone)benzene was added into a 500 ml three-necked flask, and 250 ml of m-cresol was added. After stirring for a period of time to completely dissolve it, 3% of the solvent volume of the catalyst isoquinoline was added. 10 mmol of 3,3',4,4'-benzophenonetetracarboxylic dianhydride was slowly added to the above solution in batches, and the solid content in the reaction system was 15%. Stirring was carried out at room temperature for 6 hours under a nitrogen atmosphere. After stirring at room temperature, the temperature was raised to 180°C and stirring was continued for 8 hours under a nitrogen atmosphere. 5 mmol of 2-azido-2-methylpropionic acid was added, and after stirring for 3 hours under a nitrogen atmosphere, the mixture was purified and dried to obtain polyimide-1 having azido groups at both ends, i.e., A-block.
其中1,4-双(2-三氟甲基-4-氨基苯砜基)苯的结构式为
The structural formula of 1,4-bis(2-trifluoromethyl-4-aminophenylsulfone)benzene is
3,3',4,4'-二苯甲酮四羧酸二酐的结构式为
The structural formula of 3,3',4,4'-benzophenone tetracarboxylic dianhydride is
制备A-嵌段的反应过程以及A-嵌段的结构式如下所示
The reaction process for preparing the A-block and the structural formula of the A-block are shown below:
其中,A4为二胺的残基,A5为二酐的残基,x为A-嵌段的聚合度。在实施例1中制备的A-嵌段聚酰亚胺-1中A4
Wherein, A4 is the residue of diamine, A5 is the residue of dianhydride, and x is the degree of polymerization of A - block.
A5 A 5 is
制备B-嵌段:Preparation of B-block:
将摩尔比为700:1:0.1的偏二氟乙烯单体、RAFT链转移剂(CTA-炔烃)和偶氮二异丁腈添加到500ml的四氢呋喃溶液中,其中RAFT链转移剂的结构式如下所示
Vinylidene fluoride monomer, RAFT chain transfer agent (CTA-alkyne) and azobisisobutyronitrile in a molar ratio of 700:1:0.1 were added to 500 ml of tetrahydrofuran solution, wherein the structural formula of the RAFT chain transfer agent is as follows:
将混合物进行至少三次冷冻-解冻循环并置于预热至80oC的油浴中。反应6小时后,通过在液氮中冷却终止反应,溶液在大量过量的甲醇中沉淀。通过过滤收集聚合物并用甲醇从氯仿中再沉淀两次。将所得产物在室温下真空干燥过夜以除去所有痕量的残留溶剂,得到末端具有炔基的聚偏二氟乙烯,即B-嵌段聚合物。The mixture was subjected to at least three freeze-thaw cycles and placed in an oil bath preheated to 80 ° C. After 6 hours of reaction, the reaction was terminated by cooling in liquid nitrogen and the solution was precipitated in a large excess of methanol. The polymer was collected by filtration and reprecipitated twice from chloroform with methanol. The resulting product was dried under vacuum at room temperature overnight to remove all traces of residual solvent to obtain polyvinylidene fluoride with alkynyl groups at the end, i.e., B-block polymer.
制备B-嵌段的反应过程如下所示,
The reaction process for preparing the B-block is shown below,
制备BAB型嵌段共聚物:Preparation of BAB type block copolymers:
将末端具有炔基的聚偏二氟乙烯、两端均具有叠氮基的聚酰亚胺和CuBr按照摩尔比1:2.5:4,添加到干燥的Schlenk管中,脱气处理后加入4ml无水N,N-二甲基甲酰胺(DMF)和0.14mmol N,N,N',N,'N”-五甲基二亚乙基三胺(PMDETA)。在60℃下搅拌反应3天,通过暴露于空气中终止反应。反应混合物通过中性氧化铝柱过滤除去铜催化剂,将溶液减压浓缩并在20倍过量的混合溶剂(甲醇与水的体积比为1:1)中进行沉淀,过滤收集产物,真空干燥得到BAB型嵌段共聚物,其作为电池粘结剂使用。Polyvinylidene fluoride with an alkynyl group at the end, polyimide with an azide group at both ends, and CuBr were added to a dry Schlenk tube in a molar ratio of 1:2.5:4. After degassing, 4 ml of anhydrous N,N-dimethylformamide (DMF) and 0.14 mmol N,N,N',N,'N"-pentamethyldiethylenetriamine (PMDETA) were added. The reaction was stirred at 60°C for 3 days and terminated by exposure to air. The reaction mixture was filtered through a neutral alumina column to remove the copper catalyst, the solution was concentrated under reduced pressure and precipitated in a 20-fold excess of a mixed solvent (the volume ratio of methanol to water was 1:1), the product was collected by filtration, and vacuum dried to obtain a BAB-type block copolymer, which was used as a battery binder.
2)正极极片的制备2) Preparation of positive electrode
将锂镍钴锰(NCM)材料、导电剂碳黑、粘结剂、N-甲基吡咯烷酮(NMP)按重量比为96.9:2.1:1:21搅拌混合均匀,得到正极浆料,浆料的固含量为73%;之后将正极浆料均匀涂覆于正极集流体上,之后经过烘干、冷压、分切,得到正极极片。Lithium nickel cobalt manganese (NCM) material, conductive agent carbon black, binder, and N-methylpyrrolidone (NMP) are stirred and mixed evenly in a weight ratio of 96.9:2.1:1:21 to obtain a positive electrode slurry with a solid content of 73%. The positive electrode slurry is then evenly coated on the positive electrode collector, and then dried, cold pressed, and cut to obtain a positive electrode sheet.
3)负极极片的制备 3) Preparation of negative electrode sheet
将活性物质人造石墨、导电剂碳黑、粘结剂丁苯橡胶(SBR)、增稠剂羟甲基纤维素钠(CMC)按照重量比为96.2:0.8:0.8:1.2溶于溶剂去离子水中,混合均匀后制备成负极浆料;将负极浆料一次或多次均匀涂覆在负极集流体铜箔上,经过烘干、冷压、分切得到负极极片。The active material artificial graphite, the conductive agent carbon black, the binder styrene-butadiene rubber (SBR), and the thickener sodium hydroxymethyl cellulose (CMC) are dissolved in the solvent deionized water in a weight ratio of 96.2:0.8:0.8:1.2, and the negative electrode slurry is prepared after being evenly mixed; the negative electrode slurry is evenly coated on the negative electrode collector copper foil once or multiple times, and the negative electrode sheet is obtained after drying, cold pressing, and slitting.
4)隔离膜4) Isolation film
以聚丙烯膜作为隔离膜。Polypropylene film is used as the isolation film.
5)电解液的制备5) Preparation of electrolyte
在氩气气氛手套箱中(H2O<0.1ppm,O2<0.1ppm),将有机溶剂碳酸乙烯酯(EC)/碳酸甲乙酯(EMC)按照体积比3/7混合均匀,加入12.5%LiPF6锂盐溶解于有机溶剂中,搅拌均匀,得到实施例1的电解液。In an argon atmosphere glove box (H 2 O<0.1ppm, O 2 <0.1ppm), organic solvents ethylene carbonate (EC)/ethyl methyl carbonate (EMC) were mixed uniformly in a volume ratio of 3/7, 12.5% LiPF 6 lithium salt was added and dissolved in the organic solvent, and stirred uniformly to obtain the electrolyte of Example 1.
6)电池的制备6) Preparation of batteries
将实施例1正极极片、隔离膜、负极极片按顺序叠好,使隔离膜处于正、负极片之间起到隔离的作用,然后卷绕得到裸电芯,给裸电芯焊接极耳,并将裸电芯装入铝壳中,并在80℃下烘烤除水,随即注入电解液并封口,得到不带电的电池。不带电的电池再依次经过静置、热冷压、化成、整形、容量测试等工序,获得实施例1的锂离子电池产品。The positive electrode sheet, the separator, and the negative electrode sheet of Example 1 are stacked in order, so that the separator is between the positive and negative electrode sheets to play an isolating role, and then wound to obtain a bare cell, and the bare cell is welded with a pole ear, and the bare cell is placed in an aluminum shell, and baked at 80°C to remove water, and then the electrolyte is injected and sealed to obtain an uncharged battery. The uncharged battery is then subjected to the processes of static, hot and cold pressing, formation, shaping, and capacity testing in sequence to obtain the lithium-ion battery product of Example 1.
实施例2~11Embodiments 2 to 11
实施例2的电池与实施例1的电池制备方法相似,但是通过调整B-嵌段的聚合反应温度和反应时间,以及A-嵌段的二酐和二胺的摩尔用量,调整B-嵌段以及A-嵌段的聚合度,调整B-嵌段以及A-嵌段的重均分子量,具体调整参数如表1所示。The battery of Example 2 is prepared in a similar manner to the battery of Example 1, but the polymerization reaction temperature and reaction time of the B-block, the molar amounts of the dianhydride and diamine of the A-block, the polymerization degrees of the B-block and the A-block, and the weight average molecular weights of the B-block and the A-block are adjusted. The specific adjustment parameters are shown in Table 1.
实施例12~15Embodiments 12 to 15
实施例12~15的电池与实施例1的电池制备方法相似,但是调整了粘结剂的质量百分比,基于正极活性材料的质量计,具体参数如表1所示。The preparation methods of the batteries of Examples 12 to 15 are similar to those of the battery of Example 1, but the mass percentage of the binder is adjusted. The specific parameters are shown in Table 1 based on the mass of the positive electrode active material.
实施例16Example 16
实施例16的电池与实施例4的电池制备方法相似,但是将二胺 单体调整为9.5mmol的1,4-双(4-氨基苯砜基)苯,使得制备的A-嵌段为仅包含砜基且两端均具有叠氮基的聚酰亚胺-2,具体参数如表1所示。The battery of Example 16 is prepared in a similar manner to the battery of Example 4, except that the diamine The monomer was adjusted to 9.5 mmol of 1,4-bis(4-aminophenylsulfone)benzene, so that the prepared A-block was polyimide-2 containing only sulfone groups and having azide groups at both ends. The specific parameters are shown in Table 1.
其中1,4-双(4-氨基苯砜基)苯的结构式如下所示,
The structural formula of 1,4-bis(4-aminophenylsulfone)benzene is shown below:
在实施例16中制备的A-嵌段聚酰亚胺-2中A4
In the A-block polyimide-2 prepared in Example 16, A4 is
A5 A 5 is
实施例17Embodiment 17
实施例17的电池与实施例4的电池制备方法相似,但是将二胺调整为9.5mmol的1,4-双(2-三氟甲基-4-氨基苯氧基)苯,使得制备的A-嵌段为只含有三氟甲基的两端均具有叠氮基的聚酰亚胺,具体参数如表1所示。The preparation method of the battery of Example 17 is similar to that of the battery of Example 4, but the diamine is adjusted to 9.5 mmol of 1,4-bis(2-trifluoromethyl-4-aminophenoxy)benzene, so that the prepared A-block is a polyimide containing only trifluoromethyl groups and having azide groups at both ends. The specific parameters are shown in Table 1.
其中1,4-双(2-三氟甲基-4-氨基苯氧基)苯的结构式如下所示
The structural formula of 1,4-bis(2-trifluoromethyl-4-aminophenoxy)benzene is shown below
在实施例17中制备的A-嵌段聚酰亚胺-3中A4A5 In the A-block polyimide-3 prepared in Example 17, A4 is A 5 is
实施例18Embodiment 18
实施例18的电池与实施例4的电池制备方法相似,但是将A-嵌段替换成两端均具有叠氮基的聚酰胺-6,具体参数如表1所示,制备方法如下所示:The preparation method of the battery of Example 18 is similar to that of the battery of Example 4, but the A-block is replaced with polyamide-6 having azide groups at both ends. The specific parameters are shown in Table 1, and the preparation method is as follows:
将含有0.3%的草酸、含有5%的乙二胺和含有85%的己内酰胺的4kg水溶液加入到5L搅拌反应釜中,通入大量氮气除去体系中的氧气,在250℃下搅拌反应24小时后,加入5mmol 4-乙酰氨基苯磺酰叠氮,在氮气氛围下搅拌3小时后,提纯干燥,得到两端均具有叠氮基的聚酰胺,即A-嵌段共聚物。4 kg of an aqueous solution containing 0.3% oxalic acid, 5% ethylenediamine and 85% caprolactam was added to a 5 L stirred reactor, and a large amount of nitrogen was introduced to remove oxygen in the system. After stirring the reaction at 250°C for 24 hours, 5 mmol 4-acetylaminobenzenesulfonyl azide was added. After stirring for 3 hours under a nitrogen atmosphere, the mixture was purified and dried to obtain a polyamide with azide groups at both ends, namely, A-block copolymer.
上述反应示意过程如下所示:
The above reaction schematic process is as follows:
实施例19Embodiment 19
实施例19的电池与实施例4的电池制备方法相似,但是将二胺调整为1,4-双(4-氨基苯氧基)苯,具体参数如表1所示。The preparation method of the battery of Example 19 is similar to that of the battery of Example 4, but the diamine is adjusted to 1,4-bis(4-aminophenoxy)benzene. The specific parameters are shown in Table 1.
其中1,4-双(4-氨基苯氧基)苯的结构式如下所示,
The structural formula of 1,4-bis(4-aminophenoxy)benzene is shown below:
在实施例19中制备的A-嵌段聚酰亚胺-4中A4A5 In the A-block polyimide-4 prepared in Example 19, A4 is A 5 is
实施例20Embodiment 20
实施例20的电池与实施例4的电池制备方法相似,但是将二酐调整为2,2'-双(三氟甲基)-3,3',4,4'-二苯甲醚四羧酸二酐,将二胺调整为4,4'-二氨基二苯醚,具体参数如表1所示。The preparation method of the battery of Example 20 is similar to that of the battery of Example 4, but the dianhydride is adjusted to 2,2'-bis(trifluoromethyl)-3,3',4,4'-diphenyl ether tetracarboxylic dianhydride, and the diamine is adjusted to 4,4'-diaminodiphenyl ether. The specific parameters are shown in Table 1.
其中2,2'-双(三氟甲基)-3,3',4,4'-二苯甲醚四羧酸二酐的结构式如下所示,
The structural formula of 2,2'-bis(trifluoromethyl)-3,3',4,4'-diphenylether tetracarboxylic dianhydride is as follows:
4,4'-二氨基二苯醚的结构如下所示,
The structure of 4,4'-diaminodiphenyl ether is shown below.
在实施例20中制备的A-嵌段聚酰亚胺-5中的A4为
A4 in the A-block polyimide-5 prepared in Example 20 is
A5为 A5
实施例21Embodiment 21
实施例21的电池与实施例4的电池制备方法相似,但是将二酐调整为2,2'-双(三氟甲基)-3,3',4,4'-二苯甲醚四羧酸二酐,将二胺调整为1,4-(双2-三氟甲基-4-氨基苯氧基)苯,具体参数如表1所示。The preparation method of the battery of Example 21 is similar to that of the battery of Example 4, but the dianhydride is adjusted to 2,2'-bis(trifluoromethyl)-3,3',4,4'-diphenylethertetracarboxylic dianhydride, and the diamine is adjusted to 1,4-(bis-2-trifluoromethyl-4-aminophenoxy)benzene. The specific parameters are shown in Table 1.
其中2,2'-双(三氟甲基)-3,3',4,4'-二苯甲醚四羧酸二酐的结构式如下所示,
The structural formula of 2,2'-bis(trifluoromethyl)-3,3',4,4'-diphenylether tetracarboxylic dianhydride is as follows:
1,4-(双2-三氟甲基-4-氨基苯氧基)苯的结构如下所示,
The structure of 1,4-(bis-2-trifluoromethyl-4-aminophenoxy)benzene is shown below.
在实施例21中制备的A-嵌段聚酰亚胺-6中的A4为
A4 in the A-block polyimide-6 prepared in Example 21 is
A5为 A5
实施例22Embodiment 22
实施例22的电池与实施例4的电池制备方法相似,但是将二胺调整为4,4'-二氨基二苯砜,具体参数如表1所示。The preparation method of the battery of Example 22 is similar to that of the battery of Example 4, but the diamine is adjusted to 4,4'-diaminodiphenyl sulfone. The specific parameters are shown in Table 1.
其中4,4'-二氨基二苯砜的结构如下所示,
The structure of 4,4'-diaminodiphenyl sulfone is shown below:
在实施例22中制备的A-嵌段聚酰亚胺-7中的A4为
A4 in the A-block polyimide-7 prepared in Example 22 is
A5为 A5
实施例23Embodiment 23
实施例23的电池与实施例4的电池制备方法相似,但是将二酐调整为3,3',4,4'-二苯基砜四羧酸二酸酐,将二胺调整为1,4-双(2-三氟 甲基-4-氨基苯酮基)苯,具体参数如表1所示。The preparation method of the battery of Example 23 is similar to that of the battery of Example 4, but the dianhydride is adjusted to 3,3',4,4'-diphenylsulfone tetracarboxylic dianhydride, and the diamine is adjusted to 1,4-bis(2-trifluoro methyl-4-aminophenone)benzene, the specific parameters are shown in Table 1.
其中3,3',4,4'-二苯基砜四羧酸二酸酐的结构如下所示,
The structure of 3,3',4,4'-diphenylsulfone tetracarboxylic acid dianhydride is shown below:
1,4-双(2-三氟甲基-4-氨基苯酮基)苯的结构如下所示,
The structure of 1,4-bis(2-trifluoromethyl-4-aminophenyl)benzene is shown below.
在实施例23中制备的A-嵌段聚酰亚胺-8中的A4为
A4 in the A-block polyimide-8 prepared in Example 23 is
A5为 A5
实施例24Embodiment 24
实施例24的电池与实施例4的电池制备方法相似,但是将二酐调整为2,2'-双(三氟甲基)-3,3',4,4'-二苯甲醚四羧酸二酐,将二胺调整为4,4'-二氨基二苯砜,具体参数如表1所示。 The preparation method of the battery of Example 24 is similar to that of the battery of Example 4, but the dianhydride is adjusted to 2,2'-bis(trifluoromethyl)-3,3',4,4'-diphenylethertetracarboxylic dianhydride, and the diamine is adjusted to 4,4'-diaminodiphenyl sulfone. The specific parameters are shown in Table 1.
其中2,2'-双(三氟甲基)-3,3',4,4'-二苯甲醚四羧酸二酐结构如下所示,
The structure of 2,2'-bis(trifluoromethyl)-3,3',4,4'-diphenylether tetracarboxylic dianhydride is shown below:
4,4'-二氨基二苯砜的结构如下所示,
The structure of 4,4'-diaminodiphenyl sulfone is shown below,
在实施例24中制备的A-嵌段聚酰亚胺-9中的A4为
A4 in the A-block polyimide-9 prepared in Example 24 is
A5为 A5
实施例25Embodiment 25
实施例25的电池与实施例4的电池制备方法相似,但是将A-嵌段替换成两端均具有叠氮基的聚酰胺-66,具体参数如表1所示,制备方法如下所示:The preparation method of the battery of Example 25 is similar to that of the battery of Example 4, but the A-block is replaced with polyamide-66 having azide groups at both ends. The specific parameters are shown in Table 1, and the preparation method is as follows:
将10.5mmol的己二胺加入到500ml的三口烧瓶中,加入250ml的间甲酚,搅拌一段时间使其完全溶解后,再加入溶剂体积3%的催化剂异喹啉;将10mmol的己二酸分批次缓慢加入上述溶液中,反应体系中固含量为15%,氮气氛围下常温搅拌6小时;常温搅拌结束 后,升温至180℃,氮气氛围下继续搅拌8小时;加入5mmol 2-叠氮-2-甲基丙酸,在氮气氛围下搅拌3小时后,提纯干燥,得到两端均具有叠氮基的聚酰胺-66,即A-嵌段。10.5 mmol of hexamethylenediamine was added to a 500 ml three-necked flask, and 250 ml of m-cresol was added. After stirring for a period of time to completely dissolve it, 3% of the solvent volume of the catalyst isoquinoline was added; 10 mmol of adipic acid was slowly added to the above solution in batches, and the solid content in the reaction system was 15%. Stirring was carried out at room temperature for 6 hours under a nitrogen atmosphere; stirring at room temperature was completed. Then, the temperature was raised to 180° C. and stirring was continued for 8 hours under a nitrogen atmosphere; 5 mmol of 2-azido-2-methylpropionic acid was added, and the mixture was stirred for 3 hours under a nitrogen atmosphere, and then purified and dried to obtain polyamide-66 having azido groups at both ends, namely, A-block.
上述反应示意过程如下所示:
The above reaction schematic process is as follows:
对比例1Comparative Example 1
对比例1的电池与实施例1的电池制备方法相似,但是粘结剂为聚偏二氟乙烯,重均分子量为120万,具体参数如表1所示,购买自索尔维集团的5130。The preparation method of the battery of Comparative Example 1 is similar to that of the battery of Example 1, but the binder is polyvinylidene fluoride with a weight average molecular weight of 1.2 million. The specific parameters are shown in Table 1 and are purchased from Solvay Group's 5130.
对比例2Comparative Example 2
对比例2的电池与实施例1的电池制备方法相似,但是粘结剂为重均分子量为120万的聚酰亚胺-1,具体参数如表1所示,制备方法与实施例1中的聚酰亚胺-1类似,只是将二胺含量调整为24mmol;将二酐含量调整为24.5mmol,其中反应体系中固含量为15%,氮气氛围下常温搅拌12小时,常温搅拌结束后,升温至180℃,氮气氛围下继续搅拌20小时,提纯干燥得到含三氟甲基和砜基的聚酰亚胺,其重均分子量为120万。The preparation method of the battery in Comparative Example 2 is similar to that of the battery in Example 1, but the binder is polyimide-1 with a weight average molecular weight of 1.2 million. The specific parameters are shown in Table 1. The preparation method is similar to that of the polyimide-1 in Example 1, except that the diamine content is adjusted to 24 mmol; the dianhydride content is adjusted to 24.5 mmol, wherein the solid content in the reaction system is 15%, and stirring is carried out at room temperature for 12 hours under a nitrogen atmosphere. After stirring at room temperature, the temperature is raised to 180°C, and stirring is continued for 20 hours under a nitrogen atmosphere. The polyimide containing trifluoromethyl and sulfone groups is purified and dried, and the weight average molecular weight thereof is 1.2 million.
对比例3Comparative Example 3
对比例3的电池与实施例1的电池制备方法相似,但是粘结剂为聚偏二氟乙烯与聚酰亚胺的共混物,具体参数如表1所示,制备方法如下:The preparation method of the battery of Comparative Example 3 is similar to that of the battery of Example 1, but the binder is a blend of polyvinylidene fluoride and polyimide. The specific parameters are shown in Table 1. The preparation method is as follows:
共混:将对比例2中的聚酰亚胺-1与对比例1中聚偏二氟乙烯按照质量比6:4进行共混,得到聚偏二氟乙烯与聚酰亚胺-1共混物粘结 剂。Blending: The polyimide-1 in comparative example 2 and the polyvinylidene fluoride in comparative example 1 were blended in a mass ratio of 6:4 to obtain a polyvinylidene fluoride and polyimide-1 blend adhesive. dose.
二、性能测试2. Performance Test
1、极片性能测试1. Pole performance test
1)膜片电阻测试1) Diaphragm resistance test
在正极极片左、中、右处裁剪烘干后的正极膜层,裁剪为3mm直径的小圆片。开启元能科技极片电阻仪电源,将其置于极片电阻仪“探头”合适位置,点击“开始”按钮,待示数稳定,读取即可。每个小圆片测试两个位置,最后计算六次测量的平均值,即为该极片的膜层电阻。Cut the dried positive electrode film layer at the left, middle and right of the positive electrode piece into small discs with a diameter of 3mm. Turn on the power of Yuanneng Technology's electrode piece resistor meter, place it in the appropriate position of the "probe" of the electrode piece resistor meter, click the "start" button, wait for the reading to stabilize, and then read it. Test two positions of each small disc, and finally calculate the average value of the six measurements, which is the film resistance of the electrode piece.
2)粘结力测试2) Adhesion test
参考GB-T2790-1995国标《胶粘剂180°剥离强度实验方法》,本申请实施例和对比例的粘结力测试过程如下:With reference to GB-T2790-1995 national standard "Adhesive 180° Peel Strength Test Method", the adhesion test process of the embodiments and comparative examples of the present application is as follows:
用刀片截取宽度为30mm,长度为100-160mm的试样,将专用双面胶贴于钢板上,胶带宽度20mm,长度90-150mm。将前面截取的极片试样的正极膜层面贴在双面胶上,后用2kg压辊沿同一个方向滚压三次。将宽度与极片等宽,长度为250mm的纸带固定于极片集流体上,并且用皱纹胶固定。打开三思拉力机电源(灵敏度为1N),指示灯亮,调整限位块到合适位置,将钢板未贴极片的一端用下夹具固定。将纸带向上翻折,用上夹具固定,利用拉力机附带的手动控制器上的“上行”和“下行”按钮调整上夹具的位置。然后进行测试并读取数值。将极片受力平衡时的力除以胶带的宽度作为单位长度的极片的粘结力,以表征正极膜层与集流体之间的粘结强度。Use a blade to cut a sample with a width of 30mm and a length of 100-160mm, and stick a special double-sided tape on the steel plate. The tape is 20mm wide and 90-150mm long. Stick the positive electrode film layer of the electrode sample cut earlier on the double-sided tape, and then roll it three times in the same direction with a 2kg roller. Fix a paper tape with a width equal to the electrode and a length of 250mm on the electrode collector and fix it with wrinkled glue. Turn on the power of the Sansi tensile machine (sensitivity is 1N), the indicator light is on, adjust the limit block to the appropriate position, and fix the end of the steel plate without the electrode with the lower clamp. Fold the paper tape upwards and fix it with the upper clamp. Use the "up" and "down" buttons on the manual controller attached to the tensile machine to adjust the position of the upper clamp. Then test and read the value. The force when the electrode is balanced divided by the width of the tape is taken as the bonding force of the electrode per unit length to characterize the bonding strength between the positive electrode film layer and the current collector.
3)极片吸液速率测试3) Electrode liquid absorption rate test
将冷压后的正极极片裁剪为边长为5厘米的正方形测试样品;首先,将样品在80℃下干燥4h,测试极片厚度后,固定在样品台上,然后挑选d=200μm的毛细管,用5000目砂纸打磨端面至平整,利用显微镜观察毛细管与极片间状态;用毛细管吸取电解液,控制电解液高度h=3mm,下降毛细管与极片接触,同时用秒表计时,当液面下降完毕后,停止计时,读取吸液时间t,记录数据;利用公式计算极片的平均吸液速率v,v=π×(d/2)2×h×ρ/t。 The cold-pressed positive electrode was cut into a square test sample with a side length of 5 cm; first, the sample was dried at 80°C for 4 h, and after the thickness of the electrode was tested, it was fixed on the sample table, and then a capillary with d = 200 μm was selected, and the end face was polished with 5000 mesh sandpaper until it was flat, and the state between the capillary and the electrode was observed under a microscope; the electrolyte was absorbed by the capillary, and the electrolyte height was controlled to h = 3 mm, and the capillary was lowered to contact the electrode, and a stopwatch was used at the same time. When the liquid level was completely lowered, the timing was stopped, the liquid absorption time t was read, and the data was recorded; the average liquid absorption rate v of the electrode was calculated using the formula, v = π × (d/2)2 × h × ρ/t.
2、电池性能测试2. Battery performance test
1)金属溶出测试1) Metal dissolution test
常温下,所制作锂离子电池以0.5C(即2小时内完全放掉理论容量的电流值)的电流进行第一次充电和放电,充电为恒流恒压充电,终止电压为4.2V,截至电流为0.05C,放电终止电压为2.8V,然后电池搁置24小时后以0.5C恒流恒压充电至4.2V,然后用1C的电流对满充电池进行放电,放电终止电压均为2.8V,电芯进行拆解,取出负极极片,采用ICP(电感耦合等离子体)法测试金属Co、Mn的沉积量。At room temperature, the prepared lithium-ion battery was charged and discharged for the first time with a current of 0.5C (i.e., the current value that completely discharges the theoretical capacity within 2 hours). The charging was constant current and constant voltage charging, the termination voltage was 4.2V, the cut-off current was 0.05C, and the discharge termination voltage was 2.8V. After the battery was left for 24 hours, it was charged to 4.2V with a constant current and constant voltage of 0.5C, and then the fully charged battery was discharged with a current of 1C. The discharge termination voltage was 2.8V. The battery cell was disassembled, the negative electrode plate was taken out, and the ICP (inductively coupled plasma) method was used to test the deposition of metal Co and Mn.
2)电池循环容量保持率测试2) Battery cycle capacity retention test
电池循环容量保持率测试过程如下:在25℃下,将制备的电池,以1/3C恒流充电至4.3V,再以4.3V恒定电压充电至电流为0.05C,搁置5分钟,再以1/3C放电至2.8V,所得容量记为初始容量C0。对上述同一个电池重复以上步骤,并同时记录循环第n次后电池的放电容量Cn,则每次循环后电池容量保持率Pn=Cn/C0*100%,以P1、P2……P500这500个点值为纵坐标,以对应的循环次数为横坐标,得到电池容量保持率与循环次数的曲线图。The test process of battery cycle capacity retention rate is as follows: at 25°C, the prepared battery is charged to 4.3V at a constant current of 1/3C, then charged to a current of 0.05C at a constant voltage of 4.3V, left for 5 minutes, and then discharged to 2.8V at 1/3C. The obtained capacity is recorded as the initial capacity C0. Repeat the above steps for the same battery, and record the discharge capacity Cn of the battery after the nth cycle at the same time. Then the battery capacity retention rate after each cycle is Pn = Cn/C0*100%, with the 500 point values of P1, P2...P500 as the vertical coordinates and the corresponding number of cycles as the horizontal coordinates, to obtain a curve graph of battery capacity retention rate and cycle number.
该测试过程中,第一次循环对应n=1、第二次循环对应n=2、……第500次循环对应n=500。表1中实施例或对比例对应的电池容量保持率数据是在上述测试条件下循环500次之后测得的数据,即P500的值。In the test process, the first cycle corresponds to n=1, the second cycle corresponds to n=2, ... the 500th cycle corresponds to n=500. The battery capacity retention rate data corresponding to the embodiments or comparative examples in Table 1 are the data measured after 500 cycles under the above test conditions, that is, the value of P500.
3)45℃下全电池容量保持率3) Full battery capacity retention rate at 45°C
以1C恒流充电至4.2V,再以4.2V恒定电压充电至电流为0.05C,搁置10分钟,然后以1C的恒定电流放电至截止电压2.8V,记录存储前容量CAP1;以1C的恒定电流充电至截止4.2V,再以4.2V恒定电压充电至电流为0.05C,将锂离子电池放置在45℃的烘箱中放置120天后,取出进行1C恒流放电至2.8V,记录存储后容量CAP2,依照如下公式计算锂离子二次电池存储容量保持率:Charge to 4.2V with a constant current of 1C, then charge to a current of 0.05C with a constant voltage of 4.2V, leave for 10 minutes, then discharge to a cut-off voltage of 2.8V with a constant current of 1C, and record the capacity before storage CAP 1 ; charge to a cut-off voltage of 4.2V with a constant current of 1C, then charge to a current of 0.05C with a constant voltage of 4.2V, place the lithium-ion battery in an oven at 45°C for 120 days, take it out and discharge to 2.8V with a constant current of 1C, record the capacity after storage CAP 2 , and calculate the storage capacity retention rate of the lithium-ion secondary battery according to the following formula:
锂离子二次电池存储容量保持率(%)=CAP2/CAP1*100%。Lithium ion secondary battery storage capacity retention rate (%) = CAP 2 /CAP 1 * 100%.
4)全电池70℃产气测试 4) Full battery 70℃ gas generation test
在70℃下,存储100%充电状态(SOC)的全电池。在存储前后及过程中测量电芯的开路电压(OCV)和交流内阻(IMP)以监控SOC,并测量电芯的体积。其中在每存储48小时后取出全电池,静置1小时后测试OCV、IMP,并在冷却至室温后用排水法测量电芯体积。排水法即先用表盘数据自动进行单位转换的天平单独测量电芯的重力F1,然后将电芯完全置于去离子水(密度已知为1g/cm3)中,测量此时的电芯的重力F2,电芯受到的浮力F浮即为F1-F2,然后根据阿基米德原理F浮=ρgV_排,计算得到电芯体积V=(F1-F2)/ρg。Full batteries with 100% state of charge (SOC) are stored at 70°C. The open circuit voltage (OCV) and AC internal resistance (IMP) of the battery cells are measured before, during and after storage to monitor the SOC, and the volume of the battery cells is measured. The full battery is taken out after every 48 hours of storage, and the OCV and IMP are tested after standing for 1 hour. The volume of the battery cells is measured by the water displacement method after cooling to room temperature. The water displacement method is to first use a balance that automatically converts units using dial data to measure the gravity F1 of the battery cell separately, and then place the battery cell completely in deionized water (density is known to be 1g/ cm3 ), and measure the gravity F2 of the battery cell at this time. The buoyancy Ffloat on the battery cell is F1-F2, and then according to the Archimedean principle Ffloat=ρgV_排, the battery cell volume V=(F1-F2)/ρg is calculated.
每次测试完体积后,对电芯进行补电,以1C的恒定电流充电至4.25V,后以4.25V恒压充电至电流降到0.05C,补电完成后入炉继续测试。After each volume test, the battery cell is recharged at a constant current of 1C to 4.25V, and then charged at a constant voltage of 4.25V until the current drops to 0.05C. After the recharging is completed, the battery cell is put into the furnace to continue testing.
存储90天后,测量电芯体积,并计算相对于存储前的电芯体积,存储后的电芯体积增加量,即产气量,产气量/电芯初始体积即得电池体积膨胀率。After 90 days of storage, the volume of the battery cells was measured, and the increase in the volume of the battery cells after storage relative to the volume of the battery cells before storage, i.e. the gas production, was calculated. The gas production/initial volume of the battery cells gave the battery volume expansion rate.
3、聚合物检测3. Polymer detection
1)重均分子量测试方法1) Weight average molecular weight test method
采用Waters 2695 Isocratic HPLC型凝胶色谱仪(示差折光检测器2141)。质量百分比为3.0%的聚苯乙烯溶液试样做参比,选择匹配的色谱柱(油性:Styragel HT5 DMF7.8*300mm+Styragel HT4)。用纯化后的N-甲基吡咯烷酮(NMP)溶剂配置3.0%的聚合物溶液,配置好的溶液静置一天,备用。测试时,先用注射器吸取四氢呋喃,进行冲洗,重复几次。然后吸取5ml实验溶液,排除注射器中的空气,将针尖擦干。最后将试样溶液缓缓注入进样口。待示数稳定后获取数据。A Waters 2695 Isocratic HPLC gel chromatograph (differential refractive index detector 2141) was used. A 3.0% polystyrene solution sample was used as a reference, and a matching chromatographic column (oily: Styragel HT5 DMF7.8*300mm+Styragel HT4) was selected. A 3.0% polymer solution was prepared with purified N-methylpyrrolidone (NMP) solvent, and the prepared solution was allowed to stand for one day for use. During the test, tetrahydrofuran was first drawn with a syringe and rinsed, and repeated several times. Then 5 ml of the experimental solution was drawn, the air in the syringe was removed, and the needle tip was wiped dry. Finally, the sample solution was slowly injected into the injection port. Data was obtained after the indication stabilized.
实施例和对比例中极片与电池的性能测试如表1和表2所示。 The performance tests of the pole pieces and the batteries in the embodiments and comparative examples are shown in Tables 1 and 2.
表1

Table 1

表2

Table 2

三、各实施例、对比例测试结果分析III. Analysis of test results of various embodiments and comparative examples
实施例1~25中粘结剂均包括BAB型嵌段共聚物,其中B-嵌段均包含衍生自偏二氟乙烯的结构单元,A-嵌段包含酰亚胺或者酰胺结构单元。以上述聚偏二氟乙烯-聚酰亚胺-聚偏二氟乙烯嵌段共聚物或聚偏二氟乙烯-聚酰胺-聚偏二氟乙烯嵌段共聚物制备的粘结剂能够降低极片的膜片电阻,提高极片的吸液速率,抑制正极活性材料中过渡金属的溶出,进而提高电池的循环性能和存储性能。The binders in Examples 1 to 25 all include BAB type block copolymers, wherein the B-blocks all include structural units derived from vinylidene fluoride, and the A-blocks include imide or amide structural units. The binders prepared with the above polyvinylidene fluoride-polyimide-polyvinylidene fluoride block copolymers or polyvinylidene fluoride-polyamide-polyvinylidene fluoride block copolymers can reduce the film resistance of the pole piece, increase the liquid absorption rate of the pole piece, inhibit the dissolution of transition metals in the positive electrode active material, and thus improve the cycle performance and storage performance of the battery.
从实施例1~6与对比例2的对比可见,相比于单独的非氟聚合物,以BAB三嵌段共聚物作为粘结剂能够提高电池的循环性能和高温存储性能。From the comparison between Examples 1 to 6 and Comparative Example 2, it can be seen that, compared with the single non-fluorinated polymer, using the BAB triblock copolymer as a binder can improve the cycle performance and high-temperature storage performance of the battery.
从实施例1~6与对比例3的对比可见,相比于非氟聚合物与含氟聚合物的简单共混,以BAB三嵌段共聚物作为粘结剂能够降低极片的膜片电阻,提高极片的粘结力,提高电池的循环性能和高温存储性能。From the comparison of Examples 1 to 6 with Comparative Example 3, it can be seen that compared with the simple blending of non-fluorinated polymers and fluorinated polymers, using BAB triblock copolymer as a binder can reduce the membrane resistance of the electrode, improve the adhesion of the electrode, and improve the cycle performance and high-temperature storage performance of the battery.
从实施例1~7与对比例1的对比可见,嵌段共聚物中,基于嵌段共聚物的总质量计,每个含氟嵌段B-嵌段的质量百分比为15%~35%,非氟嵌段A-嵌段的质量百分比为30%~70%时,BAB型嵌段共聚物能够降低极片的膜片电阻,有效抑制正极活性材料中过渡金属的溶出,提高电池的循环性能、高温存储性能,减少电池在高温下的产气量。From the comparison of Examples 1 to 7 with Comparative Example 1, it can be seen that in the block copolymer, based on the total mass of the block copolymer, when the mass percentage of each fluorine-containing block B-block is 15% to 35%, and the mass percentage of the non-fluorine block A-block is 30% to 70%, the BAB-type block copolymer can reduce the diaphragm resistance of the electrode, effectively inhibit the dissolution of transition metals in the positive electrode active material, improve the cycle performance and high-temperature storage performance of the battery, and reduce the gas production of the battery at high temperature.
从实施例1~5与实施例6~7的对比可见,嵌段共聚物中,基于嵌段共聚物的总质量计,每个含氟嵌段B-嵌段的质量百分比为17.5%~32.5%,非氟嵌段A-嵌段的质量百分比为35%~65%时,BAB型嵌段共聚物能够在降低极片的膜片电阻,提高电池的循环性能、高温存储性能的同时,进一步兼顾极片的粘结力和吸液速率,提高电池的综合性能。From the comparison between Examples 1 to 5 and Examples 6 to 7, it can be seen that in the block copolymer, based on the total mass of the block copolymer, when the mass percentage of each fluorine-containing block B-block is 17.5% to 32.5%, and the mass percentage of the non-fluorine block A-block is 35% to 65%, the BAB-type block copolymer can reduce the diaphragm resistance of the electrode, improve the cycle performance and high-temperature storage performance of the battery, while further taking into account the adhesion and liquid absorption rate of the electrode, thereby improving the overall performance of the battery.
从实施例1~11、实施例16~25和对比例1的对比可知,重均分子量为40万~200万的BAB型嵌段共聚物使得极片具有优异的吸液速率和较低的膜片电阻。另外该嵌段共聚物能够抑制正极活性材料 中过渡金属的溶出,提高电池的循环性能、高温存储性能和安全性能。From the comparison of Examples 1 to 11, Examples 16 to 25 and Comparative Example 1, it can be seen that the BAB type block copolymer with a weight average molecular weight of 400,000 to 2,000,000 enables the electrode to have an excellent liquid absorption rate and a low membrane resistance. In addition, the block copolymer can inhibit the positive electrode active material The dissolution of transition metals improves the battery's cycle performance, high-temperature storage performance and safety performance.
从实施例17与实施例19的对比可见,A-嵌段包含含有三氟甲基的酰亚胺结构单元时,该BAB型嵌段共聚物能够进一步提高极片的粘结力和吸液速率,降低过渡金属的溶出量,提高电池的循环性能和高温存储性能。From the comparison between Example 17 and Example 19, it can be seen that when the A-block contains an imide structural unit containing a trifluoromethyl group, the BAB-type block copolymer can further improve the adhesion and liquid absorption rate of the electrode, reduce the dissolution amount of transition metals, and improve the cycle performance and high-temperature storage performance of the battery.
从实施例16与实施例19的对比可见,A-嵌段包含含有砜基的酰亚胺结构单元时,该BAB型嵌段共聚物能够进一步提高极片的粘结力和吸液速率,降低过渡金属的溶出量,提高电池的循环性能和高温存储性能。From the comparison between Example 16 and Example 19, it can be seen that when the A-block contains an imide structural unit containing a sulfone group, the BAB-type block copolymer can further improve the adhesion and liquid absorption rate of the electrode, reduce the dissolution amount of transition metals, and improve the cycle performance and high-temperature storage performance of the battery.
从实施例4与实施例19的对比可见,A-嵌段包含含有三氟甲基和砜基的酰亚胺结构单元时,该BAB型嵌段共聚物能够进一步提高极片的粘结力和吸液速率,降低过渡金属的溶出量,提高电池的循环性能和高温存储性能。From the comparison between Example 4 and Example 19, it can be seen that when the A-block contains an imide structural unit containing a trifluoromethyl group and a sulfone group, the BAB-type block copolymer can further improve the adhesion and liquid absorption rate of the electrode, reduce the dissolution amount of transition metals, and improve the cycle performance and high-temperature storage performance of the battery.
从实施例1、实施例12~15可见,粘结剂的质量百分比为0.1%~3%时,基于正极活性材料的质量计时,该粘结剂使得极片具有优异的吸液速率和较低的膜片电阻,使得电池具有高的循环性能和高温存储性能。It can be seen from Examples 1 and 12 to 15 that when the mass percentage of the binder is 0.1% to 3%, based on the mass of the positive electrode active material, the binder enables the electrode to have an excellent liquid absorption rate and a lower membrane resistance, so that the battery has high cycle performance and high temperature storage performance.
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。 It should be noted that the present application is not limited to the above-mentioned embodiments. The above-mentioned embodiments are only examples, and the embodiments having the same structure as the technical idea and exerting the same effect within the scope of the technical solution of the present application are all included in the technical scope of the present application. In addition, without departing from the scope of the main purpose of the present application, various modifications that can be thought of by those skilled in the art to the embodiments and other methods of combining some of the constituent elements in the embodiments are also included in the scope of the present application.

Claims (24)

  1. 一种BAB型嵌段共聚物,其特征在于,包含A-嵌段和B-嵌段,所述B-嵌段包含式I所示的结构单元,所述A-嵌段包含式II所示的结构单元、式Ⅲ所示的结构单元、式Ⅳ所示的结构单元中的一种或多种,
    A BAB type block copolymer, characterized in that it comprises an A-block and a B-block, wherein the B-block comprises a structural unit represented by formula I, and the A-block comprises one or more of a structural unit represented by formula II, a structural unit represented by formula III, and a structural unit represented by formula IV.
    其中R1、R2、R3各自独立地选自氢、氟、至少含有一个氟原子的C1-3烷基中的一种或多种,R4选自取代或未取代的C6-25的芳香基,R5、R6、R7、R8各自独立地选自取代或未取代的C2-24烷基、取代或未取代的C6-25的芳香基。 R1 , R2 , R3 are each independently selected from one or more of hydrogen, fluorine, and C1-3 alkyl containing at least one fluorine atom; R4 is selected from substituted or unsubstituted C6-25 aromatic groups; and R5 , R6 , R7 , R8 are each independently selected from substituted or unsubstituted C2-24 alkyl groups and substituted or unsubstituted C6-25 aromatic groups.
  2. 根据权利要求1所述的BAB型嵌段共聚物,其特征在于,所述BAB型嵌段共聚物中,每个所述B-嵌段的质量百分比为15%~35%,所述A-嵌段的质量百分比为30%~70%,基于所述嵌段共聚物的总质量计。 The BAB type block copolymer according to claim 1, characterized in that, in the BAB type block copolymer, the mass percentage of each of the B-blocks is 15% to 35%, and the mass percentage of the A-block is 30% to 70%, based on the total mass of the block copolymer.
  3. 根据权利要求1或2所述的BAB型嵌段共聚物,其特征在于,所述BAB型嵌段共聚物的重均分子量为40万~200万。The BAB type block copolymer according to claim 1 or 2, characterized in that the weight average molecular weight of the BAB type block copolymer is 400,000 to 2,000,000.
  4. 根据权利要求1至3中任一项所述的BAB型嵌段共聚物,其特征在于,所述A-嵌段包含含有三氟甲基的式II所示的结构单元。The BAB type block copolymer according to any one of claims 1 to 3, characterized in that the A-block comprises a structural unit of formula II containing a trifluoromethyl group.
  5. 根据权利要求4所述的BAB型嵌段共聚物,其特征在于,所述含有三氟甲基的式II所示的结构单元包含
    The BAB type block copolymer according to claim 4, characterized in that the structural unit represented by formula II containing a trifluoromethyl group comprises
    中的一种或多种。One or more of .
  6. 根据权利要求1至5中任一项所述的BAB型嵌段共聚物,其特征在于,所述A-嵌段包含含有砜基的式II所示的结构单元。The BAB type block copolymer according to any one of claims 1 to 5, characterized in that the A-block comprises a structural unit represented by formula II containing a sulfone group.
  7. 根据权利要求6所述的BAB型嵌段共聚物,其特征在于,所述含有砜基的式II所示的结构单元包含

    The BAB type block copolymer according to claim 6, characterized in that the structural unit represented by formula II containing a sulfone group comprises

    中的一种或多种。One or more of .
  8. 根据权利要求1至7中任一项所述的BAB型嵌段共聚物,其特征在于,所述式I所示的结构单元包含衍生自偏二氟乙烯的结构单元、衍生自四氟乙烯的结构单元、衍生自氟乙烯的结构单元、衍生自三氟乙烯的结构单元、衍生自六氟丙烯的结构单元中的一种或多种。The BAB-type block copolymer according to any one of claims 1 to 7, characterized in that the structural unit represented by formula I comprises one or more of a structural unit derived from vinylidene fluoride, a structural unit derived from tetrafluoroethylene, a structural unit derived from vinyl fluoride, a structural unit derived from trifluoroethylene, and a structural unit derived from hexafluoropropylene.
  9. 根据权利要求1至8中任一项所述的BAB型嵌段共聚物,其特征在于,所述式II所示的结构单元包括The BAB type block copolymer according to any one of claims 1 to 8, characterized in that the structural unit represented by formula II comprises
    中的一种或多种,其中n为6-12之间的任意整数。 One or more of , wherein n is any integer between 6 and 12.
  10. 一种BAB型嵌段共聚物的制备方法,其特征在于,包括以下步骤:A method for preparing a BAB type block copolymer, characterized in that it comprises the following steps:
    制备B-嵌段:将至少一种式Ⅴ所示单体聚合制备B-嵌段,
    Preparation of B-block: polymerizing at least one monomer represented by formula V to prepare B-block,
    其中A1、A2、A3各自独立地选自氢、氟、至少含有一个氟原子的C1-3烷基中的一种或多种;wherein A 1 , A 2 , and A 3 are each independently selected from one or more of hydrogen, fluorine, and a C 1-3 alkyl group containing at least one fluorine atom;
    制备A-嵌段:将至少一种二元胺与至少一种二元酐或至少一种二元酸聚合制备A-嵌段,或者将内酰胺单体开环聚合制备A-嵌段;Preparation of A-block: polymerizing at least one diamine with at least one dibasic anhydride or at least one dibasic acid to prepare A-block, or ring-opening polymerization of lactam monomer to prepare A-block;
    制备BAB型嵌段共聚物:将所述B-嵌段和所述A-嵌段接合制备BAB型嵌段共聚物。Preparation of BAB type block copolymer: The B-block and the A-block are joined to prepare a BAB type block copolymer.
  11. 根据权利要求10所述BAB型嵌段共聚物的制备方法,其特征在于,所述制备B-嵌段具体包括:The method for preparing a BAB type block copolymer according to claim 10, characterized in that the preparation of the B-block specifically comprises:
    将至少一种式Ⅴ所示单体、链转移剂和引发剂在70~90℃的反应温度下通过可逆加成-裂解链转移聚合,反应5~8.5小时得到单端具有叠氮基团或炔基的B-嵌段。At least one monomer represented by formula V, a chain transfer agent and an initiator are subjected to reversible addition-fragmentation chain transfer polymerization at a reaction temperature of 70 to 90° C. for 5 to 8.5 hours to obtain a B-block having an azide group or an alkynyl group at one end.
  12. 根据权利要求10或11所述BAB型嵌段共聚物的制备方法,其特征在于,所述制备A-嵌段具体包括:The method for preparing a BAB type block copolymer according to claim 10 or 11, characterized in that the preparation of the A-block specifically comprises:
    将催化剂、至少一种二元胺和至少一种二元酐或至少一种二元酸在室温下搅拌反应4~10小时,升温至170~210℃反应5~20小时, 得到两端的端基均为酸酐、羧基或氨基的产物;The catalyst, at least one diamine and at least one dibasic anhydride or at least one dibasic acid are stirred and reacted at room temperature for 4 to 10 hours, and then heated to 170 to 210° C. for 5 to 20 hours. A product is obtained in which both end groups are anhydride, carboxyl or amino;
    对产物的端基进行官能化反应,得到两端均具有炔基或叠氮基团的所述A-嵌段。The terminal groups of the product are subjected to functionalization reaction to obtain the A-block having alkynyl groups or azide groups at both ends.
  13. 根据权利要求10或11所述BAB型嵌段共聚物的制备方法,其特征在于,所述制备A-嵌段具体包括:The method for preparing a BAB type block copolymer according to claim 10 or 11, characterized in that the preparation of the A-block specifically comprises:
    将端基调节剂、水和至少一种内酰胺单体在250℃~280℃的反应温度下聚合反应12~24小时,得到两端的端基均为羧基或氨基的产物;Polymerizing an end group regulator, water and at least one lactam monomer at a reaction temperature of 250° C. to 280° C. for 12 to 24 hours to obtain a product having end groups at both ends being carboxyl or amino groups;
    对产物的端基进行官能化反应,得到两端均具有炔基或叠氮基团的所述A-嵌段。The terminal groups of the product are subjected to functionalization reaction to obtain the A-block having alkynyl groups or azide groups at both ends.
  14. 根据权利要求10至13中任一项所述BAB型嵌段共聚物的制备方法,其特征在于,所述制备BAB型嵌段共聚物具体包括:The method for preparing the BAB type block copolymer according to any one of claims 10 to 13, characterized in that the preparation of the BAB type block copolymer specifically comprises:
    将两端均具有炔基或叠氮基团的所述A-嵌段与单端具有叠氮基团或炔基的所述B-嵌段混合,进行点击反应,制备BAB型嵌段共聚物,其中所述B-嵌段和所述A-嵌段的端基不同。The A-block having alkynyl or azide groups at both ends and the B-block having an azide or alkyne group at one end are mixed and subjected to a click reaction to prepare a BAB type block copolymer, wherein the terminal groups of the B-block and the A-block are different.
  15. 根据权利要求11至14中任一项所述BAB型嵌段共聚物的制备方法,其特征在于,所述链转移剂为含末端炔基或叠氮基团的RAFT链转移剂。The method for preparing a BAB type block copolymer according to any one of claims 11 to 14, characterized in that the chain transfer agent is a RAFT chain transfer agent containing a terminal acetylenic group or an azide group.
  16. 根据权利要求13至15中任一项所述BAB型嵌段共聚物的制备方法,其特征在于,所述端基调节剂为二元胺或二元酸。The method for preparing a BAB type block copolymer according to any one of claims 13 to 15, characterized in that the terminal group regulator is a diamine or a dibasic acid.
  17. 权利要求1至9中任一项所述的BAB型嵌段共聚物在二次电池中的应用。Use of the BAB type block copolymer according to any one of claims 1 to 9 in a secondary battery.
  18. 根据权利要求17所述的应用,其特征在于,所述二次电池 包括锂离子电池、钠离子电池、镁离子电池、钾离子电池中的至少一种。The use according to claim 17, characterized in that the secondary battery It includes at least one of a lithium ion battery, a sodium ion battery, a magnesium ion battery, and a potassium ion battery.
  19. 一种正极极片,其特征在于,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,所述正极膜层包括正极活性材料、导电剂和粘结剂,所述粘结剂为权利要求1至9中任一项所述的BAB型嵌段共聚物或权利要求10至16中任一项所述的制备方法制备的BAB型嵌段共聚物。A positive electrode plate, characterized in that it includes a positive electrode current collector and a positive electrode film layer arranged on at least one surface of the positive electrode current collector, the positive electrode film layer includes a positive electrode active material, a conductive agent and a binder, and the binder is a BAB type block copolymer as described in any one of claims 1 to 9 or a BAB type block copolymer prepared by the preparation method as described in any one of claims 10 to 16.
  20. 根据权利要求19所述的正极极片,其特征在于,所述粘结剂的质量百分比为0.1%~3%,基于所述正极活性材料的总质量计。The positive electrode sheet according to claim 19 is characterized in that the mass percentage of the binder is 0.1% to 3%, based on the total mass of the positive electrode active material.
  21. 根据权利要求19或20所述的正极极片,其特征在于,所述正极膜层与所述正极集流体间单位长度的粘结力不小于11.5N/m,可选为11.5-15N/m。The positive electrode plate according to claim 19 or 20 is characterized in that the bonding force per unit length between the positive electrode film layer and the positive electrode current collector is not less than 11.5 N/m, and can be optionally 11.5-15 N/m.
  22. 根据权利要求19至21中任一项所述的正极极片,其特征在于,所述正极极片对电解液的吸液速率大于0.31μg/s,可选为0.32-0.5μg/s,所述电解液的密度为1.1-1.2g/cm3The positive electrode plate according to any one of claims 19 to 21, characterized in that the electrolyte absorption rate of the positive electrode plate is greater than 0.31 μg/s, and can be 0.32-0.5 μg/s, and the electrolyte density is 1.1-1.2 g/cm 3 .
  23. 一种二次电池,其特征在于,包括电极组件和电解液,所述电极组件包括隔离膜、负极极片和权利要求19至23中任一项所述的正极极片。A secondary battery, characterized in that it comprises an electrode assembly and an electrolyte, wherein the electrode assembly comprises a separator, a negative electrode sheet and a positive electrode sheet according to any one of claims 19 to 23.
  24. 一种用电装置,其特征在于,包括权利要求23所述的二次电池。 An electrical device, characterized by comprising the secondary battery as claimed in claim 23.
PCT/CN2023/096928 2022-09-30 2023-05-29 Bab type block copolymer, preparation method, binder, positive electrode plate, secondary battery, and electric device WO2024066422A1 (en)

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