Patent Application
20240380072
This application relates to the field of battery technologies, and in particular, to a binder and a preparation method thereof, and a separator, an electrode assembly, a battery cell, a battery, and an electric apparatus.
With the rapid growth of portable electronic devices, electric vehicles, and the like, the demand for traction batteries is also increasing constantly. Electrochemical performance of batteries is also attracting more and more attention.
Currently, battery cells are having an opening issue. To be specific, gaps are easily formed between electrode plates and the separator, resulting in deteriorated cycling performance of batteries.
This application is mainly intended to provide a binder, so as to increase adhesion force between a separator and an electrode plate by the binder, thus improving cycling performance of batteries.
To achieve the above objectives, this application proposes a binder. The binder includes a capsule and a core material provided in the capsule, where the capsule includes an organic polymer, and the core material includes a plasticizer.
The binder of this application includes a capsule and a core material provided in the capsule, where the capsule includes an organic polymer, and the core material includes a plasticizer. The plasticizer is encapsulated as the core material inside the capsule of the organic polymer to improve adhesion performance of the organic polymer, so as to increase adhesion force between a separator and an electrode plate by the binder.
Optionally, a mass ratio of the core material to the capsule is 1:(10-100), optionally 1:(20-90).
In the capsule-shaped binder, the main adhesion is still provided by the capsule. In addition, to avoid rupture of the capsule, mass of the capsule is designed to be greater than that of the core material so as to guarantee stability of the capsule structure and adhesion. The mass ratio of the core material to the capsule is 1:(10-100), where in 1:(10-100), the values include minimum and maximum values of the range and each value between such minimum and maximum values. Specific examples include but are not limited to point values in the embodiments and 1:10, 1:20, 1:30, 1:40, 1:50, 1:60, 1:70, 1:80, 1:90, 1:100, and the like.
Optionally, the mass ratio of the core material to the capsule is 1:(20-90).
In 1:(20-90), the values include minimum and maximum values of the range and each value between such minimum and maximum values. Specific examples include but are not limited to point values in the embodiments and 1:20, 1:30, 1:40, 1:50, 1:60, 1:70, 1:80, 1:90, and the like.
Optionally, a median particle size by volume Dv50 of the binder is 0.5 μm-100 μm, optionally 7 μm-8 μm.
Theoretically, the median particle size by volume Dv50 of the binder in this application may be less than 0.5 μm or greater than 100 μm. However, considering that the binder in this application is used on a separator, the median particle size by volume Dv50 of the binder can be neither excessively large nor excessively small. Excessively small binder is prone to block pores of a separator and reduce passage of lithium ions through the separator; and excessively large binder, when applied on a separator, may lead to formation of a thicker coating, affecting energy density of the subsequently prepared battery. Therefore, the median particle size by volume Dv50 of the binder is 0.5 μm-100 μm, where in 0.5 μm-100 μm, the values include minimum and maximum values of the range and each value between such minimum and maximum values. Specific examples include but are not limited to point values in the embodiments and 0.5 μm, 1 μm, 5 μm, 10 μm, 15 μm, 20 μm, 25 μm, 30 μm, 35 μm, 40 μm, 45 μm, 50 μm, 60 μm, 70 μm, 80 μm, 90 μm, 100 μm, and the like.
Optionally, the median particle size by volume Dv50 of the binder is 7 μm-8 μm.
When the median particle size by volume Dv50 of the binder is 7 μm-8 μm, the obtained separator features good performance. In 7 μm-8 μm, the values include minimum and maximum values of the range and each value between such minimum and maximum values. Specific examples include but are not limited to point values in the embodiments and 7 μm, 7.5 μm, 8 μm, and the like.
Optionally, the capsule includes at least one of polyacrylate polymer and urea-formaldehyde resin.
The capsule in this application is required to have adhesion performance. Polyacrylate polymer and urea-formaldehyde resin have good adhesion, and therefore can provide better adhesion when used as the capsule. Certainly, a material of the capsule in this application is not limited, and other materials with good adhesion and stability can be applied to this application.
Optionally, constituent monomers of the polyacrylate polymer include a first polymeric flexible monomer, a second polymeric polar monomer, and a third polymeric molecular weight regulating monomer.
In this application, the constituent monomers of the polyacrylate polymer include the first polymeric flexible monomer, the second polymeric polar monomer, and the third polymeric molecular weight regulating monomer, and the polymer is obtained through a crosslinking reaction of the three monomers. Molecular weight and glass transition temperature of the polymer can be controlled to improve the adhesion performance of the binder.
Optionally, a molar ratio of the first polymeric flexible monomer, the second polymeric polar monomer, and the third polymeric molecular weight regulating monomer is 1:(0.01-0.8):(0.01-0.15), optionally 1:(0.05-0.7):(0.05-0.12).
When the molar ratio of the first polymeric flexible monomer, the second polymeric polar monomer, and the third polymeric molecular weight regulating monomer is 1:(0.01-0.8):(0.01-0.15), the binder features good adhesion. In 1:(0.01-0.8):(0.01-0.15), the values include minimum and maximum values of the range and each value between such minimum and maximum values. Specific examples include but are not limited to point values in the embodiments and 1:0.01:0.01, 1:0.1:0.01, 1:0.4:0.01, 1:0.8:0.01, 1:0.01:0.05, 1:0.01:0.1, 1:0.01:0.15, 1:0.1:0.01, 1:0.1:0.05, 1:0.1:0.15, 1:0.4:0.01, 1:0.4:0.05, 1:0.4:0.15, 1:0.8:0.01, 1:0.8:0.05, 1:0.8:0.15, and the like.
Optionally, the molar ratio of the first polymeric flexible monomer, the second polymeric polar monomer, and the third polymeric molecular weight regulating monomer is 1:(0.05-0.7):(0.05-0.12).
When the molar ratio of the first polymeric flexible monomer, the second polymeric polar monomer, and the third polymeric molecular weight regulating monomer is 1:(0.05-0.7):(0.05-0.12), the binder features good adhesion. In 1:(0.05-0.7):(0.05-0.12), the values include minimum and maximum values of the range and each value between such minimum and maximum values. Specific examples include but are not limited to point values in the embodiments and 1:0.05:0.05, 1:0.1:0.05, 1:0.4:0.05, 1:0.7:0.05, 1:0.1:0.05, 1:0.1:0.1, 1:0.1:0.12, and the like.
Optionally, the first polymeric flexible monomer contains an ester bond in structure, the second polymeric polar monomer contains a cyano group in structure, and the third polymeric molecular weight regulating monomer contains an amide bond.
The ester bond can improve flexibility of a molecular chain, the cyano group can improve the polarity of the monomer, and the amide bond has polarity and can easily form a hydrogen bond, which can improve adhesion. The first polymeric flexible monomer contains the ester bond in structure, the second polymeric polar monomer contains the cyano group in structure, and the third polymeric molecular weight regulating monomer contains the amide bond, so that with the polymer obtained by polymerization of the above three monomers, the molecular weight and glass transition temperature of the polymer can be controlled to improve the adhesion performance of the binder.
Optionally, the first polymeric flexible monomer is an acrylate monomer, the second polymeric polar monomer is an acrylonitrile monomer, and the third polymeric molecular weight regulating monomer is an acrylamide monomer.
The acrylate monomer can improve swelling resistance of the polymer, and as a flexible monomer chain segment in a molecular chain segment, can regulate the glass transition temperature of the polymer and improve toughness of the binder when applied, thereby facilitating good adhesion.
The acrylonitrile monomer has a cyano group with strong polarity, conducive to improving ionic conductivity and improving adhesion.
The acrylamide monomer regulates the molecular weight and also features good adhesion.
With the polymer prepared using the above three types of monomers, the molecular weight and glass transition temperature of the polymer can be controlled to improve the adhesion performance of the binder.
Optionally, the acrylate monomer includes at least one of methyl acrylate, ethyl acrylate, n-butyl acrylate, isobutyl acrylate, sec-butyl acrylate, tert-butyl acrylate, n-propyl acrylate, cyclohexyl acrylate, lauryl acrylate, 2-ethylhexyl acrylate, 2-hydroxyethyl acrylate, 2-hydroxypropyl acrylate, methyl methacrylate, ethyl methacrylate, n-butyl methacrylate, 2-ethylhexyl methacrylate, isobornyl methacrylate, lauryl methacrylate, 2-hydroxyethyl methacrylate, and 2-hydroxypropyl methacrylate;
Based on the fact that the acrylate monomer helps improve the adhesion of the binder, the acrylate monomer may include at least one of methyl acrylate, ethyl acrylate, n-butyl acrylate, isobutyl acrylate, sec-butyl acrylate, tert-butyl acrylate, n-propyl acrylate, cyclohexyl acrylate, lauryl acrylate, 2-ethylhexyl acrylate, 2-hydroxyethyl acrylate, 2-hydroxypropyl acrylate, methyl methacrylate, ethyl methacrylate, n-butyl methacrylate, 2-ethylhexyl methacrylate, isobornyl methacrylate, lauryl methacrylate, 2-hydroxyethyl methacrylate, and 2-hydroxypropyl methacrylate. To be specific, the constituent monomers of the polyacrylate polymer may include one of the above acrylate monomers, or may include more than one of the above acrylate monomers, which is not specifically limited.
Based on the fact that the acrylonitrile monomer helps improve the adhesion of the binder, the acrylonitrile monomer includes at least one of acrylonitrile and methacrylonitrile. To be specific, the constituent monomers of the polyacrylate polymer may include one of the above acrylonitrile monomers, or may include more than one of the above acrylonitrile monomers, which is not specifically limited.
Based on the fact that the acrylamide monomer helps improve the adhesion of the binder, the acrylamide monomer includes at least one of acrylamide, N-methylolacrylamide, and N-butoxymethylacrylamide. To be specific, the constituent monomers of the polyacrylate polymer may include one of the above acrylamide monomers, or may include more than one of the above acrylamide monomers, which is not specifically limited.
Optionally, the plasticizer includes at least one of dibutyl phthalate, dioctyl adipate, dibutyl sebacate, dioctyl sebacate, and dibutyl adipate.
The core material is a plasticizer material, and the plasticizer may be a commonly used plasticizer, a specific type of which is not limited. For example, the core material includes at least one of dibutyl phthalate, dioctyl adipate, dibutyl sebacate, dioctyl sebacate, and dibutyl adipate.
This application provides a preparation method of binder including the following steps:
In this application, the capsule-shaped binder is obtained through emulsion polymerization. The prepolymer of the capsule and the emulsion of the core material are first prepared separately, then the prepolymer and the initiator are added dropwise into the emulsion, and the mixture is heated for reaction, so that the prepolymer of the capsule forms the polymer on a surface of the core material to obtain the capsule-shaped binder.
Optionally, the organic polymer includes at least one of polyacrylate polymer and urea-formaldehyde resin.
A type of the organic polymer in this application is not limited, and the organic polymer is required to have adhesion. For example, the organic polymer may be polyacrylate polymer or urea-formaldehyde resin.
Optionally, a mass ratio of the plasticizer to the constituent monomers of the organic polymer is 1:(10-100), optionally 1:(20-90).
In the capsule-shaped binder, the main adhesion is still provided by the capsule. In addition, to avoid rupture of the capsule, mass of the capsule is designed to be greater than that of the core material so as to guarantee stability of the capsule structure and adhesion. A mass ratio of the core material to the capsule is 1:(10-100), where in 1:(10-100), the values include minimum and maximum values of the range and each value between such minimum and maximum values. Specific examples include but are not limited to point values in the embodiments and 1:10, 1:20, 1:30,1:40, 1:50, 1:60, 1:70, 1:80, 1:90, 1:100, and the like.
Optionally, the mass ratio of the plasticizer to the constituent monomers of the organic polymer is 1:(20-90).
In 1:(20-90), the values include minimum and maximum values of the range and each value between such minimum and maximum values. Specific examples include but are not limited to point values in the embodiments and 1:20, 1:30, 1:40, 1:50, 1:60, 1:70, 1:80, 1:90, and the like.
An embodiment of this application provides a separator, where the separator is provided with the foregoing binder or a binder prepared by using the foregoing preparation method of binder.
The separator being coated with the foregoing binder can improve adhesion performance between an electrode plate and the binder, and alleviate the opening issue in an existing pre-cold pressing process for battery cells.
An embodiment of this application provides an electrode assembly, where the electrode assembly includes the foregoing separator.
The electrode assembly includes a positive electrode plate, a negative electrode plate, and a separator. The binder is applied on the separator to adhere the electrode plates and the separator together, so as to alleviate the opening issue for electrode plates and separators.
An embodiment of this application provides a battery cell, where the battery cell includes the foregoing electrode assembly.
The foregoing electrode assembly being applied to the battery cell can improve large-clamp cycling performance of the battery cell.
An embodiment of this application provides a battery, where the battery includes the foregoing battery cell.
An embodiment of this application provides an electric apparatus, where the electric apparatus includes the foregoing battery cell or battery.
To describe the technical solutions of the embodiments of this application more clearly, the following briefly describes the accompanying drawings required for describing the embodiments or the prior art. Apparently, the accompanying drawings in the following descriptions show merely some embodiments of this application, and persons of ordinary skill in the art may still derive other drawings from the accompanying drawings without creative efforts.
The achievement of the objectives, functional features, and advantages of this application are further described in connection with the embodiments and with reference to the accompanying drawings.
The following clearly and completely describes the technical solutions in the embodiments of this application with reference to the accompanying drawings in the embodiments of this application. Apparently, the described embodiments are some but not all embodiments of this application. All other embodiments obtained by persons of ordinary skill in the art based on the embodiments of this application without creative efforts shall fall within the protection scope of this application.
The following specifically discloses in detail embodiments of the binder and preparation method thereof, and the separator, electrode assembly, battery cell, battery, and electric apparatus containing such binder of this application, with appropriate reference to the accompanying drawings. However, there may be cases where unnecessary detailed descriptions are omitted. For example, detailed descriptions of well-known matters and repeated descriptions of actually identical structures have been omitted. This is to avoid unnecessarily prolonging the following description, for ease of understanding by persons skilled in the art. In addition, the accompanying drawings and the following descriptions are provided for persons skilled in the art to fully understand this application and are not intended to limit the subject matter recorded in the claims.
“Ranges” disclosed in this application are defined in the form of lower and upper limits. A given range is defined by one lower limit and one upper limit selected, where the selected lower and upper limits define boundaries of that particular range. Ranges defined in this method may or may not include end values, and any combinations may be used, meaning any lower limit may be combined with any upper limit to form a range. For example, if ranges of 60-120 and 80-110 are provided for a specific parameter, it should be understood that ranges of 60-110 and 80-120 can also be envisioned. In addition, if minimum values of a range are given as 1 and 2, and maximum values of the range are given as 3, 4, and 5, the following ranges can all be envisioned: 1-3, 1-4, 1-5, 2-3, 2-4, and 2-5. In this application, unless otherwise stated, a value range of “a-b” is a short representation of any combination of real numbers between a and b, where both a and b are real numbers. For example, a value range of “0-5” means that all real numbers from “0-5” are listed herein, and “0-5” is just an abbreviated representation of a combination of these values. In addition, when a parameter is expressed as an integer greater than or equal to 2, this is equivalent to disclosure that the parameter is, for example, an integer: 2, 3, 4, 5, 6, 7, 8, 9, 10, 11, or 12.
Unless otherwise specified, all the embodiments and optional embodiments of this application can be combined with each other to form new technical solutions.
Unless otherwise specified, all the technical features and optional technical features of this application can be combined with each other to form new technical solutions.
Unless otherwise specified, all the steps in this application can be performed in the order described or in random order, preferably, in the order described. For example, a method including steps (a) and (b) indicates that the method may include steps (a) and (b) performed in order or may include steps (b) and (a) performed in order. For example, the foregoing method may further include step (c), which indicates that step (c) may be added to the method in any ordinal position, for example, the method may include steps (a), (b), and (c), steps (a), (c), and (b), steps (c), (a), and (b), or the like.
Unless otherwise specified, “include” and “contain” mentioned in this application are inclusive or may be exclusive. For example, the terms “include” and “contain” can mean that other unlisted components may also be included or contained, or only listed components are included or contained.
Unless otherwise specified, 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 one of the following conditions satisfies the condition “A or B”: A is true (or present) and B is false (or not present); A is false (or not present) and B is true (or present); or both A and B are true (or present).
A lithium-ion battery is formed by four parts: a positive electrode material, a negative electrode material, an electrolyte, and a separator. The separator is a functional film material of a microporous structure, is generally 8 μm-40 μm thick, and in a battery system, plays the role of separating positive and negative electrodes, blocking passage of electrons in a circuit during charging and discharging, and allowing free passage of lithium ions in the electrolyte. The separator can selectively close its micropores in a case of charging and discharging or temperature rise of the battery to limit excessively large current and prevent short circuits. Performance of the separator directly determines overall performance of the battery. Conventional lithium-ion battery separators are polyolefin separators, and are mostly single-layer or three-layer structures, for example, single-layer PE, single-layer PP, and PP/PE/PP composite film. However, conventional lithium-ion battery separators are non-polar, have poor adhesion when directly adhered to positive and negative electrode plates, and are typically coated with a binder on surface for adhesion. A commonly used binder is polyvinylidene fluoride, and this polymer is homopolymer with a crystallinity of about 50%. The relatively high crystallinity leads to insufficient adhesion force between the separator and positive and negative electrode plates, which often results in the opening issue for battery cells; and also leads to poor electrolyte infiltration, such that requirements for coated separator performance of traction lithium-ion batteries cannot be satisfied.
A battery cell is formed by adhering positive and negative electrode plates and a separator, and the battery cell has certain hardness. To be specific, the adhered positive and negative electrode plates and the separator are attached to and support each other to form a structure with a certain thickness, and this structure with a certain thickness has certain hardness. The negative electrode swells during charging and discharging, and if adhesion force is poor, a gap will be formed between the positive and negative electrode plates and the separator, such that the positive and negative electrode plates and the separator cannot be attached to and support each other, leading to a loose battery cell with decreased hardness. In this case, kinetic performance of the battery cell is deteriorated, for example, rate performance is deteriorated; and cycling performance is also deteriorated. For example, in an electric vehicle, a loose battery cell in a battery leads to slower charging speed and deteriorated cycling performance of the battery, directly resulting in shorter service life of the battery, frequent battery replacement for the electric vehicle, and increased costs for a consumer on the electric vehicle.
In view of this, this application provides a binder, where the binder includes a capsule and a core material provided in the capsule, the capsule including an organic polymer, and the core material including a plasticizer.
The organic polymer is a polymer obtained by polymerization of organic monomers, and in this application, it refers to an organic polymer with adhesion.
The binder refers to a material with adhesion performance for adhering different substances together.
A capsule structure refers to an encapsulation structure for encapsulating content. As shown in
For the plasticizer, the main function of the plasticizer is to weaken secondary bonds between polymer molecules, increase mobility of resin molecular chains, reduce crystallinity of resin molecules, and increase plasticity of resin molecules, thereby enhancing flexibility thereof. Addition of the plasticizer, as a type of substance that can improve physical properties of polymers, can reduce forces between polymer molecular chains, lowering glass transition temperature, flow temperature, and melting point of microcrystals contained for polymers. The plasticizer can improve plasticity of resin, making products soft and resistant to low temperature.
In this application, the capsule structure is used to encapsulate the plasticizer core material to obtain the capsule-structured binder. This improves overall flexibility of the capsule-structured binder and thus improves adhesion performance of the binder, so as to increase adhesion force between a separator and an electrode plate by the binder. The binder of this application provides good adhesion performance, such that swelling of an electrode plate does not lead to separation of the electrode plate from a separator, avoiding problems such as the opening issue for a battery cell, also allowing good hardness maintained for the battery cell, and thus improving kinetic performance and cycling performance of the battery cell.
For example, during pre-cold pressing of the battery cell, due to improved flexibility of the binder, the binder can fully penetrate into gaps between positive and negative electrode plates and the separator. To be specific, gaps are present between the electrode plates and the separator, and the binder penetrates into the gaps so that the electrode plates and the separator are effectively connected, and it is difficult for the binder to come out of the gaps. During swelling of the electrode plates, the binder has toughness, and therefore the binder can still effectively connect the two during swelling. This can make full use of the adhesion performance of the binder, and in turn helps improve kinetic performance and large-clamp cycling performance of a battery.
In this application, compared with the plasticizer being directly added inside the organic polymer, the plasticizer being provided inside the capsule of the organic polymer can boost even distribution of the plasticizer. For example, the plasticizer being put among monomers of the organic polymer for polymerization may lead to uneven dispersion of the plasticizer inside the organic polymer, and this mixed polymerized binder being applied to a separator, in the case of uneven dispersion of the plasticizer, may lead to good flexibility in some parts of the separator and poor flexibility in other parts, such that overall performance of the separator is unstable. By contrast, preparation of capsule-structured binder can result in a binder having a capsule structure containing relatively uniform plasticizer core material, improving the overall performance of the binder and facilitating application of the binder to the separator to improve the overall performance of the separator.
Before the binder is applied onto the separator, the binder needs to be pre-mixed with other raw materials. The pre-mixed raw materials are aqueous systems, while the plasticizer is an oily substance, so the plasticizer being exposed leads to poor mixing and dispersion, poor uniformity of mixing, poor uniformity of the materials applied on the separator, and poor performance of the separator. Therefore, the plasticizer being accommodated inside the capsule as the core material not only facilitates the pre-mixing operation but also improves the overall performance of the separator.
In some embodiments, a mass ratio of the core material to the capsule is 1:(10-100), optionally 1:(20-90).
In the capsule-shaped binder, the main adhesion is still provided by the capsule. In addition, to avoid rupture of the capsule, mass of the capsule is designed to be greater than that of the core material so as to guarantee stability of the capsule structure and adhesion. The mass ratio of the core material to the capsule is 1:(10-100), where in 1:(10-100), the values include minimum and maximum values of the range and each value between such minimum and maximum values. Specific examples include but are not limited to point values in the embodiments and 1:10, 1:20, 1:30, 1:40, 1:50, 1:60, 1:70, 1:80, 1:90, 1:100, and the like.
For a mass ratio test method, during preparation of the binder, mass of monomers put during reaction for preparation of a core layer structure is recorded as m, mass of monomers used for preparation of a shell layer structure is recorded as n, and then a mass ratio of the core layer structure to the shell layer structure is m:n.
In some embodiments, the mass ratio of the core material to the capsule is 1:(20-90).
In 1:(20-90), the values include minimum and maximum values of the range and each value between such minimum and maximum values. Specific examples include but are not limited to point values in the embodiments and 1:20, 1:30, 1:40, 1:50, 1:60, 1:70, 1:80, 1:90, and the like.
In some embodiments, a median particle size by volume Dv50 of the binder is 0.5 μm-50 μm.
The median particle size by volume Dv50 of the binder may be measured by using a common method in the art. For example, it may be measured in accordance with GB/T 19077-2016 by using a Malvern laser particle size analyzer, for example, using an instrument such as Mastersizer-3000 from Malvern.
In some embodiments, the median particle size by volume Dv50 of the binder is 0.5 μm-100 μm, optionally 7 μm-8 μm.
Theoretically, the median particle size by volume Dv50 of the binder in this application may be less than 0.5 μm or greater than 100 μm. However, considering that the binder in this application is used on a separator, the median particle size by volume Dv50 of the binder can be neither excessively large nor excessively small. Excessively small binder is prone to block pores of a separator and reduce passage of lithium ions through the separator; and excessively large binder, when applied on a separator, may lead to formation of a thicker coating, affecting energy density of the subsequently prepared battery. Therefore, the median particle size by volume Dv50 of the binder is 0.5 μm-100 μm, where in 0.5 μm-100 μm, the values include minimum and maximum values of the range and each value between such minimum and maximum values. Specific examples include but are not limited to point values in the embodiments and 0.5 μm, 1 μm, 5 μm, 10 μm, 15 μm, 20 μm, 25 μm, 30 μm, 35 μm, 40 μm, 45 μm, 50 μm, 60 μm, 70 μm, 80 μm, 90 μm, 100 μm, and the like.
In some embodiments, the median particle size by volume Dv50 of the binder is 7 μm-8 μm.
When the median particle size by volume Dv50 of the binder is 7 μm-8 μm, the obtained separator features good performance. In 7 μm-8 μm, the values include minimum and maximum values of the range and each value between such minimum and maximum values. Specific examples include but are not limited to point values in the embodiments and 7 μm, 7.5 μm, 8 μm, and the like.
In some embodiments, the capsule includes at least one of polyacrylate polymer and urea-formaldehyde resin.
Polyacrylate polymer is a polymer with acrylates as monomers.
Urea-formaldehyde resin is initial urea-formaldehyde resin formed by condensation of urea and formaldehyde under the action of a catalyst (an alkaline or acidic catalyst).
The capsule in this application is required to have adhesion performance. Polyacrylate polymer has good adhesion, and therefore can provide better adhesion when used as the capsule. Certainly, a material of the capsule in this application is not limited, and other materials with good adhesion and stability can be applied to this application.
A polymer capsule is prepared by encapsulating the plasticizer through at least one of polyacrylate polymer and urea-formaldehyde resin, which can make full use of a synergistic effect of the two. The polymer capsule is applied onto a separator, which improves pre-cold pressing adhesion force between the separator and positive and negative electrode plates and avoids problems such as the opening issue for a battery cell. In addition, the binder is applied onto the separator which is in turn applied to a lithium-ion battery, which can improve hardness of the battery cell and cycling performance of the lithium-ion battery.
In some embodiments, constituent monomers of the polyacrylate polymer include a first polymeric flexible monomer, a second polymeric polar monomer, and a third polymeric molecular weight regulating monomer.
The flexible monomer has a homopolymer glass transition temperature lower than that of a rigid monomer. Compared with a rigid group, the flexible monomer has certain flexibility, with a chain segment able to move, and the flexible monomer chain segment can regulate glass transition temperature of the polymer and improve toughness of the binder when applied, thereby facilitating good adhesion.
The polar monomer is a monomer that contains a polar group. The polar monomer helps improve adhesion of the polymer.
The molecular weight regulating monomer is a monomer involved in a crosslinking reaction and used for regulating a molecular weight of the polymer. A molecular weight of the binder falling within a specified range helps improve the adhesion.
In this application, the constituent monomers of the polyacrylate polymer include the first polymeric flexible monomer, the second polymeric polar monomer, and the third polymeric molecular weight regulating monomer, and the polymer is obtained through a crosslinking reaction of the three monomers. Molecular weight and glass transition temperature of the polymer can be controlled to improve the adhesion performance of the binder.
The modified polymer has a lowered softening point, such that the binder can fully penetrate into gaps between positive and negative electrode plates and the separator. To be specific, gaps are present between the electrode plates and the separator, and the binder penetrates into the gaps so that the electrode plates and the separator are effectively connected, and it is difficult for the binder to come out of the gaps. During swelling of the electrode plates, the binder has toughness, and therefore the binder can still effectively connect the two during swelling. This can make full use of the adhesion performance of the binder, and in turn helps improve kinetic performance and large-clamp cycling performance of a battery.
The softening point refers to a temperature at which a substance softens. The softening point is related to both the structure and molecular weight of the polymer. In this application, the molecular weight of the polymer is regulated by the third polymeric molecular weight regulating monomer so as to improve the softening point of the polymer.
The large-clamp cycling performance is a cycling functional testing performance for battery cells. During the testing process, a battery cell is placed in a clamp, and a certain force is applied to the clamp to compress the battery cell. The battery cell swells after fully charged, and under the compression of both the clamping force and the force from swelling, the battery cell deforms. This test is conducted to evaluate shape retention performance and compression resistance of the battery cell. With the binder in this solution, the good adhesion performance alleviates the swelling of the battery cell, resulting in better shape retention of the battery cell. The battery cell using the binder in this application exhibits good performance retention under the large-clamp testing conditions, indicating that the battery cell obtained using the binder in this solution features good shape retention. After the battery cell is assembled into a battery, space for mounting the battery cell in the battery can be reduced since the battery cell is less prone to deformation, allowing the battery to be made smaller. This is because if the battery cell is prone to deformation, such deformation compresses a structure near the battery cell. To avoid such phenomenon, more space is required for accommodating the deformed battery cell, to be specific, space needs to be reserved in the battery for accommodating the deformed part of the battery cell, thus taking up more space inside the battery.
In addition, good large-clamp cycling performance of the battery cell also indicates good cycling performance of the battery cell. For example, when the battery cell swells, the gap between the electrode plates and the separator becomes larger, and the path of lithium ions passing through the positive and negative electrodes becomes longer, resulting in deteriorated cycling.
In some embodiments, a molar ratio of the first polymeric flexible monomer, the second polymeric polar monomer, and the third polymeric molecular weight regulating monomer is 1:(0.01-0.8):(0.01-0.15), optionally 1:(0.05-0.7):(0.05-0.12).
For a molar ratio test method, during preparation of the binder, mole numbers of the monomers put during reaction for preparation of a shell layer structure are recorded, where the mole number of the monomer is equal to mass of the monomer divided by a molecular weight of the monomer, the mole number of the first polymeric flexible monomer is defined as a, the mole number of the second polymeric polar monomer is defined as b, the mole number of the third polymeric molecular weight regulating monomer is defined as c, and then the molar ratio of the first polymeric flexible monomer, the second polymeric polar monomer, and the third polymeric molecular weight regulating monomer is a:b:c.
When the molar ratio of the first polymeric flexible monomer, the second polymeric polar monomer, and the third polymeric molecular weight regulating monomer is 1:(0.01-0.8):(0.01-0.15), the binder features good adhesion. In 1:(0.01-0.8):(0.01-0.15), the values include minimum and maximum values of the range and each value between such minimum and maximum values. Specific examples include but are not limited to point values in the embodiments and 1:0.01:0.01, 1:0.1:0.01, 1:0.4:0.01, 1:0.8:0.01, 1:0.01:0.05, 1:0.01:0.1, 1:0.01:0.15, 1:0.1:0.01, 1:0.1:0.05, 1:0.1:0.15, 1:0.4:0.01, 1:0.4:0.05, 1:0.4:0.15, 1:0.8:0.01, 1:0.8:0.05, 1:0.8:0.15, and the like.
In some embodiments, the molar ratio of the first polymeric flexible monomer, the second polymeric polar monomer, and the third polymeric molecular weight regulating monomer is 1:(0.05-0.7):(0.05-0.12).
When the molar ratio of the first polymeric flexible monomer, the second polymeric polar monomer, and the third polymeric molecular weight regulating monomer is 1:(0.05-0.7):(0.05-0.12), the binder features good adhesion. In 1:(0.05-0.7):(0.05-0.12), the values include minimum and maximum values of the range and each value between such minimum and maximum values. Specific examples include but are not limited to point values in the embodiments and 1:0.05:0.05, 1:0.1:0.05, 1:0.4:0.05, 1:0.7:0.05, 1:0.1:0.05, 1:0.1:0.1, 1:0.1:0.12, and the like.
In some embodiments, the first polymeric flexible monomer contains an ester bond (—COOR (R is generally another non-H group such as an alkyl group)) in structure, the second polymeric polar monomer contains a cyano group (—C≡N) in structure, and the third polymeric molecular weight regulating monomer contains an amide bond (—CO—NH—).
The ester bond can improve flexibility of a molecular chain, the cyano group can improve the polarity of the monomer, and the amide bond has polarity and can easily form a hydrogen bond, which can improve adhesion. The first polymeric flexible monomer contains the ester bond in structure, the second polymeric polar monomer contains the cyano group in structure, and the third polymeric molecular weight regulating monomer contains the amide bond, so that with the polymer obtained by polymerization of the above three monomers, the molecular weight and glass transition temperature of the polymer can be controlled to improve the adhesion performance of the binder.
In some embodiments, the first polymeric flexible monomer is an acrylate monomer, the second polymeric polar monomer is an acrylonitrile monomer, and the third polymeric molecular weight regulating monomer is an acrylamide monomer.
The acrylate monomer can improve swelling resistance of the polymer, and as a flexible monomer chain segment in a molecular chain segment, can regulate the glass transition temperature of the polymer and improve toughness of the binder when applied, thereby facilitating good adhesion.
The acrylonitrile monomer has a cyano group with strong polarity, conducive to improving ionic conductivity and improving adhesion.
The acrylamide monomer regulates the molecular weight and also features good adhesion.
With the polymer prepared using the above three types of monomers, the molecular weight and glass transition temperature of the polymer can be controlled to improve the adhesion performance of the binder.
In some embodiments, the acrylate monomer includes at least one of methyl acrylate, ethyl acrylate, n-butyl acrylate, isobutyl acrylate, sec-butyl acrylate, tert-butyl acrylate, n-propyl acrylate, cyclohexyl acrylate, lauryl acrylate, 2-ethylhexyl acrylate, 2-hydroxyethyl acrylate, 2-hydroxypropyl acrylate, methyl methacrylate, ethyl methacrylate, n-butyl methacrylate, 2-ethylhexyl methacrylate, isobornyl methacrylate, lauryl methacrylate, 2-hydroxyethyl methacrylate, and 2-hydroxypropyl methacrylate; and/or the acrylonitrile monomer includes at least one of acrylonitrile and methacrylonitrile; and/or the acrylamide monomer includes at least one of acrylamide, N-methylolacrylamide, and N-butoxymethylacrylamide.
Based on the fact that the acrylate monomer helps improve the adhesion of the binder, the acrylate monomer may include at least one of methyl acrylate, ethyl acrylate, n-butyl acrylate, isobutyl acrylate, sec-butyl acrylate, tert-butyl acrylate, n-propyl acrylate, cyclohexyl acrylate, lauryl acrylate, 2-ethylhexyl acrylate, 2-hydroxyethyl acrylate, 2-hydroxypropyl acrylate, methyl methacrylate, ethyl methacrylate, n-butyl methacrylate, 2-ethylhexyl methacrylate, isobornyl methacrylate, lauryl methacrylate, 2-hydroxyethyl methacrylate, and 2-hydroxypropyl methacrylate. To be specific, the constituent monomers of the polyacrylate polymer may include one of the above acrylate monomers, or may include more than one of the above acrylate monomers, which is not specifically limited.
Based on the fact that the acrylonitrile monomer helps improve the adhesion of the binder, the acrylonitrile monomer includes at least one of acrylonitrile and methacrylonitrile. To be specific, the constituent monomers of the polyacrylate polymer may include one of the above acrylonitrile monomers, or may include more than one of the above acrylonitrile monomers, which is not specifically limited.
Based on the fact that the acrylamide monomer helps improve the adhesion of the binder, the acrylamide monomer includes at least one of acrylamide, N-methylolacrylamide, and N-butoxymethylacrylamide. To be specific, the constituent monomers of the polyacrylate polymer may include one of the above acrylamide monomers, or may include more than one of the above acrylamide monomers, which is not specifically limited.
In some embodiments, the plasticizer includes at least one of dibutyl phthalate, dioctyl adipate, dibutyl sebacate, dioctyl sebacate, and dibutyl adipate.
The core material is a plasticizer material, and the plasticizer may be a commonly used plasticizer, a specific type of which is not limited. For example, the core material includes at least one of dibutyl phthalate, dioctyl adipate, dibutyl sebacate, dioctyl sebacate, and dibutyl adipate.
In some embodiments, as shown in
In this application, the capsule-shaped binder is obtained through emulsion polymerization. The prepolymer of the capsule and the emulsion of the core material are first prepared separately, then the prepolymer and the initiator are added into the emulsion, and the mixture is heated for reaction, so that the prepolymer of the capsule forms the polymer on a surface of the core material to obtain the capsule-shaped binder.
Emulsion polymerization: emulsion polymerization is that monomers are dispersed in water through emulsifier and mechanical stirring to form an emulsion, and then an initiator is added to initiate monomer polymerization.
Emulsifier: emulsifier is a type of substance that can convert mutually immiscible oil and water into an emulsion that is difficult to stratify. The emulsifier is generally a surfactant having both properties of some hydrophilic polar groups and hydrophobic (lipophilic) non-polar groups.
Initiator: initiator is a substance that can initiate a polymerization reaction of monomers. For example, a free radical initiator refers to a type of compound that is readily decomposed by heat into free radicals (that are, primary free radicals), and can be used to initiate free radical polymerization and co-polymerization reactions of alkene and diene monomers.
For ease of description, in the foregoing preparation method of binder, the process of the foregoing preparation method is defined in paragraphs as step 1, step 2, and step 3 according to the writing order of the paragraphs. It can be understood by those skilled in the art that in the foregoing method in specific embodiments, the writing order of the steps does not imply a strict order of execution or constitute any limitation on the process of implementation, and a specific execution order of the steps should be determined based on their functions and possible internal logics.
In step 1, water, the emulsifier, and the constituent monomers of the organic polymer are mixed and stirred, and water and the emulsifier are stirred and dispersed to form an emulsion, to be specific, the emulsifier forms micelles in the aqueous phase, and most of the micelles are solubilized with monomers to obtain the prepolymer of the capsule. In step 2, water, the emulsifier, and the plasticizer are mixed and stirred, the emulsifier and water are likewise dispersed to form an emulsion, and the plasticizer enters into micelles to obtain the emulsion for later use. In step 3, the initiator and the prepolymer are added into the emulsion, and the mixture is stirred and heated for reaction, so that the constituent monomers of the organic polymer form a polymer on a surface of the core material and the organic polymer encapsulate the core material to obtain the capsule-structured binder.
The initiator in step 3 needs to be converted at a specified temperature to have the function of initiating monomer polymerization. Therefore, step 3 is entirely performed under a heating condition.
In addition, water can be either added or not added in step 3. It can be understood that when water added in steps 1 and 2 is sufficient, to be specific, when water added in steps 1 and 2 allows a solid content after the reactions in steps 1, 2, and 3 to be within a preset range, water can be not added in step 3; and when water added in steps 1 and 2 is not sufficient, a certain amount of water needs to be added in step 3 to regulate the solid content of the system, so as to prevent viscosity from increasing after reaction and the reaction rate from slowing down.
In some embodiments, the organic polymer includes at least one of polyacrylate polymer and urea-formaldehyde resin.
A type of the organic polymer in this application is not limited, and the organic polymer is required to have adhesion. For example, the organic polymer may be at least one of polyacrylate polymer and urea-formaldehyde resin.
In some embodiments, as shown in
In the capsule-shaped binder, the main adhesion is still provided by the capsule. In addition, to avoid rupture of the capsule, mass of the capsule is designed to be greater than that of the core material so as to guarantee stability of the capsule structure and adhesion. The mass ratio of the core material to the capsule is 1:(10-100), where in 1:(10-100), the values include minimum and maximum values of the range and each value between such minimum and maximum values. Specific examples include but are not limited to point values in the embodiments and 1:10, 1:20, 1:30, 1:40, 1:50, 1:60, 1:70, 1:80, 1:90, 1:100, and the like.
In some embodiments, the mass ratio of the plasticizer to the constituent monomers of the organic polymer is 1:(20-90).
In 1:(20-90), the values include minimum and maximum values of the range and each value between such minimum and maximum values. Specific examples include but are not limited to point values in the embodiments and 1:20, 1:30, 1:40, 1:50, 1:60, 1:70, 1:80, 1:90, and the like.
In some embodiments, the step of mixing and stirring water, an emulsifier, and constituent monomers of an organic polymer to obtain a prepolymer for later use includes the following step: mixing and stirring water, the emulsifier, and the constituent monomers of the organic polymer at a stirring speed of 1000 r/min-5000 r/min for 60 min±20 min to obtain the prepolymer for later use.
To obtain a fully emulsified prepolymer, it is necessary to stir at a high speed for a period of time. To be specific, water, the emulsifier, and the constituent monomers of the organic polymer are mixed and stirred at a stirring speed of 1000 r/min-5000 r/min, for example, 1000 r/min, 2000 r/min, 3000 r/min, 4000 r/min, or 5000 r/min, which is not specifically limited, for 60 min±20 min to obtain a prepolymer emulsified to uniformity under such stirring conditions for later use.
In some embodiments, the step of mixing and stirring water, an emulsifier, and a plasticizer to obtain an emulsion for later use includes the following step: mixing and stirring water, the emulsifier, and the plasticizer at a stirring speed of 1000 r/min-5000 r/min for 60 min±20 min to obtain the emulsion for later use.
To fully emulsify the plasticizer, it is necessary to stir at a high speed for a period of time. To be specific, water, the emulsifier, and the plasticizer are mixed and stirred at a stirring speed of 1000 r/min-5000 r/min, for example, 1000 r/min, 2000 r/min, 3000 r/min, 4000 r/min, or 5000 r/min, which is not specifically limited, for 60 min±20 min to obtain the emulsion for later use.
In some embodiments, the step of mixing and stirring water, an emulsifier, and a plasticizer to obtain an emulsion for later use includes the following step: mixing and stirring water and the emulsifier to obtain an emulsified solution, and putting the plasticizer into the emulsified solution and continuing to stir and emulsify the mixture to obtain the emulsion for later use.
To better emulsify the plasticizer, water and the emulsifier are mixed and stirred first to obtain the emulsified solution, and then the plasticizer is put into the emulsified solution and the mixture is continued to be stirred and emulsified to obtain the emulsion for later use.
In some embodiments, the step of mixing and stirring water and the emulsifier to obtain an emulsified solution, and putting the plasticizer into the emulsified solution and continuing to stir and emulsify the mixture to obtain the emulsion for later use includes the following step: mixing and stirring water and the emulsifier for 10 min to 20 min to obtain the emulsified solution, and putting the plasticizer into the emulsified solution and continuing to stir and emulsify the mixture for 60 min±20 min to obtain the emulsion for later use.
In the step that water and the emulsifier are mixed and stirred first to obtain the emulsified solution, the mixture needs to be stirred for 10 min to 20 min to obtain the emulsified solution, and then the plasticizer is put into the emulsified solution and the mixture is continued to be stirred and emulsified for 60 min±20 min to obtain the emulsion for later use.
In some embodiments, the step of adding the prepolymer and an initiator into the emulsion and heating for reaction to obtain a binder includes the following step: dropwise adding the prepolymer and the initiator into the emulsion at a speed of 10 mL/min-500 mL/min and heating for reaction to obtain the binder after cooling.
To avoid explosive polymerization caused by putting the prepolymer and the initiator into the emulsion all at once, it is necessary to dropwise add the prepolymer and the initiator into the emulsion slowly, for example, at a dropwise addition speed of 10 mL/min, 50 mL/min, 100 mL/min, 150 mL/min, 200 mL/min, 250 mL/min, 300 mL/min, 350 mL/min, 400 mL/min, 450 mL/min, or 500 mL/min, which is not specifically limited.
In some embodiments, the step of adding the prepolymer and an initiator into the emulsion and heating for reaction to obtain a binder includes the following step: adding the prepolymer and the initiator into the emulsion, heating to 90° C.±10° C., and stirring for reaction for 30 min±20 min to obtain the binder.
The initiator needs to initiate monomer polymerization at a specified temperature, so the prepolymer and the initiator are added into the emulsion, and the mixture is heated to 90° C.±10° C. and stirred for reaction for 30 min±20 min to obtain the binder.
In some embodiments, the step of adding the prepolymer and an initiator into the emulsion and heating for reaction to obtain a binder includes the following step: adding the prepolymer and the initiator into the emulsion, heating for reaction, and after cooling, adjusting pH to 6-8 to obtain the binder.
For the prepared binder, particles are prone to agglomeration, leading to sedimentation and hindering use and storage of the binder. Therefore, to avoid agglomeration and sedimentation of the binder, a pH adjusting reagent is added to the prepared binder to make the particles in the core-shell structure evenly dispersed and the system stable. A pH range of the binder is pH 6-8, for example, it may be pH 6, pH 7, or pH 8, which is not specifically limited. It can be understood that the specific pH adjusting reagent used is not limited in this application, for example, ammonium hydroxide may be used to adjust the pH.
In some embodiments, in step 1, the mass of the emulsifier accounts for 0.15%-5% of the mass of the constituent monomers of the organic polymer; and in step 3, the mass of the initiator accounts for 0.15%-1% of the mass of the constituent monomers of the organic polymer.
The amount of the emulsifier needs to be moderate. The emulsifier is an important component for emulsion polymerization since the emulsifier can convert mutually immiscible oil (monomer)-water into a fairly stable emulsion that is difficult to stratify. In an emulsion polymerization system, the emulsifier mainly has three functions: the first is to reduce surface tension and disperse monomers into tiny droplets; the second is to form a protective layer on the surface of the droplets or particles to prevent coalescence and keep the emulsion stable; and the third is to form micelles to solubilize the monomers. The size and number of micelles depend on the amount of the emulsifier, so the amount of the emulsifier directly influences performance of a product. In step 1, the mass of the emulsifier accounts for 0.15% to 5% of the mass of the constituent monomers of the organic polymer, for example, 0.15%, 0.2%, 0.25%, 0.3%, 0.35%, 0.4%, 0.45%, or 5%, which is not specifically limited. The amount of the initiator has great influence on speed of polymerization and performance of a product. Increased amount of the initiator leads to accelerated speed of polymerization, which leads to unstable polymerization reaction, decreased molecular weight and product yield, and deteriorated performance of the polymer. In addition, insufficient initiator also leads to difficulty in polymerization reaction. Therefore, in step 3, the mass of the initiator accounts for 0.15% to 1% of the mass of the constituent monomers of the organic polymer, for example, 0.15%, 0.2%, 0.25%, 0.3%, 0.35%, 0.4%, 0.45%, 0.5%, 0.55%, 0.6%, 0.65%, 0.7%, 0.75%, 0.8%, 0.85%, 0.9%, 0.95%, or 1%, which is not specifically limited.
In some embodiments, in steps 1 and 2, the emulsifier includes an anionic emulsifier, and in step 3, the initiator includes at least one of an azo initiator, an organic peroxide initiator, and an inorganic peroxide initiator.
The anionic emulsifier is a surface active substance, and when dissolved in water, has its active part that tends to dissociate into negatively charged ions, characterized by having a large organic anion that can react with alkali to generate a salt. In terms of structure of the negatively charged ion part, the salt can be divided into three types: carboxylate type, sulfonate type, and sulfate type.
The azo initiator refers to a type of free radical initiators containing a nitrogen-nitrogen double bond in molecular structure.
The peroxide initiator refers to a type of compound containing peroxy (—O—O—), for which after heated, the —O—O— bond breaks and splits into two corresponding free radicals, thereby initiating monomer polymerization. The peroxide initiators are divided into two types: inorganic peroxide initiator and organic peroxide initiator. The inorganic peroxide initiator includes hydrogen peroxide, ammonium persulfate, potassium persulfate, or the like; and the organic peroxide initiator includes benzoyl peroxide, tert-butyl benzoyl peroxide, methyl ethyl ketone peroxide, and the like.
The emulsifier refers to a substance that can make water into emulsion state. A specific type and structure of the emulsifier are not limited in this application, and any substance that can provide the above function and has no influence on a reaction system can be applied in this application. For example, in steps 1 and 2, the emulsifier used includes an anionic emulsifier. The initiator refers to a substance that can initiate monomer to undergo a polymerization reaction. A specific type and structure of the initiator is not limited in this application, and any substance that can provide the above function and has no influence on a reaction system can be applied in this application. For example, in step 3, the initiator includes at least one of an azo initiator, an organic peroxide initiator, and an inorganic peroxide initiator.
In some embodiments, in steps 1 and 2, the emulsifier includes at least one of sodium lauryl sulfate, sodium dodecyl sulfonate, sodium dodecyl benzene sulfonate, sodium styrene sulfonate, and sodium vinyl sulfonate; and in step 3, the initiator includes at least one of azobisisobutyronitrile, azobisisheptanenitrile, isopropyl benzene hydrogen peroxide, tert-butyl hydrogen peroxide, benzoyl peroxide and the like, ammonium persulfate, potassium persulfate, sodium persulfate, and hydrogen peroxide.
The emulsifier refers to a substance that can make water into emulsion state. For example, the emulsifier used in steps 1 and 2 includes at least one of sodium lauryl sulfate, sodium dodecyl sulfonate, sodium dodecyl benzene sulfonate, sodium styrene sulfonate, and sodium vinyl sulfonate. To be specific, the emulsifier used may be one of the above substances, for example, a preferred emulsifier is sodium dodecyl benzene sulfonate; or it may be a mixture of more than one of the above substances. The initiator refers to a substance that can initiate monomer to undergo a polymerization reaction. For example, the initiator used in step 3 includes at least one of azobisisobutyronitrile, azobisisheptanenitrile, isopropyl benzene hydrogen peroxide, tert-butyl hydrogen peroxide, benzoyl peroxide and the like, ammonium persulfate, potassium persulfate, sodium persulfate, and hydrogen peroxide. To be specific, the initiator used may be one of the above substances, for example, a preferred initiator is potassium persulfate; or it may be a mixture of more than one of the above substances.
In some embodiments, a total mass of water in step 1 and water in step 2 accounts for 30%-60% of mass of all the materials in steps 1, 2, and 3; and water in steps 1 and 2 is deionized water.
As a dispersion medium, water has functions such as mass transfer and temperature control. If the amount of water is excessively small or excessively large, it is difficult to control viscosity of the reaction system to fall within a reasonable range. The total mass of water in step 1, water in step 2, and water in step 3 accounts for 30%-60% of the mass of all the materials in steps 1, 2, and 3, for example, 30%, 35%, 45%, 50%, 55%, or 60%, which is not specifically limited. In addition, water in steps 1, 2, and 3 is deionized water, so as to avoid impurities in water affecting the polymerization reaction.
An embodiment of this application further provides a separator, where the separator is provided with the foregoing binder or a binder prepared by using the foregoing preparation method of binder. The binder has adopted all the technical solutions of all the foregoing embodiments, and therefore has at least all the beneficial effects brought by the technical solutions of the foregoing embodiments. Details are not described herein again.
The separator being coated with the foregoing binder can improve adhesion performance between an electrode plate and the binder, and alleviate the opening issue in an existing pre-cold pressing process for battery cells.
An embodiment of this application further provides an electrode assembly, where the electrode assembly includes the foregoing separator. The separator has adopted all the technical solutions of all the foregoing embodiments, and therefore has at least all the beneficial effects brought by the technical solutions of the foregoing embodiments. Details are not described herein again.
The electrode assembly includes a positive electrode plate, a negative electrode plate, and a separator. The binder is applied on the separator to adhere the electrode plates and the separator together, so as to alleviate the opening issue for electrode plates and separators.
An embodiment of this application further provides a battery cell, where the battery cell includes the foregoing electrode assembly. The electrode assembly has adopted all the technical solutions of all the foregoing embodiments, and therefore has at least all the beneficial effects brought by the technical solutions of the foregoing embodiments. Details are not described herein again.
The foregoing electrode assembly being applied to the battery cell can improve large-clamp cycling performance of the battery cell.
An embodiment of this application further provides a battery, where the battery includes the foregoing battery cell. The battery cell has adopted all the technical solutions of all the foregoing embodiments, and therefore has at least all the beneficial effects brought by the technical solutions of the foregoing embodiments. Details are not described herein again.
The battery may include a battery module and a battery pack.
An embodiment of this application further provides an electric apparatus, where the electric apparatus includes the foregoing battery cell or battery. The battery cell or the battery has adopted all the technical solutions of all the foregoing embodiments, and therefore has at least all the beneficial effects brought by the technical solutions of the foregoing embodiments. Details are not described herein again.
In addition, the following describes an electrode assembly, a battery cell, a battery, and an electric apparatus in this application with appropriate reference to the accompanying drawings.
An embodiment of this application provides an electrode assembly.
Generally, the electrode assembly includes a positive electrode plate, a negative electrode plate, an electrolyte, and a separator. During charging and discharging of a battery, active ions are intercalated and deintercalated between the positive electrode plate and the negative electrode plate. The electrolyte conducts ions between the positive electrode plate and the negative electrode plate. The separator is disposed between the positive electrode plate and the negative electrode plate to mainly prevent a short circuit between positive and negative electrodes and to allow the ions to pass through. The separator is the foregoing separator provided in this application.
The positive electrode plate includes a positive electrode current collector and a positive electrode film layer provided on at least one surface of the positive electrode current collector.
For example, the positive electrode current collector includes two opposite surfaces in its thickness direction, and the positive electrode film layer is disposed on either or both of the two opposite surfaces of the positive electrode current collector.
In some embodiments, the positive electrode current collector may be a metal foil current collector or a composite current collector. For example, an aluminum foil may be used as the metal foil. The composite current collector may include a polymer material matrix and a metal layer formed on at least one surface of the polymer material matrix. The composite current collector may be formed by forming a metal material (aluminum, aluminum alloy, nickel, nickel alloy, titanium, titanium alloy, silver, silver alloy, or the like) on a polymer material matrix (for example, matrices of polypropylene (PP), polyethylene terephthalate (PET), polybutylene terephthalate (PBT), polystyrene (PS), and polyethylene (PE)).
In some embodiments, when the electrode assembly is used for a lithium-ion battery, a positive electrode active material may be a well-known positive electrode active material used for lithium-ion batteries in the art. For example, the positive electrode active material may include at least one of the following materials: olivine-structured lithium-containing phosphate, lithium transition metal oxide, and respective modified compounds thereof. However, this application is not limited to these materials, but may use other conventional materials that can be used as positive electrode active materials for batteries instead. One of these positive electrode active materials may be used alone, or two or more of them may be used in combination. Examples of the lithium transition metal oxide may include but are not limited to at least one of lithium cobalt oxide (for example, LiCoO2), lithium nickel oxide (for example, LiNiO2), lithium manganese oxide (for example, LiMnO2 and LiMn2O4), lithium nickel cobalt oxide, lithium manganese cobalt oxide, lithium nickel manganese oxide, lithium nickel cobalt manganese oxide (for example, LiNi1/3Co1/3Mn1/3O2 (NCM333 for short), LiNi0.5Co0.2Mn0.3O2 (NCM523 for short), LiNi0.5Co0.25Mn0.25O2 (NCM211 for short), LiNi0.6Co0.2Mn0.2O2 (NCM622 for short), and LiNi0.8Co0.1Mn0.1O2 (NCM811 for short)), lithium nickel cobalt aluminum oxide (for example, LiNi0.85Co0.15Al0.05O2), and modified compounds thereof. Examples of the olivine-structured lithium-containing phosphate may include but are not limited to at least one of lithium iron phosphate (for example, LiFePO4 (LFP for short)), a composite material of lithium iron phosphate and carbon, lithium manganese phosphate (for example, LiMnPO4), a composite material of lithium manganese phosphate and carbon, lithium manganese iron phosphate, and a composite material of lithium manganese iron phosphate and carbon.
In some embodiments, the positive electrode film layer further optionally includes a binder. For example, the binder may include at least one of polyvinylidene fluoride (PVDF), polytetrafluoroethylene (PTFE), vinylidene fluoride-tetrafluoroethylene-propylene terpolymer, vinylidene fluoride-hexafluoropropylene-tetrafluoroethylene terpolymer, tetrafluoroethylene-hexafluoropropylene copolymer, and fluorine-containing acrylate resin.
In some embodiments, the positive electrode film layer further optionally includes a conductive agent. For example, the conductive agent may include at least one of superconducting carbon, acetylene black, carbon black, Ketjen black, carbon dots, carbon nanotubes, graphene, and carbon nanofiber.
In some embodiments, the positive electrode plate may be prepared in the following manner: the foregoing constituents used for preparing the positive electrode plate, for example, the positive electrode active material, the conductive agent, the binder, and any other constituent, are dispersed in a solvent (for example, N-methylpyrrolidone) to form a positive electrode slurry; and the positive electrode slurry is applied onto the positive electrode current collector, followed by processes such as drying and cold pressing to obtain the positive electrode plate.
The negative electrode plate includes a negative electrode current collector and a negative electrode film layer disposed on at least one surface of the negative electrode current collector, where the negative electrode film layer includes a negative electrode active material.
For example, the negative electrode current collector includes two opposite surfaces in its thickness direction, and the negative electrode film layer is disposed on either or both of the two opposite surfaces of the negative electrode current collector.
In some embodiments, the negative electrode current collector may be a metal foil current collector or a composite current collector. For example, a copper foil may be used as the metal foil. The composite current collector may include a polymer material matrix and a metal layer formed on at least one surface of the polymer material matrix. The composite current collector may be formed by forming a metal material (copper, copper alloy, nickel, nickel alloy, titanium, titanium alloy, silver, silver alloy, or the like) on a polymer material matrix (for example, matrices of polypropylene (PP), polyethylene terephthalate (PET), polybutylene terephthalate (PBT), polystyrene (PS), and polyethylene (PE)).
In some embodiments, the negative electrode active material may be a well-known negative electrode active material used for batteries in the art. For example, the negative electrode active material may include at least one of the following materials: artificial graphite, natural graphite, soft carbon, hard carbon, a silicon-based material, a tin-based material, lithium titanate, and the like. The silicon-based material may be selected from at least one of elemental silicon, silicon-oxygen compound, silicon-carbon composite, silicon-nitrogen composite, and silicon alloy. The tin-based material may be selected from at least one of elemental tin, tin-oxygen compound, and tin alloy. However, this application is not limited to these materials, but may use other conventional materials that can be used as negative electrode active materials for batteries instead. One of these negative electrode active materials may be used alone, or two or more of them may be used in combination.
In some embodiments, the negative electrode film layer further optionally includes a binder. The binder may be selected from at least one of styrene-butadiene rubber (SBR), polyacrylic acid (PAA), polyacrylic acid sodium (PAAS), polyacrylamide (PAM), polyvinyl alcohol (PVA), sodium alginate (SA), polymethacrylic acid (PMAA), and carboxymethyl chitosan (CMCS).
In some embodiments, the negative electrode film layer further optionally includes a conductive agent. The conductive agent may be selected from at least one of superconducting carbon, acetylene black, carbon black, Ketjen black, carbon dots, carbon nanotubes, graphene, and carbon nanofiber.
In some embodiments, the negative electrode film layer further optionally includes other additives such as a thickener (for example, sodium carboxymethyl cellulose (CMC-Na)).
In some embodiments, the negative electrode plate may be prepared in the following manner: the constituents used for preparing the negative electrode plate, for example, the negative electrode active material, the conductive agent, the binder, and any other constituent, are dispersed in a solvent (for example, deionized water) to form a negative electrode slurry; and the negative electrode slurry is applied onto the negative electrode current collector, followed by processes such as drying and cold pressing to obtain the negative electrode plate.
The electrolyte conducts ions between the positive electrode plate and the negative electrode plate. The electrolyte is not specifically limited to any particular type in this application, and may be selected according to requirements.
In some embodiments, the electrolyte is a liquid electrolyte. The liquid electrolyte includes an electrolytic salt and a solvent.
In some embodiments, the electrolytic salt may be selected from at least one of lithium hexafluorophosphate, lithium tetrafluoroborate, lithium perchlorate, lithium hexafluoroborate, lithium bis(fluorosulfonyl) imide, lithium bis-trifluoromethanesulfonimide, lithium trifluoromethanesulfonate, lithium difluorophosphate, lithium difluorooxalatoborate, lithium bisoxalatoborate, lithium difluorobisoxalate phosphate, and lithium tetrafluoro oxalate phosphate.
In some embodiments, the solvent may 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, sulfolane, methyl sulfonyl methane, ethyl methanesulfonate, and diethyl sulfone.
In some embodiments, the liquid electrolyte further optionally includes an additive. For example, the additive may include a negative electrode film-forming additive or a positive electrode film-forming additive, or may include an additive capable of improving some performance of the battery, for example, an additive for improving overcharge performance of the battery, or an additive for improving high- or low-temperature performance of the battery.
In some embodiments, the electrode assembly further includes a separator. The separator is not limited to any particular type in this application, and may be any well-known porous separator with good chemical stability and mechanical stability.
In some embodiments, a material of the separator may be selected from at least one of glass fiber, non-woven fabric, polyethylene, polypropylene, and polyvinylidene fluoride. The separator may be a single-layer film or a multi-layer composite film, and is not particularly limited. When the separator is a multi-layer composite film, all layers may be made of same or different materials, which is not particularly limited.
In some embodiments, the positive electrode plate, the negative electrode plate, and the separator may be made into the electrode assembly through winding or lamination.
In some embodiments, the electrode assembly may include an outer package. The outer package may be used for packaging the electrode assembly and the electrolyte.
In some embodiments, the outer package of the electrode assembly may be a hard shell, for example, a hard plastic shell, an aluminum shell, or a steel shell. The outer package of the electrode assembly may alternatively be a soft pack, for example, a soft pouch. A material of the soft pack may be plastic. As the plastic, polypropylene, polybutylene terephthalate, polybutylene succinate, and the like may be listed.
The electrode assembly is not limited to any specific shape in this application, and the electrode assembly may be cylindrical, rectangular, or of any other shape. For example,
In some embodiments, referring to
In some embodiments, the electrode assemblies may be assembled into a battery module, and the battery module may include one or more electrode assemblies. The specific quantity may be chosen by persons skilled in the art according to use and capacity of the battery module.
Optionally, the battery module 4 may further include a housing with an accommodating space, and the plurality of electrode assemblies 5 are accommodated in the accommodating space.
In some embodiments, the battery module may be further assembled into a battery pack, and the battery pack may include one or more battery modules. The specific quantity may be chosen by persons skilled in the art according to use and capacity of the battery pack.
In addition, this application further provides an electric apparatus. The electric apparatus includes at least one of the electrode assembly, the battery module, or the battery pack provided in this application. The electrode assembly, the battery module, or the battery pack may be used as a power source for the electric apparatus or an energy storage unit of the electric apparatus. The electric apparatus may include a mobile device (for example, a mobile phone or a notebook computer), an electric vehicle (for example, a battery electric vehicle, a hybrid electric vehicle, a plug-in hybrid electric vehicle, an electric bicycle, an electric scooter, an electric golf vehicle, or an electric truck), an electric train, a ship, a satellite system, an energy storage system, or the like, but is not limited thereto.
The electrode assembly, the battery module, or the battery pack may be selected for the electric apparatus based on requirements for using the electric apparatus.
In another example, the apparatus may be a mobile phone, a tablet computer, a notebook computer, or the like. Such apparatus is generally required to be light and thin and may use an electrode assembly as its power source.
The following describes examples of this application. The examples described below are illustrative and only used for explaining this application, and cannot be construed as limitations on this application. Examples whose technical solutions or conditions are not specified are made in accordance with technical solutions or conditions described in literature in the field or made in accordance with product instructions. The reagents or instruments used are all conventional products that are commercially available if no manufacturer is indicated.
In step 1, 75.24 g of methyl acrylate, 18.55 g of acrylonitrile, and 6.21 g of acrylamide were separately added into a 500 mL three-necked bottle at a molar ratio of 1:0.4:0.1, then 3.6 g of sodium dodecyl sulfonate and 150 g of deionized water were added, and the mixture was fully stirred for 60 min for dispersion and emulsification to obtain a prepolymer of a capsule material, which was poured into a container for later use.
In step 2, 100 mL of deionized water and 0.15 g of sodium dodecyl benzene sulfonate were added into the 500 mL three-necked bottle, the mixture was well stirred and emulsified at a rotation speed of 5000 r/min for 10 min, 10 g of dibutyl phthalate was added, and the mixture was continued to be emulsified for 60 min to obtain a uniform and stable emulsion.
In step 3, the prepolymer of the capsule material prepared in step 1 and an initiator solution (a solution formed by dissolving 0.2 g of potassium persulfate in deionized water) were slowly added dropwise using a peristaltic pump, and after the dropwise addition was complete, the mixture was heated to 90° C. and maintained at that temperature for reaction for 0.5 h, and then cooled down to 40° C., the pH was adjusted to 7-8 with ammonium hydroxide, and then the mixture was filtered and discharged.
Commercially available PP-PE copolymer microporous film with a thickness of 20 μm and an average pore size of 80 nm (Model 20 from Advanced Electronic Technology, Co., Ltd.) was used as a substrate. The binder prepared as described above was added into deionized water and stirred and mixed to uniformity, to obtain a slurry (with a solid content of 20%). The slurry was uniformly applied onto both surfaces of the substrate and dried to remove the solvent, with the composition applied on the substrate having a density of 1.0 g/m2 to obtain a separator.
Polyvinylidene fluoride (PVDF), lithium iron phosphate (LFP), a conductive agent carbon black, and N-methylpyrrolidone (NMP), at a mass ratio of 1.2:58.38:0.42:40, were well mixed and stirred to prepare a positive electrode slurry. The positive electrode slurry was uniformly applied onto a positive electrode current collector aluminum foil with a loading amount of 200 g/m2, followed by drying, cold pressing, and slitting, to obtain a positive electrode plate.
Artificial graphite, a conductive agent acetylene black, a binder styrene-butadiene rubber (SBR), and a thickener sodium carboxymethyl cellulose (CMC-Na), at a mass ratio of 96.2:1.0:1.6:1.2, were added into deionized water and well mixed and stirred to prepare a negative electrode slurry (with a solid content of 63%). The negative electrode slurry was uniformly applied onto a negative electrode current collector copper foil with a loading amount of 98 g/m2, followed by drying, cold pressing, and slitting, to obtain a negative electrode plate.
At 25° C., ethylene carbonate (EC), ethyl methyl carbonate (EMC), and diethyl carbonate (DEC) were mixed at a volume ratio of 1:1:1 to obtain a mixed solvent, and then LiPF6 was dissolved in the mixed solvent to obtain an electrolyte, where a concentration of LiPF6 was 1 mol/L.
The foregoing positive electrode plate, separator, and negative electrode plate were stacked in sequence and wound, and pre-pressed and formed (during which the separator was adhered to the electrode plates), to obtain an electrode assembly. The electrode assembly was placed in an outer package, the foregoing electrolyte was added, and processes such as sealing, standing, formation, and aging were performed to obtain an electrode assembly.
The experimental data of examples 2 to 18 were obtained by changing parameters on the basis of example 1 (as shown in Table 1 and Table 2).
15 g of urea, 38.01 g of formaldehyde solution, 1.5 g of ammonium chloride, 1.5 g of resorcinol, 1.5 g of sodium dodecylbenzene sulfonate, and 100 g of deionized water were added into a 250 mL four-necked flask as a continuous phase of reaction. Stirring was performed until full dissolution, the pH value was adjusted to 4 with an HCl solution, and then 5 g of dibutyl phthalate was added and emulsified for 30 min at the stirring speed. After the temperature of the solution was raised to 60° C., the reaction was continued for 4 h and then ended. The cooled aqueous solution of microcapsules was filtered, washed with a large amount of deionized water, and then filtered and dried.
At room temperature, 60.92 g of methyl acrylate, 33.04 g of acrylonitrile, and 6.04 g of acrylamide were weighed and added into a 500 mL four-necked flask equipped with a mechanical stirrer, a thermometer, and a condenser tube, and then 3 g of an emulsifier sodium lauryl sulfate, 1 g of an initiator ammonium persulfate, and 120 g of deionized water were added. The mixture was stirred and emulsified at a rotation speed of 1600 rpm for 30 min, and then the temperature was raised to 75° C. for reaction for 4 h, the pH value was adjusted to 6-8, and the temperature was lowered to below 40° C. to stop the reaction. The mixture was filtered and discharged.
752.4 g of methyl acrylate, 36 g of sodium dodecyl sulfonate, and 1.2 kg of deionized water were added into a three-necked bottle and well stirred for dispersion and emulsification. The temperature was raised to 70° C. and an initiator solution (a solution formed by dissolving 0.6 g of potassium persulfate in deionized water) was added and stirred for reaction for 30 min. Then the temperature was continued to raise to 80° C., and an initiator solution (a solution formed by dissolving 1.2 g of potassium persulfate in 100 g of deionized water) was slowly added dropwise using a peristaltic pump. After the dropwise addition was complete, the mixture was heated to 90° C. and maintained at that temperature for reaction for 0.5 h, and then cooled down to 40° C., the pH was adjusted to 7-8 with ammonium hydroxide, and then the mixture was filtered and discharged.
Deionized water and an initiator with a specified ratio were added into a three-necked flask equipped with a reflux condenser, a thermometer, and a stirring magnet. After stirred to uniformity at room temperature, the mixture was heated to a given temperature to induce decomposition of the initiator. After the temperature was kept constant for about half an hour, a peristaltic pump was used to control the concentration of acrylonitrile into the polymerization system, and the monomer was added into water in small droplets to implement a polymerization reaction. After the monomer was added dropwise, the reaction was continued for a specified period at a constant temperature under stirring. After the reaction ended, the three-necked flask was cooled in the air to room temperature, the reaction was stopped, and the mixture was filtered and discharged.
30 g-90 g of acrylamide monomer was added into 120 g of water to prepare an acrylamide solution, and 0.02 g-1 g of persulfate was dissolved in 30 g of water to obtain an initiator solution. 37.5 g of a solvent isopropanol was added into a 250 mL four-necked reaction flask, stirred at a stirring speed of 200 r/min, and heated to reflux. The monomer solution and the initiator solution were continuously added dropwise with the dropwise addition speed controlled and a dropwise addition time of 120 min. The reflux reaction was kept for 2 h, and the isopropanol was distilled out to obtain a polyacrylamide solution, followed by filter and discharge.
The polyacrylate solution prepared in comparative example 1 and a plasticizer dibutyl phthalate were mixed at a mass ratio of 100:5 and well stirred to obtain a mixed solution of polyacrylate and plasticizer.
Preparation of wall material melamine resin: Melamine, formaldehyde, and water at a mass ratio of 1:2:5 were used to prepare a wall material. 15.0 g of melamine and 30.0 g of formaldehyde solution were added into 45.0 g of deionized water, triethanolamine was added dropwise to adjust the pH to 8-9, the mixture was heated through water bath at 70° C. and stirred until the wall material became transparent, then 30.0 g of deionized water was added, and the mixture was continued to be stirred for 30 minutes to obtain the wall material.
Preparation of capsule: 71.91 g of distilled water and 0.09 g of sodium dodecyl benzene sulfonate were mixed and stirred for 10 min, and then 9 g of dibutyl phthalate was added. The mixture was stirred for 60 min in water bath at 70° C. to obtain a core material emulsion. The cooled wall material melamine resin was slowly added into the core material emulsion, and then citric acid was added into the mixed solution to adjust the pH to 2.5-3.0. The mixture was slowly heated to 70° C. and stirred for 3 h, and then the reaction was stopped. After standing at room temperature, the resulting product was rinsed and filtered several times with deionized water and anhydrous ethanol. Finally, the resulting product was heated and dried in an oven at 40° C. for 48 h, and the powder obtained was microcapsules encapsulated with melamine resin.
As shown in Tables 1 and 2, in examples 1 to 4 and examples 17 and 18, the ratios of the three capsule polymers were changed while all other conditions remained unchanged; in examples 5 to 8 and examples 13 to 16, the masses of the core material and the capsule were changed while all other conditions remained unchanged; and in examples 9 to 11, the median particle sizes by volume Dv50 of the binders were changed while all other conditions remained unchanged.
As shown in Table 3, the binder in comparative example 1 is an acrylate copolymer obtained by copolymerization of methyl acrylate, acrylonitrile, and acrylamide; the binder in comparative example 2 is a polymer obtained by polymerization of acrylonitrile; the binder in comparative example 3 is a polymer obtained by polymerization of acrylamide; the binder in comparative example 4 is a polymer obtained by polymerization of acrylamide; the binder in comparative example 5 is a polymer obtained by mixing polymerization of a plasticizer and a polyacrylate copolymer; and the binder in comparative example 6 is a binder prepared using melamine resin as capsule and plasticizer as core material.
A battery electrode plate and a separator were stacked and placed on a hot pressing machine, where parameters of the hot pressing machine was set as follows: temperature was 25° C., pressure was 10 t, and time was 30 s. A sample of adhered separator/positive electrode plate was obtained under the action of pressure. The sample of adhered separator/electrode plate was cut into rectangular sample strips of 150 mm×20 mm. The electrode plate side of the rectangular sample strip was attached to a steel plate with double-sided tape, and the separator was separated from the electrode plate by 2 cm along a length direction at one end of the rectangular sample strip to obtain a test specimen.
The steel plate was kept horizontal and fixed with a lower clamp of a universal testing machine (Model CTM2100 from Xie Qiang Instrument Manufacturing (Shanghai) Co., Ltd.), and the peeled end of the separator was fixed with an upper clamp of the universal testing machine and connected to a tensile machine. The test conditions were set to a stretching speed of 20 mm/min and a horizontal pull of 10 cm. After the tension became stable, the tension value was recorded, and the adhesion force between the separator and the electrode plate was obtained based on a ratio of the tension value to width of the sample. In addition, the data of adhesion force between the separator and the electrode plate can indirectly indicate the adhesion performance of the binder. A greater value of adhesion force between the separator and the electrode plate means better adhesion performance.
A battery cell was put on a table with two ends horizontal, with the middle hollow part fixed at a width of 12 cm. The battery cell was laid flat naturally, and a deviation of the battery cell center from the horizontal datum line was measured, so as to evaluate the hardness of the battery cell. A greater deviation of the battery cell center from the horizontal datum line indicates a lower hardness of the battery cell.
At 25° C., the battery prepared in example 1 was constant-current charged to 3.8 V at ⅓ C, then constant-voltage charged to 0.05 C at 3.8 V, left standing for 5 min, then discharged to 2.0 V at ⅓ C, and the resulting discharge capacity was recorded as the initial capacity C0. The preceding steps were repeated for the same battery and the discharge capacity Cn after the n-th cycle was recorded, and the battery capacity retention rate Pn after each cycle=(Cn/C0)×100%. The battery capacity retention rate after 500 cycles can be used to reflect the difference in cycling performance.
As shown in Table 4, the battery cells obtained using the binders in examples 1 to 18 show a good adhesion force between the separator and the electrode plate, while the battery cells obtained using the binders in comparative examples 1 to 6 show an adhesion force not as good as that in examples 1 to 18. This indicates that the binders in examples 1 to 18 have better adhesion performance than the binders in comparative examples 1 to 6. In addition, examples 1 to 18 show better cycling performance of batteries than comparative examples 1 to 6. This indicates that under the condition of improved adhesion performance of a binder, applying such binder to a separator of a battery can effectively improve the cycling performance of the battery.
The foregoing descriptions are merely preferred embodiments of this application, but are not intended to limit the patent scope of this application. Any equivalent structural transformations made by using the content of the specification and drawings or directly/indirectly used in other related technical fields are included in the patent protection scope of this application.
| Number | Date | Country | Kind |
|---|---|---|---|
| 202310010649.0 | Jan 2023 | CN | national |
This application is a continuation of international application PCT/CN2023/099992, filed on Jun. 13, 2023, which claims priority to Chinese Patent Application No. 202310010649.0 filed on Jan. 4, 2023, which are incorporated herein by reference in their entireties.
| Number | Date | Country | |
|---|---|---|---|
| Parent | PCT/CN2023/099992 | Jun 2023 | WO |
| Child | 18778968 | US |
