Patent Application
20250125491
The present application belongs to the field of battery technology, and in particular relates to a separator, a method for preparing the same, and a secondary battery and an electrical device related thereto.
In recent years, secondary batteries have been widely used in energy storage power systems such as hydraulic, thermal, wind and solar power plants, as well as in many fields such as electric tools, electric bicycles, electric motorcycles, electric vehicles, military equipment, and aerospace. With the application and promotion of secondary batteries, their safety issues, especially thermal safety issues, have received more and more attention. However, the existing methods for improving the thermal safety performance of secondary batteries are often not conducive to balancing the energy density and service life of secondary batteries. Therefore, how to obtain a secondary battery having the combined characteristics of high energy density, high thermal safety performance, long service life and good rate performance is a key challenge in designing secondary battery.
An object of the present application is to provide a separator, a method for preparing the same and the secondary battery and an electrical device related thereto, wherein the separator has characteristics including excellent heat resistance, high bonding strength, good electrolyte infiltration and retention and the like, which enables secondary battery using the separator to have the combined characteristics of high energy density, high thermal safety performance, long cycle life, and good rate performance.
A first aspect of the present application provides a separator, including a porous substrate and a coating layer disposed on one or more surfaces of the porous substrate, wherein the coating layer includes a three-dimensional skeleton structure and a filler, and at least a portion of the filler is filled in the three-dimensional skeleton structure, and the filler is secondary particles formed by agglomeration of primary particles.
The filler in the coating layer is secondary particles formed by agglomeration of primary particles, and the filler with secondary particle morphology has the advantages of large specific surface area and good affinity with the three-dimensional skeleton structure, thus can interact with the three-dimensional skeleton structure to from a stable spatial network structure. This can not only increase the number of ion conductivity channels of the separator, promote ion transport, but also improve the electrolyte infiltration and retention characteristics of the separator. Therefore, the secondary battery using the separator of this application can have a long cycle life and good rate performance. At least a portion of the filler is filled in the three-dimensional skeleton structure, which helps the filler and the three-dimensional skeleton structure to form an embedding effect, thereby not only increasing the heat resistance of the separator, reducing the shrinkage of the separator when heated, reducing the risk of short circuit between the positive electrode and the negative electrode, resulting in high thermal safety performance of the secondary battery, but also maintaining high bonding strength between the coating layer and the porous substrate, preventing the filler from falling off during the long-term charge and discharge of the secondary battery. The coating layer of the present application includes a three-dimensional skeleton structure, and at least a portion of the filler is filled in the three-dimensional skeleton structure, thus there are many contact sites between the filler and the three-dimensional skeleton structure, which can reduce the amount of binder used in the coating layer, thereby effectively reducing the risk of clogging by the binder and further improving the cycle life and rate performance of the secondary battery. Since the coating layer of the present application has high heat resistance, thus thinner porous substrates can be used, and the secondary battery can further have high energy density.
In some embodiments of the present application, the primary particles that constitute the filler has an average particle size of from 8 nm to 30 nm, optionally from 10 nm to 20 nm. As a result, the filler can have a good secondary particle morphology, and the appropriate ranges allow the filler and the three-dimensional skeleton structure to better overlap to form an integrated effect.
In some embodiments of the present application, the filler has an average particle size of ≤200 nm, optionally from 50 nm to 200 nm. As a result, the filler can have a higher specific surface area, and the filler with an average particle size within the suitable ranges can further be better matched with the length of the three-dimensional skeleton structure, so that the filler and the three-dimensional skeleton structure can be better overlapped to form an integrated effect, thereby increasing the affinity between the filler and the three-dimensional skeleton structure and increasing the electrolyte infiltration and retention characteristics of the separator.
In some embodiments of the present application, the filler has a BET specific surface area of ≥20 m2/g, optionally from 30 m2/g to 80 m2/g. As a result, the filler has better affinity with the three-dimensional skeleton structure, and meanwhile the filler can improve the electrolyte infiltration and retention characteristics of the separator.
In some embodiments of the present application, the filler includes one or more of inorganic particles and organic particles.
In some embodiments of the present application, the inorganic particles comprise one or more of boehmite, aluminum oxide, barium sulfate, magnesium oxide, magnesium hydroxide, silicon oxide, tin dioxide, titanium oxide, calcium oxide, zinc oxide, zirconium oxide, yttrium oxide, nickel oxide, hafnium oxide, cerium oxide, zirconium titanate, barium titanate and magnesium fluoride; more optionally, the inorganic particles comprise one or more of boehmite, aluminum oxide, barium sulfate, magnesium oxide, silicon oxide, titanium oxide, zinc oxide, cerium oxide, and barium titanate.
In some embodiments of the present application, the organic particles comprise one or more of polystyrene and polyacrylic wax.
In some embodiments of the present application, the filler comprises inorganic particles with secondary particle morphology, and the inorganic particles with secondary particle morphology have a crystal form including at least two of α crystal form, θ crystal form, γ crystal form and η crystal form. Optionally, the inorganic particles with secondary particle morphology have α crystal form including two or more of α crystal form, θ crystal form and γ crystal form.
In some embodiments of the present application, based on the total weight of the inorganic particles with secondary particle morphology, the inorganic particles with secondary particle morphology of α crystal form is present in an amount of ≥1.2 wt. % in the inorganic particles with secondary particle morphology, and optionally from 1.2 wt. % to 10 wt. %.
In some embodiments of the present application, based on the total weight of the inorganic particles with secondary particle morphology, the inorganic particles with secondary particle morphology of θ crystal form is present in an amount of ≥50 wt. % in the inorganic particles with secondary particle morphology, and optionally from 60 wt. % to 85 wt. %.
In some embodiments of the present application, based on the total weight of the inorganic particles with secondary particle morphology, the inorganic particles with secondary particle morphology of γ crystal form is present in an amount of ≥10 wt. % in the inorganic particles with secondary particle morphology, and optionally from 15 wt. % to 60 wt. %.
In some embodiments of the present application, based on the total weight of the inorganic particles with secondary particle morphology, the inorganic particles with secondary particle morphology of η crystal form is present in an amount of ≤5 wt. % in the inorganic particles with secondary particle morphology, and optionally ≤2 wt. %.
By selecting the fillers of different crystal forms, it facilitates improving one or more of heat resistance, bonding strength, and electrolyte infiltration and retention characteristics of the separator.
In some embodiments of the present application, the primary particles that constitute the filler have an average particle size of d1 nm, a material that constitutes the three-dimensional skeleton structure has an average particle size of d2 nm, and the separator satisfies: d1≤√{square root over (2)}d2. In this way, the materials that constitute the three-dimensional skeleton structure can be overlapped in the gaps between the primary particles that constitute the filler, which facilitates the overlap between the filler and the three-dimensional skeleton structure to form an integrated effect. Therefore, the coating layer can have a more stable spatial network structure, and the coating layer can further have a uniform nanopore structure, thereby enabling the separator better having the combined characteristics of high heat resistance, high bonding strength, and good electrolyte infiltration and retention.
In some embodiments of the present application, the three-dimensional skeleton structure is formed by fibrous objects, and the fibrous objects optionally have a morphology comprising one or more of rod shape, tubular shape and fibrous shape.
In some embodiments of the present application, a material that constitutes the three-dimensional skeleton structure has an average diameter of ≤40 nm, optionally from 10 nm to 35 nm. As a result, this can further improve the ion transport characteristics and voltage breakdown resistance characteristics of the separator, and at the same time it also facilitates the overlap between the material that constitutes the three-dimensional skeleton structure and the filler to form an integrated effect, thereby further improving the heat resistance of the separator.
In some embodiments of the present application, a material that constitutes the three-dimensional skeleton structure has an average length of from 100 nm to 600 nm, optionally from 200 nm to 450 nm. As a result, this can further improve the heat resistance and ion transport characteristics of the separator.
In some embodiments of the present application, a material that constitutes the three-dimensional skeleton structure has an aspect ratio of from 5 to 60, optionally from 10 to 30. As a result, this can further improve the electrolyte infiltration and retention characteristics of the separator.
In some embodiments of the present application, the fibrous objects includes one or more of organic materials and inorganic materials. Optionally, the organic materials comprise one or more of nanocellulose, polytetrafluoroethylene nanofibers and polyamide nanofibers; optionally, the nanocellulose comprises one or more of cellulose nanofibers, cellulose nanowhiskers and bacterial nanocellulose. Optionally, the inorganic materials comprise one or more of halloysite nanotubes, nanorod-shaped alumina, nanorod-shaped boehmite, nanorod-shaped silica and glass fiber.
In some embodiments of the present application, a material that constitutes the three-dimensional skeleton structure comprises nanocellulose, and the nanocellulose comprises one or more of unmodified nanocellulose and modified nanocellulose.
In some embodiments of the present application, the modified nanocellulose comprises a modifying group, and the modifying group comprises one or more of an amino group, a carboxyl group, an aldehyde group, a sulfonic acid group, a boric acid group, and a phosphoric acid group, and optionally comprises one or more of a sulfonic acid group, a boric acid group, and a phosphoric acid group. When the nanocellulose has the above-mentioned specific modifying group, on one hand, it can be effectively improve the heat resistance of the separator, thereby improving the thermal safety performance of the secondary battery; on the other hand, it can further improve the bonding strength between the coating layer and the porous substrate.
In some embodiments of the present application, the modified nanocellulose comprises a hydroxyl group and a modifying group, and a molar ratio of the modifying group to the hydroxyl group is from 1:4 to 4:1, optionally from 2:3 to 7:3. As a result, this can further improve the heat resistance, ion transport characteristics and electrolyte infiltration and retention characteristics of the separator.
In some embodiments of the present application, a material that constitutes the three-dimensional skeleton structure comprises a sulfonic acid group, and the material that constitutes the three-dimensional skeleton structure has a sulfur amount of ≥0.1 wt %, optionally from 0.2 wt % to 0.5 wt %, based on the total weight of the material that constitutes the three-dimensional skeleton structure.
In some embodiments of the present application, the three-dimensional skeleton structure is present in an amount of from 5 wt. % to 40 wt. %, optionally from 10 wt. % to 25 wt. %, based on the total weight of the coating layer.
In some embodiments of the present application, the filler is present in an amount of ≥60 wt. %, optionally from 70 wt. % to 90 wt. %, based on the total weight of the coating layer.
When the amounts of the three-dimensional skeleton structure and the filler are within the suitable ranges, it can ensure that the coating slurry has a suitable viscosity, which is more conducive to coating process; In addition, it is also beneficial to the overlap between the three-dimensional skeleton structure and the filler to form an integrated effect, thereby enabling the coating layer to have a more stable spatial network structure.
In some embodiments of the present application, the coating layer further comprises inorganic particles with primary particle morphology, and at least a portion of the inorganic particles with primary particle morphology is embedded in the coating layer. As a result, this can better exert its supporting role in the coating layer, reduce the shrinkage of secondary particles, reduce the amount of binder, thereby improving the heat resistance of the separator.
In some embodiments of the present application, the inorganic particles with primary particle morphology have an average particle size of from 200 nm to 800 nm, optionally from 200 nm to 400 nm. As a result, the inorganic particles with primary particle morphology can better exert the supporting role, so that the coating layer maintains a stable pore/channel structure during long-term charge and discharge, which is beneficial to ion transport and meanwhile improves the heat resistance of the separator.
In some embodiments of the present application, the inorganic particles with primary particle morphology have a BET specific surface area of ≤10 m2/g, optionally from 3 m2/g to 7 m2/g. As a result, the inorganic particles with primary particle morphology can better exert the supporting role, so that the coating layer maintains a stable pore/channel structure during long-term charge and discharge, which is beneficial to ion transport and meanwhile improves the heat resistance of the separator.
In some embodiments of the present application, the inorganic particles with primary particle morphology have a crystal form including one or more of α crystal form and γ crystal form, and optionally have a crystal form including α crystal form. As a result, this can further improve the heat resistance of coating layer.
In some embodiments of the present application, the inorganic particles with primary particle morphology have a crystal form including α crystal form, and based on the total weight of the inorganic particles with primary particle morphology, the inorganic particles with primary particle morphology of α crystal form is present in an amount of ≥90 wt. % in the inorganic particles with primary particle morphology, and optionally from 95 wt. % to 100 wt. %.
In some embodiments of the present application, the inorganic particles with primary particle morphology comprises one or more of inorganic particles with a dielectric constant of 5 or more, inorganic particles having ion conductivity but no ion storage capability and inorganic particles capable of undergoing electrochemical reactions.
In some embodiments of the present application, the inorganic particles with primary particle morphology are present in an amount of ≤30 wt. %, optionally from 5 wt. % to 25 wt. %, based on the total weight of the coating layer. As a result, the inorganic particles with primary particle morphology can better exert the supporting role, so that the coating layer maintains a stable pore/channel structure during long-term charge and discharge, which is beneficial to ion transport and meanwhile improves the heat resistance of the separator.
In some embodiments of the present application, the coating layer further includes a non-granular binder.
In some embodiments of the present application, the coating layer further includes an aqueous solution-type binder.
In some embodiments of the present application, the non-granular binder in the coating layer is present in an amount of ≤2 wt. %, based on the total weight of the coating layer. The present application allows the separator to maintain high adhesiveness under the premise of reducing the amount of binder.
In some embodiments of the present application, the porous substrate has a thickness of ≤6 μm, optionally from 3 μm to 5 nm. As a result, this contributes to improving the energy density of the secondary battery.
In some embodiments of the present application, the coating layer has a thickness of ≤1 μm, optionally from 0.5 μm to 0.8 nm. As a result, this contributes to improving the energy density of the secondary battery.
In some embodiments of the present application, the separator further includes an adhesive layer, the adhesive layer is disposed on at least part of surface of the coating layer, and the adhesive layer comprises a granular binder. The adhesive layer can not only prevent the coating layer from peeling off and improve the safety performance of the secondary battery, but also improve the interface between the separator and the electrode and improve the cycle performance of the secondary battery.
In some embodiments of the present application, the granular binder includes one or more of acrylate monomer homopolymer or copolymer, acrylic monomer homopolymer or copolymer, fluorine-containing olefin monomer homopolymer or copolymer.
In some embodiments of the present application, the separator has a longitudinal thermal shrinkage rate at 150° C. for 1 h of ≤5%, optionally from 0.5% to 3%.
In some embodiments of the present application, the separator has a lateral thermal shrinkage rate at 150° C. for 1 h of ≤5%, optionally from 0.5% to 3%.
In some embodiments of the present application, the separator has a longitudinal tensile strength of ≥2000 kg/cm2, optionally from 2500 kg/m2 to 4500 kg/m2.
In some embodiments of the present application, the separator has a lateral tensile strength of ≥2000 kg/cm2, optionally from 2500 kg/m2 to 4500 kg/m2.
In some embodiments of the present application, the separator has a wetting length of ≥30 mm, optionally from 30 mm to 80 mm.
In some embodiments of the present application, the separator has a wetting speed of >3 mm/s, optionally from 3 mm/s to 10 mm/s.
In some embodiments of the present application, the separator has an air permeability of ≤300 s/100 mL, optionally from 100 s/100 mL to 230 s/100 mL.
When the properties of the separator satisfy one or more of the above conditions, it is beneficial to improving one or more of energy density, thermal safety performance, cycle life and rate performance of the secondary battery.
A second aspect of the present application provides a method for preparing the separator according to the first aspect of the present application, including the following steps: S1, providing porous substrate; S2, providing a slurry by mixing a material that constitutes the three-dimensional skeleton structure and a filler in a predetermined proportion in a solvent to formulate the slurry; S3, coating: coating one or more surfaces of the porous substrate with the slurry, and drying to obtain a separator, wherein the separator includes a porous substrate and a coating layer disposed on one or more surfaces of the porous substrate, and the coating layer includes a three-dimensional skeleton structure and a filler, and at least a portion of the filler is filled in the three-dimensional skeleton structure, and the filler is secondary particles formed by agglomeration of primary particles.
The preparation method of the separator of the present application can provide a coating layer through one coating process, which greatly simplifies the production process of the separator.
In some embodiments of the present application, the slurry further includes inorganic particles with primary particle morphology.
In some embodiments of the present application, the method further includes the step of: S4, secondary coating: coating at least part of surface of the coating layer with a slurry containing a granular binder, and drying to form an adhesive layer.
A third aspect of the present application provides a secondary battery, comprising the separator of the first aspect of the present application or the separator prepared by the method of the second aspect of the present application.
A fourth aspect of the present application provides an electrical device, comprising the secondary battery according to the third aspect of the present application.
The separator provided in this application can have the combined characteristics of high heat resistance, high bonding strength, good electrolyte infiltration and retention and the like, which further enables secondary battery using the separator to have the combined characteristics of high energy density, high thermal safety performance, long cycle life, and good rate performance. The electrical device of the present application comprises the secondary battery provided by the present application, and thus has at least the same advantages as the secondary battery.
In order to explain the technical solutions of the embodiments of the present application more clearly, the following will briefly introduce the drawings that need to be used in the embodiments of the present application. Apparently, the drawings described below are only some embodiments of the present application. A person of ordinary skill in the art can obtain other drawings based on these drawings without creative work.
In the drawings, the drawings are not necessarily drawn to scale. The reference numerals are defined as follows: 1—battery pack; 2—upper case body; 3—lower case body; 4—battery module; 5—secondary battery; 51—housing; 52—electrode assembly; and 53—cover.
Hereafter, embodiments of the separator, the preparation method therefor and the secondary battery and electrical device related thereto of the present application will be specifically described in detail with appropriate references to the accompanying drawings. However, unnecessary detailed description may be omitted. For example, detailed descriptions of well-known items and repeated descriptions of substantially the same configurations may be 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 description 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.
A “range” disclosed herein is defined in terms of lower and upper limits, and a given range is defined by selecting a lower limit and an upper limit that define the boundaries of the particular range. Ranges defined in this manner may be inclusive or exclusive of end values and may be combined arbitrarily, that is, any lower limit may be combined with any upper limit to form a range. For example, if ranges of 60-120 and 80-110 are listed for a particular parameter, it is to be understood that ranges of 60-110 and 80-120 are also contemplated. Additionally, if the minimum range values 1 and 2 are listed, and the maximum range values 3, 4, and 5 are listed, the following ranges are all expected: 1-3, 1-4, 1-5, 2-3, 2-4 and 2-5. In the present application, unless stated otherwise, the numerical range “a-b” represents an abbreviated representation of any combination of real numbers between a and b, where both a and b are real numbers. For example, the numerical range “0-5” means that all real numbers between “0-5” have been listed herein, and the range “0-5” is just an abbreviated representation of the combination of these numerical values. In addition, when a parameter is expressed as an integer greater than or equal to 2, it is equivalent to disclose that the parameter is, for example, an integer of 2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12, and the like.
Unless stated otherwise, all the embodiments and the optional embodiments of the present application can be combined with each other to form a new technical solution, and such a technical solution should be considered to be included in the disclosure of the present application.
Unless stated otherwise, all technical features and optional technical features of the present application can be combined with each other to form a new technical solution, and such a technical solutions should be considered to be included in the disclosure of the present application.
Unless stated otherwise, all steps of the present application can be carried out sequentially, and also can be carried out randomly, preferably they are carried out sequentially. For example, the method includes steps (a) and (b), indicating that the method may include steps (a) and (b) performed in sequence, or that the method may include steps (b) and (a) performed in sequence. For example, reference to the method further comprising step (c) indicates that step (c) may be added to the method in any order. As an example, the method may comprises steps (a), (b) and (c), steps (a), (c) and (b), or steps (c), (a) and (b), and the like.
Unless stated otherwise, the transition phases “comprising” and “including” mentioned in the present application means that it is drafted in an open mode or in a close mode. For example, the transition phases “comprising” and “including” may mean that other components not listed may also be included or contained, or only the listed components may be included or contained.
In the present application herein, unless otherwise stated, 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 satisfy the condition “A or B”: A is true (or exists) and B is false (or does not exist); A is false (or does not exist) and B is true (or exists); or both A and B are true (or exist).
Unless otherwise specified, the terms used in this application have the well-known meanings generally understood by those skilled in the art.
Unless otherwise specified, a numerical value for each parameter mentioned in the present application can be determined by various test methods commonly used in the art, for example, can be determined according to the test methods given in the Examples of the present application.
Normally, a secondary battery comprises an electrode assembly and an electrolyte, and the electrode assembly comprises a positive electrode plate, a negative electrode plate and a separator, the separator is disposed between the positive electrode plate and the negative electrode plate and is mainly used to prevent short circuit between positive electrode and negative electrode and meanwhile allows active ions to pass through to form a circuit.
With the application and promotion of secondary batteries, the requirements for energy density, service life and rate performance of secondary battery are getting higher and higher. To obtain a thinner separator is an effective measure to increase energy density of secondary batteries. Currently, the separators used in commercial secondary batteries are usually polyolefin porous films, such as polyethylene porous films, polypropylene porous films or polypropylene/polyethylene/polypropylene three-layer composite films, with melting points between 130° C. and 160° C. As a result, when the thickness of the separator is reduced, the heat resistance of the separator will deteriorate, and a significant thermal shrinkage effect will occur when the separator is heated, which causes direct contact between the positive and negative electrodes inside the battery, thereby resulting in internal short circuits and increasing the safety risk of secondary batteries.
In addition, the separator also needs to satisfy good wettability and retention characteristics for the electrolytic solution. In the long-term charge and discharge process of the secondary battery, the separator gradually dries up and fails, which is an important reason for the capacity decline and service life shortening of the secondary battery. This is because the internal resistance of the battery increases after the separator dries up, which leads to the incomplete charge and discharge, and then leads to the rapid capacity attenuation and a significantly shortened service life of the secondary battery. When the separator is thinned, its electrolyte wettability and retention characteristics deteriorate, thereby further exacerbating the capacity attenuation.
In order to solve the above problems, the current measures are mainly to apply a heat-resistant inorganic ceramic layer on the polyolefin porous film, which can increase the mechanical strength of the separator, reduce the shrinkage of the separator when heated, and reduce the risk of short circuit between positive electrode and negative electrode inside the batteries. In addition, as compared with the polyolefin porous film, the inorganic ceramic layer can further improve the electrolyte wettability and retention characteristics due to the presence of hydroxyl groups on surface, thereby improving the cycle performance of the secondary battery to a certain extent.
However, commercially available inorganic ceramic particles have relatively large particle size, thus will increase the overall thickness of the separator, resulting in the inability to balance the energy density of secondary batteries, especially in the field of power batteries, which is not conducive to increasing the cruising range. In addition, due to the relatively large particle size of inorganic ceramic particles, the number of layers laminated on the polyolefin porous film is reduced (usually ≤5 layers), which results in limited improvement in the heat resistance of the separator. Nanosizing inorganic ceramic particles can reduce the thickness of the coating layer and alleviate the adverse impact on the energy density of secondary batteries. However, the coating layer formed by nanosized inorganic ceramic particles has low porosity and will easily block the polyolefin porous film, thus leading to the reduction of overall porosity of the separator and an increase of the ion impedance of the separator and an obstruction of ion transport, which in turn leads to a deterioration in the capacity exertion and rate performance of the secondary battery. Meanwhile, due to the high specific surface area of nanosized inorganic ceramic particles and the contact between particles being point contact, a large amount of binder is required to ensure the adhesiveness between particles, whereas the large amount of binder will lead to the problem of blocking pores, which is detrimental to the rate performance of the secondary battery, for example, the easy formation of dendrites on the surface of the negative electrode, which is in turn further detrimental to the capacity exertion and energy density and service life of secondary battery. In addition, the adhesiveness between the inorganic ceramic layer and the polyolefin porous membrane is also poor, so the inorganic ceramic layer is easy to fall off during the long-term charge and discharge process of the secondary battery and causes a series of safety problems.
Therefore, the separator in the existing art often struggles to have the combined characteristics of high energy density, high thermal safety performance, long cycle life and and good rate performance of secondary battery.
The inventors of the present application have unexpectedly found during the research that by disposing a coating layer comprising a three-dimensional skeleton structure and a filler with secondary particle morphology on surface of porous substrate of the separator, the separator can have the combined characteristics of high heat resistance, high bonding strength, good electrolyte infiltration and retention characteristics, thereby enabling the secondary battery to have the combined characteristics of high energy density, high thermal safety performance, long cycle life and good rate performance.
Specifically, the first aspect of embodiments of the present application provides a separator, comprising a porous substrate and a coating layer disposed on one or more surfaces of the porous substrate, wherein the coating layer comprises a three-dimensional skeleton structure and a filler, and at least a portion of the filler is filled in the three-dimensional skeleton structure, and the filler is secondary particles formed by agglomeration of primary particles. In the present application, “three-dimensional framework structure” refers to a structural body having a three-dimensional spatial shape and having certain pores, which may be formed by overlapping materials that constitute the three-dimensional skeleton structure with each other.
The inventors of the present application have unexpectedly found through a lot of researches that by disposing a coating layer comprising a three-dimensional skeleton structure and a filler with secondary particle morphology on one or more surfaces of porous substrate of the separator and by filling at least a portion of the filler in the three-dimensional structure, the obtained separator can have the combined characteristics of high heat resistance, high bonding strength, good electrolyte infiltration and retention characteristics, thereby enabling the secondary battery to have the combined characteristics of high energy density, high thermal safety performance, long cycle life and good rate performance.
Although the mechanism is not very clear, the inventors of the present application anticipate the possible reasons including the following points.
First, the filler in the coating layer is secondary particles formed by agglomeration of primary particles, and the filler with secondary particle morphology has the advantages of large specific surface area and good affinity with the three-dimensional skeleton structure, thus can interact with the three-dimensional skeleton structure to from a stable spatial network structure. This can not only increase the number of ion conductivity channels of the separator, promote ion transport, but also improve the electrolyte infiltration and retention characteristics of the separator. Therefore, the secondary battery using the separator of this application can have a long cycle life and good rate performance.
Second, at least a portion of the filler is filled in the three-dimensional skeleton structure, which helps the filler and the three-dimensional skeleton structure to form an embedding effect, thereby not only increasing the heat resistance of the separator, reducing the shrinkage of the separator when heated, reducing the risk of short circuit between the positive electrode and the negative electrode, resulting in high thermal safety performance of the secondary battery, but also maintaining high bonding strength between the coating layer and the porous substrate, preventing the filler from falling off during the long-term charge and discharge of the secondary battery.
Third, the coating layer of the present application includes a three-dimensional skeleton structure, and at least a portion of the filler is filled in the three-dimensional skeleton structure, thus there are many contact sites between the filler and the three-dimensional skeleton structure, which can reduce the amount of binder used in the coating layer, thereby effectively reducing the risk of clogging by the binder and further improving the cycle life and rate performance of the secondary battery.
Fourth, since the coating layer of the present application has high heat resistance, thus thinner porous substrates can be used, and the secondary battery can further have high energy density.
In some embodiments, at least a portion of the filler is filled in the three-dimensional skeleton structure, other portions of the filler may be located on the surface of the three-dimensional skeleton structure and/or at the interface between the three-dimensional skeleton structure and the porous substrate, and a small portion of the filler may be embedded in the porous substrate at the interface position between the three-dimensional skeleton structure and the porous substrate, for example, during winding of the electrode assembly, a small portion of the filler at the interface position is embedded in the matrix and/or pores of the porous substrate due to external pressure.
In some embodiments, the primary particles that constitute the filler may have an average particle size of optionally from 8 nm to 30 nm, optionally from 10 nm to 20 nm. As a result, the filler can have good secondary particle morphology, and the appropriate ranges allow the filler and the three-dimensional skeleton structure to better overlap to form an integrated effect, thereby preventing the filler and the material that constitutes the three-dimensional skeleton structure from entering into the pores of the porous substrate after the three-dimensional skeleton structure collapses. The entering causes pore plugging of the porous substrate and affecting the ion transport.
In some embodiments, the filler may have an average particle size of ≤200 nm, optionally from 50 nm to 200 nm. As a result, the filler can have a higher specific surface area, and the filler with an average particle size within the suitable ranges can further be better matched with the length of the three-dimensional skeleton structure, so that the filler and the three-dimensional skeleton structure can be better overlapped to form an integrated effect, thereby increasing the affinity between the filler and the three-dimensional skeleton structure and increasing the electrolyte infiltration and retention characteristics of the separator.
In some embodiments, the filler may have a BET specific surface area of ≥20 m2/g, optionally from 30 m2/g to 80 m2/g. As a result, the filler has better affinity with the three-dimensional skeleton structure, and meanwhile the filler can improve the electrolyte infiltration and retention characteristics of the separator.
In some embodiments, the filler may comprise one or more selected from inorganic particles and organic particles.
Optionally, the inorganic particles comprise one or more of boehmite (γ-AlOOH), aluminum oxide (Al2O3), barium sulfate (BaSO4), magnesium oxide (MgO), magnesium hydroxide (Mg(OH)2), silicon oxide SiOx (0<x≤2), tin dioxide (SnO2), titanium oxide (TiO2), calcium oxide (CaO), zinc oxide (ZnO), zirconium oxide (ZrO2), yttrium oxide (Y2O3), nickel oxide (NiO), hafnium dioxide (HfO2), cerium oxide (CeO2), zirconium titanate (ZrTiO3), barium titanate (BaTiO3), and magnesium fluoride (MgF2). More optionally, the inorganic particles comprise one or more of boehmite (γ-AlOOH), aluminum oxide (Al2O3), barium sulfate (BaSO4), magnesium oxide (MgO), silicon oxide SiOx (0<x ≤2), titanium oxide (TiO2), zinc oxide (ZnO), cerium oxide (CeO2), and barium titanate (BaTiO3).
Optionally, the organic particles comprise one or more of polystyrene and polyacrylic wax.
In some embodiments, the filler may comprise inorganic particles with secondary particle morphology, and the inorganic particles with secondary particle morphology have α crystal form including two or more of α crystal form, θ crystal form, γ crystal form and η crystal form. Optionally, the inorganic particles with secondary particle morphology have a crystal form including two or more of α crystal form, θ crystal form and γ crystal form.
In the X-ray diffraction spectra measured by using an X-ray diffraction meter, the inorganic particles with secondary particle morphology of α crystal form have diffraction peaks at 2θ of 57.48°±0.2° and 43.34°±0.2°. In some embodiments, based on the total weight of the inorganic particles with secondary particle morphology, the inorganic particles with secondary particle morphology of α crystal form is present in an amount of ≥1.2 wt. %, optionally from 1.2 wt. % to 10 wt. %, more optionally from 1.2 wt. % to 5 wt. % in the inorganic particles with secondary particle morphology.
In the X-ray diffraction spectra measured by using an X-ray diffraction meter, the inorganic particles with secondary particle morphology of θ crystal form have diffraction peaks at 2θ of 36.68°±0.2° and 31.21°±0.2°. In some embodiments, based on the total weight of the inorganic particles with secondary particle morphology, the inorganic particles with secondary particle morphology of θ crystal form is present in an amount of ≥50 wt. %, optionally from 60 wt. % to 85 wt. %, more optionally from 60 wt. % to 82.5 wt. % in the inorganic particles with secondary particle morphology.
In the X-ray diffraction spectra measured by using an X-ray diffraction meter, the inorganic particles with secondary particle morphology of γ crystal form have diffraction peaks at 2θ of 66.95°±0.2° and 45.91°±0.2°. In some embodiments, based on the total weight of the inorganic particles with secondary particle morphology, the inorganic particles with secondary particle morphology of γ crystal form is present in an amount of ≥10 wt. %, optionally from 15 wt. % to 60 wt. %, more optionally from 15 wt. % to 35 wt. % in the inorganic particles with secondary particle morphology.
In the X-ray diffraction spectra measured by using an X-ray diffraction meter, the inorganic particles with secondary particle morphology of η crystal form have diffraction peaks at 2θ of 31.89°±0.2° and 19.37°±0.2°. In some embodiments, based on the total weight of the inorganic particles with secondary particle morphology, the inorganic particles with secondary particle morphology of η crystal form is present in an amount of ≤5 wt. %, optionally ≤2 wt. %, more optionally ≤1 wt. % in the inorganic particles with secondary particle morphology.
Inorganic particles with secondary particle morphology of α crystal form have the advantages of high hardness, good heat resistance, low dielectric constant, high safety and high true density; inorganic particles with secondary particle morphology of θ crystal form have moderate specific surface area and hardness, which can better improve the heat resistance and ion transport characteristics of the separator at the same time; inorganic particles with the secondary morphology of γ crystal form and η crystal form have the advantage of large specific surface area.
Therefore, by selecting the fillers of different crystal forms, it facilitates improving one or more of heat resistance, bonding strength, and electrolyte infiltration and retention characteristics of the separator.
In some embodiments, the filler comprises inorganic particles with secondary particle morphology, and the inorganic particles with secondary particle morphology have α crystal form including α crystal form, θ crystal form, γ crystal form and η crystal form, and the inorganic particles with secondary particle morphology of α crystal form may be present in an amount of from 1.2 wt. % to 5 wt. %, the inorganic particles with secondary particle morphology of θ crystal form may be present in an amount of from 60 wt. % to 82.5 wt. %, the inorganic particles with secondary particle morphology of γ crystal form may be present in an amount of from 15 wt. % to 35 wt. %, and the inorganic particles with secondary particle morphology of η crystal form may be present in an amount of ≤1 wt %, based on the total weight of the inorganic particles with secondary particle morphology.
The X-ray diffraction spectrum of the inorganic particles with the secondary particle morphology can be obtained by testing the following process including: oven drying the inorganic particles with the secondary particle morphology, milling in a mortar (such as an agate mortar) for 30 minutes, and then testing using an X-ray diffractometer (such as a Miniflex 600-C) to obtain the X-ray diffraction spectrum. Cu target, Ni filter, tube pressure of 40 KV, tube flow of 15 mA, and continuous scanning range of from 5° to 80° may be used during the test.
In some embodiments, the filler may comprise inorganic particles with secondary particle morphology, and the inorganic particles with secondary particle morphology can be prepared by the following process including: subjecting a precursor solution of the inorganic particles to an oxidation reaction by high pressure sputtering, then heating at 600° C. to 900° C. (for example, from 1 hour to 3 hours) to form small particles, and then drying at 150° C. to 250° C. (for example, from 30 minutes to 60 minutes) to obtain the inorganic particles with secondary particle morphology.
In some embodiments, the primary particles that constitute the filler have an average particle size of d1 nm, a material that constitutes the three-dimensional skeleton structure has an average particle size of d2 nm, and the separator satisfies: d1≤√{square root over (2)}d2. In this way, the materials that constitute the three-dimensional skeleton structure can be overlapped in the gaps between the primary particles that constitute the filler, which facilitates the overlap between the filler and the three-dimensional skeleton structure to form an integrated effect. Therefore, the coating layer can have a more stable spatial network structure, and the coating layer can further have a uniform nanopore structure, thereby enabling the separator better having the combined characteristics of high heat resistance, high bonding strength, and good electrolyte infiltration and retention.
In some embodiments, the shape of the filler may comprise one or more of a string, a chain, an amorphous, a spherical, a spheroid and a pyramid.
In some embodiments, a material that constitutes the three-dimensional skeleton structure may have an average diameter of ≤40 nm, optionally from 10 nm to 35 nm. When the average diameter of a material that constitutes the three-dimensional skeleton structure is within the suitable ranges, it can further improve the ion transport characteristics and voltage breakdown resistance characteristics of the separator, and at the same time it also facilitates the overlap between the material that constitutes the three-dimensional skeleton structure and the filler to form an integrated effect, thereby further improving the heat resistance of the separator. In addition, it can effectively avoid the following situations: when the average diameter of a material that constitutes the three-dimensional skeleton structure is too high, the intertwining effect of the three-dimensional skeleton structure formed therefrom is insufficient and the pores are relatively large, which may lead to insufficient voltage breakdown resistance characteristics of the separator. At the same time, it is not conducive to the overlap with the filler to form the integrated effect; and during the drying process of coating layer, the three-dimensional skeleton structure is easy to collapse due to the lack of support by the filler, thereby causing the pore plugging due to the directly contact with the porous substrate, which may further affect the ion transport characteristics.
In some embodiments, a material that constitutes the three-dimensional skeleton structure may have an average length of from 100 nm 600 nm, optionally from 200 nm to 450 nm. When the average length of the material that constitutes the three-dimensional skeleton structure is in the appropriate ranges, the heat resistance and ion transport characteristics of the separator may be further improved. In addition, it can effectively avoid the following situations: when the average length of the material that constitutes the three-dimensional skeleton structure is too low, the overlap effect between the material and the filler is poor, the heat resistance of the coating layer becomes worse, and during the drying process of the coating layer, the three-dimensional skeleton structure is easy to collapse due to the lack of support by the filler, which may easily cause pore plugging and hinder ion transport and moisture discharge, and thus may also affect the thermal safety performance, cycle performance and rate performance of the secondary battery; when the average length of the material that constitutes the three-dimensional skeleton structure is too high, the coating slurry has high viscosity and poor flowability, which may affect the coating process of the coating slurry and thus affect the quality of the coating layer, for example affect the heat resistance and ion transport characteristics of the separator.
In some embodiments, a material that constitutes the three-dimensional skeleton structure may have an aspect ratio of from 5 to 60, optionally from 10 to 30. When the aspect ratio of the material that constitutes the three-dimensional skeleton structure is in the appropriate ranges, the electrolyte infiltration and retention characteristics of the separator may be further improved. In addition, it can effectively avoid the following situations: when the aspect ratio of the material that constitutes the three-dimensional skeleton structure is too low, the overlap effect between the material and the filler is poor, the heat resistance of the coating layer becomes worse, and during the drying process of the coating layer, the three-dimensional skeleton structure is easy to collapse due to the lack of support by the fillers, which may easily cause pore plugging and hinder ion transport and moisture discharge, and thus may also affect the thermal safety performance, cycle performance and rate performance of the secondary battery; when the aspect ratio of the material that constitutes the three-dimensional skeleton structure is too high, the three-dimensional skeleton structure as formed has relatively small pores, which may cause the deterioration of ion transport characteristics of the separator.
The average length and average diameter of the material that constitutes the three-dimensional skeleton structure may be measured by the following method: cutting a sample of 3.6 mm×3.6 mm from any area of the separator, mapping the micro-morphology and structure of the coating layer in the sample by scanning electron microscope (such as ZEISS Sigma 300) using high vacuum mode and a working voltage of 3 kV and magnification of 30,000 times, to obtain SEM images; selecting several (for example, 5 or more) test areas for statistically recording lengths according to the obtained SEM images, with each test area having a size of 0.5 μm×0.5 μm, and then taking the average of the lengths obtained from individual test areas as the average length of the material that constitutes the three-dimensional skeleton structure; selecting several (for example, 5 or more) test areas for statistically recording diameters using Nano Measurer particle size distribution statistics software according to the obtained SEM images, with each test area having a size of 0.5 μm×0.5 μm, and then taking the average of the diameters obtained from individual test areas as the average diameter of the material that constitutes the three-dimensional skeleton structure.
In some embodiments, the three-dimensional skeleton structure may be formed by fibrous objects, and the morphology of the fibrous objects may optionally comprise one or more of a rod shape, tubular shape (for example, a hollow tubular) and fibrous shape. Suitable material is conducive to the formation of a more stable spatial network structure from the three-dimensional skeleton structure and the filler, especially with the primary particles that constitute the filler, thereby further improving the heat resistance and ion transport characteristics and electrolyte wettability and retention characteristics of the separator.
In the present application, the “fibrous object” refers to a material having an aspect ratio of 5 or more.
In some embodiments, the fibrous objects may comprise one or more of organic materials and inorganic materials. The material of the fibrous objects is not particularly limited as long as it has electrical insulating property, electrochemical stability, and stability to electrolytic solution, and may be an organic material or an inorganic material.
Optionally, the organic material comprises one or more of nanocellulose, polytetrafluoroethylene nanofibers and polyamide nanofibers. Optionally, the inorganic materials comprise one or more of halloysite nanotubes, nanorod-shaped alumina, nanorod-shaped boehmite, nanorod-shaped silica and glass fiber.
In some embodiments, a material that constitutes the three-dimensional skeleton structure may comprise nanocellulose. Optionally, the nanocellulose comprises one or more of cellulose nanofibers (CNF, also referred to as nanofibril cellulose or microfibril cellulose), cellulose nanowhiskers (CNC, also referred to as cellulose nanocrystals, nanocrystalline cellulose), and bacterial nanocellulose (BNC, also referred to as bacterial cellulose or microbial cellulose). Optionally, the nanocellulose comprises cellulose nanowhiskers, which have the advantage of high crystallinity, thereby enabling better improvement of heat resistance of the separator.
Nanocellulose is a general term for cellulose with any one dimensional size of nano-scale (e.g., 100 nm or lower), and has the properties of both cellulose and nano-particles. Nanocellulose may be a polymer nanomaterial extracted from wood, cotton, and other materials in nature through one or more means in chemistry, physics, biology, etc. It has the advantages of wide sources, low cost, biodegradability, high modulus and high specific surface area, so it is an excellent substitute for traditional petrochemical resources and can effectively alleviate environmental pollution and shortage of petrochemical resources. Nanocellulose also has good high temperature resistance, and relatively small volume change after being heated, which can improve the heat resistance of the separator; at the same time, compared with traditional inorganic ceramic particles, nanocellulose has smaller density, which may further reduce the weight of secondary batteries and improve the weight energy density of secondary batteries.
The three-dimensional skeleton structure formed of the nanocellulose may further have fine nanopores to prevent current leakage, thus enabling the separator to have the combined characteristics of good electrolyte wettability and retention characteristics and good voltage breakdown resistance characteristics.
In some embodiments, the nanocellulose may comprise one or more of unmodified nanocellulose (also referred to as hydroxyl nanocellulose) and modified nanocellulose, and optionally is modified nanocellulose.
The modified nanocellulose comprises a hydroxyl group and a modifying group. In some embodiments, the modified nanocellulose comprises a modifying group, and the modifying group comprises one or more of an amino group, a carboxyl group, an aldehyde group, a sulfonic acid group, a boric acid group, and a phosphoric acid group, and optionally comprises one or more of a sulfonic acid group, a boric acid group, and a phosphoric acid group.
The inventors have found in further research that when nanocellulose has the above-mentioned specific modifying group, on one hand, it can effectively improve the heat resistance of the separator, thereby improving the thermal safety performance of the secondary battery; on the other hand, it can further improve the bonding strength between the coating layer and the porous substrate.
When the nanocellulose has the above-mentioned specific modifying groups, it also facilitates the overlap between the nanocellulose and the filler to form an integrated effect, which enables the coating layer to have a more stable spatial network structure, thereby improving the electrolyte infiltration and retention characteristics of the separator and improving ion transport characteristics and voltage breakdown resistance characteristics of the separator, and thereby being beneficial to matching with the high-voltage positive electrode active materials and further improving the energy density of the secondary battery.
In addition, the presence of modifying groups may further reduce the proportion of hydroxyl groups, which can ensure that the coating slurry has an appropriate viscosity and is thus more conducive to coating process, thereby improving the production efficiency of separator and the uniformity of coating layer.
In some embodiments, a molar ratio of the modifying group to the hydroxyl group may be from 1:4 to 4:1, optionally from 2:3 to 7:3. When the molar ratio of the modifying group to the hydroxyl group is in the appropriate ranges, the heat resistance, ion transport characteristics and electrolyte infiltration and retention characteristics of the separator can be further improved. In addition, it can effectively avoid the following situations: when the molar ratio of the modifying group to the hydroxyl group is too small, the further improvement effect of the modifying group on the heat resistance and ion transport characteristics of the separator may not be apparent; when the molar ratio of modifying group to hydroxyl group is too high, the electrolyte infiltration and retention characteristics of the separator may deteriorate, which may affect the cycle performance and safety performance of the secondary battery and meanwhile may also lead to the decline of the heat resistance of the separator and may further affect the thermal safety performance of the secondary battery.
The types of modifying group in nanocellulose may be determined by infrared spectroscopy. For example, the infrared spectrum may be used for test a material by determine the characteristic peaks contained in the material, thus determining the types of modifying group. Specifically, instruments and methods known in the field, for example an infrared spectrometer (such as IS10 Fourier transform infrared spectrometers Company in the United States), may be used for performing an analysis of infrared spectrum of a material according to GB/T 6040-2019 General Rules for Infrared Spectroscopy Analysis.
In some embodiments, a material that constitutes the three-dimensional skeleton structure comprises a sulfonic acid group, and the material that constitutes the three-dimensional skeleton structure has a sulfur amount of ≥0.1 wt. %, optionally from 0.2 wt. % to 0.5 wt. %, based on the total weight of the material that constitutes the three-dimensional skeleton structure. Optionally, a material that constitutes the three-dimensional skeleton structure comprises nanocellulose, more optionally comprises cellulose nanowhiskers.
The sulfur amount in the material that constitutes the three-dimensional skeleton structure may be determined by the testing method including: drying the material that constitutes the three-dimensional skeleton structure, grinding in a mortar (for example, an agate mortar) for 30 minutes, and then testing using an X-ray diffractometer (for example, a Miniflex 600-C) to obtain the amount of the sulfur element. Cu target, Ni filter, tube pressure of 40 KV, tube flow of 15 mA, and continuous scanning range of from 5° to 80° may be used during the test.
In some embodiments, the three-dimensional skeleton structure may be present in an amount of from 5 wt. % to 40 wt. %, optionally from 10 wt. % to 25 wt. %, based on the total weight of the coating layer. When the amount of the three-dimensional skeleton structure is within the suitable ranges, it can ensure that the coating slurry has a suitable viscosity, which is more conducive to coating process; In addition, it is also beneficial to the overlap between the three-dimensional skeleton structure and the filler to form an integrated effect, which enables the coating layer to have a more stable spatial network structure, result further improving the ion transport, electrolyte infiltration and retention characteristics and the voltage breakdown resistance of the separator.
During the long-term charge and discharge of the secondary battery, the volume of the whole battery will increase due to the irreversible changes of microstructure of the positive electrode active materials and negative electrode active materials. Especially, when the secondary battery is charged rapidly, the increase of the volume of the negative electrode active materials is higher after the intercalation of active ions. After the expansion of the battery, the separator will be squeezed and/or stretched, which will easily lead to the damage of the separator and thus increase the risk of short circuit between positive electrode and negative electrode. Therefore, the separator is also required to have good external force extrusion resistance. At least a portion of the filler being filled in the three-dimensional skeleton structure helps the coating layer to have a stable spatial network structure, which can improve the ion transport characteristics and heat resistance of the separator; In addition, it may also improve the tensile strength, puncture resistance and external force extrusion resistance of the separator.
In some embodiments, the filler may be present in an amount of ≥60 wt. %, optionally from 70 wt. % to 90 wt. %, based on the total weight of the coating layer. When the amount of the filler is in the appropriate ranges, it can ensure that the coating slurry has appropriate viscosity, which is more conducive to coating process; In addition, it is also beneficial to overlap with the three-dimensional skeleton structure to form an integrated effect, which enables the coating layer to have a more stable spatial network structure, thereby further improving the tensile strength, puncture resistance, and external compression resistance of the separator.
In some embodiments, the coating layer may further comprise inorganic particles with primary particle morphology, and at least a portion of the inorganic particles with primary particle morphology is embedded in the coating layer. The inorganic particles with primary particle morphology has a relative large particle size and a relative high strength, which can better exert its supporting role in the coating layer and reduce the shrinkage of the secondary particles, and reduce the amount of binder, thereby improving the heat resistance of the separator; and the inorganic particles with primary particle morphology has a relatively large particle size, which also helps the separator to have more pore/channel structure and less moisture content when the inorganic particles with primary particle morphology are present in a relatively low amount, thereby further improving the ion transport and the electrolyte infiltration and retention characteristics of the separator, and meanwhile improving the cycle performance of the secondary battery.
In some embodiments, at least a portion of the inorganic particles with primary particle morphology is embedded in the coating layer, and there may also be a portion of the inorganic particles with primary particle morphology protruding from the surface of the coating layer.
In some embodiments, the inorganic particles with primary particle morphology may have an average particle size of from 200 nm to 800 nm, optionally from 200 nm to 400 nm. As a result, the inorganic particles with primary particle morphology can better exert the supporting role, so that the coating layer maintains a stable pore/channel structure during long-term charge and discharge, which is beneficial to ion transport and meanwhile improves the heat resistance of the separator.
In some embodiments, the inorganic particles with primary particle morphology may have a BET specific surface area of ≤10 m2/g, optionally from 3 m2/g to 7 m2/g. As a result, the inorganic particles with primary particle morphology can better exert the supporting role, so that the coating layer maintains a stable pore/channel structure during long-term charge and discharge, which is beneficial to ion transport and meanwhile improves the heat resistance of the separator.
In some embodiments, the inorganic particles with primary particle morphology may have a crystal form including one or more of α crystal form and γ crystal form, and optionally have a crystal form including α crystal form. Inorganic particles with primary particle morphology of α crystal form have the advantages of high hardness, good heat resistance, low dielectric constant, high safety and high true density, which can further improve the heat resistance of the coating layer.
In some embodiments, the inorganic particles with primary particle morphology have a crystal form including α crystal form, and based on the total weight of the inorganic particles with primary particle morphology, the inorganic particles with primary particle morphology of α crystal form may be present in an amount of ≥90 wt. % in the inorganic particles with primary particle morphology, and optionally from 95 wt % to 100 wt %;
In some embodiments, the inorganic particles with primary particle morphology may have a shape including one or more of spherical, dumbbell, and polygonal.
In some embodiments, the inorganic particles with primary particle morphology may comprise one or more of inorganic particles with a dielectric constant of 5 or more, inorganic particles having ion conductivity but no ion storage capability and inorganic particles capable of undergoing electrochemical reactions.
Optionally, the inorganic particles with a dielectric constant of 5 or more comprise one or more of: oehmite, aluminum oxide (or alumina), zinc oxide, silicon oxide, titanium oxide, zirconium oxide, barium oxide, calcium oxide, magnesium oxide, nickel oxide, tin oxide, cerium oxide, yttrium oxide, hafnium oxide, aluminum hydroxide, magnesium hydroxide, silicon carbide, boron carbide, aluminum nitride, silicon nitride, boron nitride, magnesium fluoride, calcium fluoride, barium fluoride, barium sulfate, magnesium aluminum silicate, lithium magnesium silicate, sodium magnesium silicate, bentonite, hectorite, zirconium titanate, barium titanate, Pb(Zr,Ti)O3 (abbreviated as PZT), Pb1-mLamZr1-nTinO3 (abbreviated as PLZT, 0<m<1, 0<n<1), Pb(Mg3Nb2/3)O3-PbTiO3 (abbreviated as PMN-PT) and their respective modified inorganic particles. Optionally, the modification mode of each inorganic particle may be chemical modification and/or physical modification. The chemical modification mode includes coupling agent modification (by using for example silane coupling agent, titanate coupling agent, etc.), surfactant modification, and polymer grafting modification, etc. The physical modification mode may be mechanical force dispersion, ultrasonic dispersion, high-energy treatment and the like. Through modification treatment, the agglomeration of inorganic particles may be reduced, thus enabling the coating layer to have a more stable and more uniform spatial network structure; in addition, by modifying inorganic particles with surfactants or polymer or coupling agents with specific functional groups, it also helps to improve the electrolyte infiltration and retention characteristics of coating layer and improve the adhesiveness of the coating layer to the porous substrate.
Optionally, the inorganic particles with ion conductivity but without ion storage capability comprise one or more of Li3PO4, lithium titanium phosphate Lix1Tiy1(PO4)3, lithium aluminum titanium phosphate Lix2Aly2Tiz1(PO4)3, (LiAlTiP)x3Oy3 type glass, lithium lanthanum titanate Lix4Lay4TiO3, lithium germanium thiophosphate Lix5Gey5Pz2Sw, lithium nitride Lix6Ny6, SiS2 type glass Lix7Siy7Sz3 and P2S5 type glass Lix8Py8Sz4, wherein 0<x1<2, 0<y1<3, 0<x2<2, 0<y2<1, 0<z1<3, 0<x3<4, 0<y3<13, 0<x4<2, 0<y4<3, 0<x5<4, 0<y5<1, 0<z2<1, 0<w<5, 0<x6<4, 0<y6<2, 0<x7<3, 0<y7<2, 0<z3<4, 0<x8<3, 0<y8<3, 0<z4<7. As a result, this can further improve the ion transport property of the separator.
Optionally, the inorganic particles capable of undergoing electrochemical reactions comprise one or more of lithium-containing transition metal oxides, lithium-containing phosphates, carbon-based materials, silicon-based materials, tin-based materials, and lithium-titanium compounds.
In some embodiments, the inorganic particles with primary particle morphology may be present in an amount of ≤30 wt. %, optionally from 5 wt. % to 25 wt. %, based on the total weight of the coating layer. As a result, the inorganic particles with primary particle morphology can better exert the supporting role, so that the coating layer maintains a stable pore/channel structure during long-term charge and discharge, which is beneficial to ion transport and meanwhile improves the heat resistance of the separator. In addition, it can effectively avoid the following situations: when the amount of the inorganic particles with primary particle morphology is high, the amount of the filler with secondary particle morphology decreases, which is not conducive to overlapping the filler with the three-dimensional skeleton structure and forming an integrated effect, and thus may affect the heat resistance, ion transport characteristics, and electrolyte wettability and retention characteristics of the separator.
In some embodiments, the coating layer may further comprise a non-granular binder. The type of the non-granular binder is not particularly limited in the present application, and any well-known material having good adhesiveness can be selected. Optionally, the non-granular binder comprises an aqueous solution-type binder, which has the advantages of good thermodynamic stability and environmental protection, thereby facilitating the preparation and application of the coating slurry. As an example, the aqueous solution-type binder may comprise one or more of an aqueous solution-type acrylic resin (for example, acrylic acid, methacrylic acid, sodium acrylate monomer homopolymer or copolymer with other comonomers), polyvinyl alcohol (PVA), isobutylene-maleic anhydride copolymer, and polyacrylamide.
Optionally, the non-granular binder in the coating layer has an amount of ≤2 wt. %, based on the total weight of the coating layer. The three-dimensional skeleton structure and the filler and the like in the coating layer of the present application can form a stable spatial network structure, thereby enabling the separator to maintain high adhesiveness under the premise of reducing the amount of binder.
In some embodiments, the coating layer may have a thickness of ≤1 μm, optionally from 0.5 μm to 0.8 nm. As a result, this contributes to improving the energy density of the secondary battery. In the present application, the thickness of the coating layer refers to the thickness of the coating layer on one side of the porous substrate.
In some embodiments, the porous substrate may have a thickness of ≤6 μm, optionally from 3 μm to 5 nm. The coating layer of the present application may significantly improve the heat resistance of the separator, so that a thinner porous substrate can be used, thus contributing to improving the energy density of the secondary battery.
The material of the porous substrate is not specially limited in the present application, and the porous substrate may be any known substrate with good chemical and mechanical stability; for example, the porous substrate may include one or more of a porous polyolefin-based resin film (e.g. one or more of polyethylene, polypropylene, and polyvinylidene fluoride), a porous glass fiber, and a porous non-woven fabric. The porous substrate may be a single-layer film or a multilayer film. When the porous substrate is a multilayer composite film, the materials of individual layers may be the same or different. In some embodiments, the separator may further comprise an adhesive layer, the adhesive layer is disposed on at least part of surface of the coating layer, and the adhesive layer comprises a granular binder. The adhesive layer can not only prevent the coating layer from peeling off and improve the safety performance of the secondary battery, but also improve the interface between the separator and the electrode and improve the cycle performance of the secondary battery.
Optionally, the granular binder comprises one or more of a homopolymer or copolymer of acrylate monomer, a homopolymer or copolymer of acrylic monomer, a homopolymer or copolymer of fluorine-containing olefin monomer. The comonomer includes, but is not limited to, one or more of an acrylate monomer, an acrylic monomer, an olefin monomer, a halogen-containing olefin monomer, a fluoroether monomer, and the like.
Optionally, the granular binder comprises a vinylidene fluoride-based polymer, such as a homopolymer of vinylidene fluoride monomer (VDF) and/or a copolymer of vinylidene fluoride monomer and a comonomer. The comonomer may be one or more of an olefin monomer, a fluorine-containing olefin monomer, a chlorine-containing olefin monomer, an acrylate monomer, an acrylic monomer, and a fluoroether monomer.
Optionally, the comonomer may comprise one or more of trifluoroethylene (VF3), chlorotrifluoroethylene (CTFE), 1,2-difluoroethylene, tetrafluoroethylene (TFE), hexafluoropropylene (HFP), perfluoro (alkylvinyl) ethers such as perfluoro (methylvinyl) ether (PMVE), perfluoro (ethylvinyl) ether (PEVE), perfluoro (propylvinyl) ether (PPVE), perfluoro (1,3-dioxole), and perfluoro (2,2-dimethyl-1,3-dioxole) (PDD).
In some embodiments, the separator has a longitudinal thermal shrinkage rate at 150° C. for 1 h of ≤5%, optionally from 0.5% to 3%.
In some embodiments, the separator has a lateral thermal shrinkage rate at 150° C. for 1 h of ≤5%, optionally from 0.5% to 3%.
The separator of the present application has low thermal shrinkage rate in both the lateral direction and the longitudinal direction at high temperature of 150° C., which can improve the safety performance of the secondary battery.
In some embodiments, the separator has a longitudinal tensile strength of ≥2000 kg/cm2, optionally from 2500 kg/m2 to 4500 kg/m2.
In some embodiments, the separator has a lateral tensile strength of ≥2000 kg/m2, optionally from 2500 kg/m2 to 4500 kg/m2.
The separator of the present application has high tensile strength in both the lateral direction and the longitudinal direction, which results in small probability of breakage of the separator when the secondary battery is expanded, thereby improving the safety performance of the secondary battery.
In some embodiments, the separator has a wetting length of ≥30 mm, optionally from 30 mm to 80 mm.
In some embodiments, the separator has a wetting speed of ≥3 mm/s, optionally from 3 mm/s to 10 mm/s.
The separator of the present application has good electrolyte infiltration and retention characteristics, which can improve the ion transport characteristics of the separator and the capacity exertion of the secondary battery.
In some embodiments, the separator has an air permeability of ≤300 s/100 mL, optionally from 100 s/100 mL to 230 s/100 mL. The separator of the present application has good air permeability, which can improve the ion transport characteristics of the separator and the capacity exertion of the secondary battery.
In this application, the average particle size or average particle diameter of a material has well-known meaning in the art, and may be measured with known instruments and methods in the art. For example, it can be determined by testing a material or separator using scanning electron microscopy, transmission electron microscopy, particle size distribution instrument to obtain a picture, randomly selecting a plurality of (for example, 10 or more) test particles (for example fillers with secondary particle morphology, and inorganic particles with primary particle morphology) from the picture, and recording the average value of the shortest diagonal length of the particles as the average particle size.
In this application, the specific surface area of a material has well-known meaning in the art, and may be measured with known instruments and methods in the art. For example, a method for analyzing and testing specific surface area by nitrogen adsorption is used according to GB/T 19587-2017, and the specific surface area can be calculated by the BET (BrunauerEmmett Teller) method. Optionally, the analyzing and testing specific surface area by nitrogen adsorption may be performed by a Tri-Star Model 3020 specific surface area & porosity analyzer from Micromeritics, USA.
In the present application, the thermal shrinkage rate, tensile strength, and air permeability of the separator have well-known meanings in the art and can be measured by methods known in the art. For example, they may be tested with reference to GB/T 36363-2018.
In this application, the wetting length and wetting speed of the separator have well-known meanings in the art, and may be measured with known instruments and methods in the art. An exemplary test method is as follows: cutting a separator into a sample with a width of 5 mm and a length of 100 mm, and fixing both ends of the sample and placing horizontally; Taking 0.5 mg of electrolyte and dropping it in the center of the sample, and after the specified time (1 min in this application), taking a photo and measuring the length of electrolyte diffusion, thereby obtaining the wetting length and wetting speed of the separator. In order to ensure the accuracy of the test results, a plurality of samples (for example, from 5 to 10) can be tested, and the test results are obtained by calculating average value. The electrolyte may be prepared by mixing ethylene carbonate (EC), ethyl methyl carbonate (EMC), and diethyl carbonate (DEC) in a volume ratio of 30:50:20 to obtain an organic solvent, and then dissolving a fully dried LiPF6 in the above organic solvent, to prepare an electrolyte with a concentration of 1 mol/L.
It should be noted that the parameters (for example, thickness, etc.) of coating layer in the above separator are all parameters of coating layer on one side of the porous substrate. When the coating layer is disposed on both sides of the porous substrate, if the coating parameters on either side satisfy the requirements in the present application, the separator is considered to fall within the scope of protection of the present application.
A second aspect of embodiments of the present application provides a method for preparing the separator according to the first aspect of embodiments of the present application, comprising the following steps: S1, providing porous substrate; S2, providing a slurry by mixing a material that constitutes the three-dimensional skeleton structure and a filler in a predetermined proportion in a solvent to formulate the slurry; S3, coating: coating one or more surfaces of the porous substrate with the slurry, and drying to obtain a separator, wherein the separator comprises a porous substrate and a coating layer disposed on one or more surfaces of the porous substrate, and the coating layer comprises a three-dimensional skeleton structure and a filler, and at least a portion of the filler is filled in the three-dimensional skeleton structure, and the filler is secondary particles formed by agglomeration of primary particles.
In some embodiments, in S2, the solvent may be water, such as deionized water.
In some embodiments, in S2, the slurry may further comprise other components, for example, may further comprise a dispersing agent, a wetting agent, a binder, and the inorganic particles with primary particle morphology and the like.
In some embodiments, in S2, the solid content of the slurry may be controlled between 28% and 45%, for example, may be between 30% and 38%. When the solid content of the slurry is within the above range, the film surface problem of the coating layer and the probability of occurrence of coating unevenness can be effectively reduced, thereby further improving the energy density and safety performance of the secondary battery.
In some embodiments, the material that constitutes the three-dimensional skeleton structure is a fibrous object, and the fibrous object may comprise one or more of organic materials and inorganic materials.
Optionally, the organic material comprises one or more of nanocellulose, polytetrafluoroethylene nanofibers and polyamide nanofibers. Optionally, the inorganic materials comprise one or more of halloysite nanotubes, nanorod-shaped alumina, nanorod-shaped boehmite, nanorod-shaped silica and glass fiber. Optionally, a material that constitutes the three-dimensional skeleton structure may comprise nanocellulose, optionally cellulose nanocrystals (CNC, also referred to as cellulose nanowhiskers, nanocrystalline cellulose).
In some embodiments, the nanocellulose can be obtained as follows: S21, providing a cellulose powder having a whiteness of ≥80%; S22, mixing and reacting the obtained cellulose powder with a modification solution, washing and removing impurities to obtain cellulose nanowhiskers; S23, adjusting the pH of the obtained cellulose nanowhiskers to neutral, and grinding and cutting to obtain nanocellulose.
Optionally, in S21, the above cellulose powder having a whiteness of ≥80% can be obtained commercially, or can be obtained by a chemical method (e.g., acid hydrolysis method, alkali treatment method, Tempo catalytic oxidation method), a biological method (e.g., enzymatic treatment method), a mechanical method (e.g., ultrafine grinding, ultrasonic crushing, high-pressure homogenization), or the like. The fiber raw material for preparing the above cellulose powder having a whiteness of ≥80% may comprise one or more of plant fibers such as cotton fibers (e.g. Gossypium fibers, kapok fibers), hemp fibers (e.g. sisal fibers, ramie fibers, jute fibers, flax fibers, marihuana fibers, abaca fibers, etc.), brown fibers, wood fibers, bamboo fibers, and grass fibers.
In some embodiments, the above-mentioned cellulose powder having a whiteness of ≥80% can also be prepared by: loosening the fiber raw material and slag removal, cooking with an alkaline solution (e.g. aqueous NaOH solution, which may have a concentration of 4 wt. % to 20 wt. %, optionally 5 wt. % to 15 wt. %), and then sequentially subjecting to water washing to remove impurities (e.g., water washing for 3 times to 6 times), bleaching (using for example sodium hypochlorite and/or hydrogen peroxide), acid washing to remove impurities, water washing to remove impurities, water discharging, and air drying, to obtain the cellulose powder.
In some embodiments, in S22, the modification solution may be an acid solution (e.g., an aqueous sulfuric acid solution, an aqueous boric acid solution, an aqueous phosphoric acid solution, an aqueous acetic acid solution) or an alkaline solution (for example a urea solution in organic solvent). Optionally, the modification solution is an acid solution.
Optionally, the acid solution may have a concentration of 5 wt. % to 80 wt. %. When an aqueous sulfuric acid solution is used as the modification solution, the concentration of the acid solution may be 40 wt. % to 80 wt. %, thus the cellulose powder having a sulfonic acid group can be obtained. When an aqueous boric acid solution is used as the modification solution, the concentration of the acid solution may be 5 wt. % to 10 wt. %, thus the cellulose powder having a boric acid group can be obtained. When an aqueous phosphoric acid solution is used as the modification solution, the concentration of the acid solution may be 45 wt. % to 75 wt. %, thus the cellulose powder having a phosphoric acid group can be obtained. When an aqueous acetic acid solution is used as the modification solution, the concentration of the acid solution may be 40 wt. % to 80 wt. %, thus the cellulose powder having a carboxylic acid group can be obtained.
Optionally, the urea solution in organic solvent is a urea solution in xylene, whereby the cellulose powder having an amine group can be obtained.
In some embodiments, in S22, optionally, the mass ratio of the cellulose powder to the modification solution may be from 1:2.5 to 1:50, optionally from 1:5 to 1:30.
When an aqueous sulfuric acid solution is used as the modification solution, the mass ratio of the cellulose powder to the acid solution may be from 1:5 to 1:30. When an aqueous boric acid solution is used as the modification solution, the mass ratio of the cellulose powder to the acid solution may be from 1:20 to 1:50. When an aqueous phosphoric acid solution is used as the modification solution, the mass ratio of the cellulose powder to the acid solution may be from 1:5 to 1:30. When an aqueous acetic acid solution is used as the modification solution, the mass ratio of the cellulose powder to the acid solution may be from 1:5 to 1:30. When a urea solution in organic solvent is used as the modification solution, the mass ratio of the cellulose powder to the urea solution in organic solvent may be from 1:4 to 1:40.
In some embodiments, in S22, when the modification solution is an acid solution, the reaction may be carried out at a condition of not higher than 80° C., optionally at a condition of from 30° C. to 60° C., and the reaction time between the cellulose powder and the modification solution may be from 0.5 h to 4 h, optionally from 1 h to 3 h.
In some embodiments, in S22, when the modification solution is an alkaline solution, the reaction may be carried out under conditions of from 100° C. to 145° C., and the reaction time of the cellulose powder and the modification solution may be from 1 h to 5 h.
In some embodiments, in S23, a grinder may be used for grinding, and a high pressure homogenizer may be used for cutting. By adjusting the grinding parameters of the grinder (e.g. number of grinding, grinding time, etc.) as well as the cutting parameters of the high-pressure homogenizer, nanocelluloses with different average diameters and/or different average lengths can be obtained.
In some embodiments, in S3, a coating machine is adopted in the coating step. In the present application, there is no particular limitation on the type of the coating machine, and for example, a commercially available coating machine can be used. The coating machine comprises a gravure roll; the gravure roll is used for transferring the coating slurry onto the porous substrate.
In some embodiments, in S3, transfer coating, spin spraying, dip coating, or the like may be adopted for the way of coating.
In some embodiments, the method further comprises the step of: S4, secondary coating: coating at least part of surface of the coating layer with a slurry containing a granular binder, and drying to form an adhesive layer.
The preparation method of the separator of the present application can provide a coating layer through one coating process, which greatly simplifies the production process of the separator.
Some raw materials and parameters such as their amounts used in the method for preparing the separator of the present application can be determined with respect to the separator of the first aspect of the embodiments of the present application, and will not be repeatedly described herein.
Unless otherwise specified, all raw materials used in the method for preparing the separator of the present application may be commercially available.
The third aspect of embodiments of the present application provides a secondary battery.
Secondary batteries, also known as rechargeable batteries or storage batteries, refer to batteries that can be used continuously by activating active materials through charging after the battery is discharged. Normally, a secondary battery comprises an electrode assembly and an electrolyte, and the electrode assembly comprises a positive electrode plate, a negative electrode plate and a separator, the separator is disposed between the positive electrode plate and the negative electrode plate and is mainly used to prevent short circuit between positive electrode and negative electrode and meanwhile allows active ions to pass through.
The present application has no particular limitation on the type of the secondary battery. For example, the secondary battery may be a lithium ion battery, a sodium ion battery, and the like. In particular, the secondary battery may be a lithium ion secondary battery.
The secondary battery of the third aspect of embodiments of the present application comprises the separator of the first aspect of embodiments of the present application or the separator prepared by the method of the second aspect of embodiments of the present application, wherein the separator is spaced between the positive electrode plate and the negative electrode plate. Optionally, the coating layer of the present application is present on at least the side of the separator close to the negative electrode plate. As a result, the secondary battery of the present application can have the combined characteristics of high energy density, high thermal safety performance, long cycle life and and good rate performance.
In some embodiments, the positive electrode plate comprises a positive electrode current collector and a positive electrode film layer which is disposed on one or more surfaces of the positive electrode current collector and comprises a positive electrode active material. For example, the positive current collector has two opposite surfaces along the thickness direction of the positive current collector, and the positive electrode film layer is disposed on any one or both of the two opposite surfaces of the positive current collector.
When the secondary battery of the present application is a lithium ion battery, the positive electrode active material may comprise, but is not limited to, one or more of lithium transition metal oxides, lithium-containing phosphates, and their respective modified compounds thereof. Examples of lithium transition metal oxides may include, but are not limited to, one or more of lithium cobalt oxide, lithium nickel oxide, lithium manganese oxide, lithium nickel cobalt oxide, lithium manganese cobalt oxide, lithium nickel manganese oxide, lithium nickel cobalt manganese oxide, lithium nickel cobalt aluminum oxide, and respective modified compounds thereof. Examples of lithium-containing phosphates may include, but are not limited to, one or more of lithium iron phosphate, composite of lithium iron phosphate with carbon, lithium manganese phosphate, composite of lithium manganese phosphate with carbon, lithium manganese iron phosphate, composite of lithium manganese iron phosphate with carbon, and respective modified compounds thereof.
In some embodiments, in order to further increase the energy density of the secondary battery, the positive electrode active material for the lithium-ion battery may comprise one or more of lithium transition metal oxides having general formula LiaNibCOcMdOeAf and modified compounds thereof. 0.8≤a≤1.2, 0.5≤b<1, 0<c<1, 0<d<1, 1≤e≤2, 0xf≤1, M is selected from one or more of Mn, Al, Zr, Zn, Cu, Cr, Mg, Fe, V, Ti and B, and A s selected from one or more of N, F, S and Cl.
As an example, positive electrode active materials for lithium-ion batteries may include one or more of LiCoO2, LiNiO2, LiMnO2, LiMn2O4, LiNi1/3Co1/3Mn1/3O2 (NCM333), LiNi0.5Co0.2Mn0.3O2 (NCM523), LiNi0.6CO0.2Mn0.2O2(NCM622), LiNi0.8Co0.1Mn0.1O2(NCM811), LiNi0.85Co0.15Al0.05O2, LiFePO4 and LiMnPO4.
When the secondary battery of the present application is a sodium ion battery, the positive electrode active material may include but not limited to one or more of sodium-containing transition metal oxides, polyanion materials (such as phosphate, fluorophosphate, pyrophosphate, sulfate, and the like salts), and Prussian blue materials.
As an example, a positive electrode active material for a sodium-ion battery may include one or more of NaFeO2, NaCoO2, NaCrO2, NaMnO2, NaNiO2, NaNi1/2Ti1/2O02, NaNi1/2Mn1/2O2, Na2/3Fe1/3Mn2/3O2, NaNi1/3Co1/3Mn1/3O2, NaFePO4, NaMnPO4, NaCoPO4, Prussian blue materials and the materials having the general formula XpM′q(PO4)rOxY3-x. In general formula XpM′q(PO4)rOxY3-x, 0<p≤4, 0<q≤2, 1≤r≤3, 0≤x≤2, X is selected from one or more of H+, Li+, Na+, K+ and NH4+, M′ is a transition metal cation and optionally is one or more of V, Ti, Mn, Fe, Co, Ni, Cu and Zn, and Y is a halogen anion and optionally is one or more of F, Cl and Br.
In the present application, the modified compounds of the above positive electrode active materials may be doping-modified and/or surface coating-modified of the positive electrode active materials.
In some embodiments, the positive electrode film layer may also optionally comprise a conductive agent for positive electrode. The present application does not particularly limit the type of conductive agent for positive electrode, and as an example, the conductive agent for positive electrode includes one or more of superconducting carbon, conductive graphite, acetylene black, carbon black, Ketjen black, carbon dots, carbon nanotubes, graphene, and carbon nanofibers. In some embodiments, the mass content of the conductive agent for positive electrode is ≤5 wt. %, based on the total weight of the positive electrode film layer.
In some embodiments, the positive electrode film layer may further optionally comprise a binder for positive electrode. The present application does not particularly limit the type of the binder for positive electrode, and as an example, the binder for positive electrode may include one or more of polyvinylidene fluoride (PVDF), polytetrafluoroethylene (PTFE), vinylidene fluoride-tetrafluoroethylene-propylene terpolymer, vinylidene fluoride-hexafluoropropylene-tetrafluoroethylene terpolymer, tetrafluoroethylene-hexafluoropropylene copolymer, and fluorinated acrylate resins. In some embodiments, the mass content of the binder for positive electrode is ≤5 wt. %, based on the total weight of the positive electrode film layer.
In some embodiments, the positive electrode current collector may be a metal foil or a composite current collector. As an example of the metal foil, aluminum foil may be used. The composite current collector may include a base layer of polymeric material and a layer of metallic material formed on one or more surfaces of the base layer of polymeric material. As an example, the metal material may comprise one or more of aluminum, aluminum alloy, nickel, nickel alloy, titanium, titanium alloy, silver, and silver alloy. As an example, the base layer of polymeric material may comprise one or more of polypropylene (PP), polyethylene terephthalate (PET), polybutylene terephthalate (PBT), polystyrene (PS), polyethylene (PE), and the like.
The positive electrode film layer is usually formed by applying a positive electrode slurry on a positive electrode current collector, drying and cold-pressing. The positive electrode slurry is usually formed by dispersing positive electrode active material, an optional conductive agent, an optional binder and any other components in a solvent and stirring them uniformly. The solvent may be N-methylpyrrolidone (NMP), but is not limited thereto.
In some embodiments, the negative electrode plate comprises a negative positive electrode current collector and a negative electrode film layer which is disposed on one or more surfaces of the negative electrode current collector and comprises a negative electrode active material. For example, the negative current collector has two opposite surfaces along the thickness direction of the negative current collector, and the positive electrode film layer is disposed on any one or both of the two opposite surfaces of the negative current collector.
The negative electrode active material can be a negative electrode active material well known in the art for secondary batteries. As an example, the negative electrode active material may include but not limited to one or more of natural graphite, artificial graphite, soft carbon, hard carbon, silicon-based material, tin-based material, and lithium titanate. The silicon-based material may include one or more of elemental silicon, silicon oxide, silicon-carbon composite, silicon-nitrogen composite, and silicon alloy. The tin-based material may include one or more of elemental tin, tin oxide, and tin alloy materials.
In some embodiments, the negative electrode film layer may also optionally comprise a conductive agent for negative electrode. The present application does not particularly limit the type of conductive agent for negative electrode, and as an example, the conductive agent for negative electrode may include one or more of superconducting carbon, conductive graphite, acetylene black, carbon black, Ketjen black, carbon dots, carbon nanotubes, graphene, and carbon nanofibers. In some embodiments, the mass content of the conductive agent for negative electrode is ≤5 wt. % based on the total weight of the negative electrode film layer.
In some embodiments, the negative electrode film layer may further optionally comprises a binder for negative electrode. The present application does not particularly limit the type of the binder for negative electrode, and as an example, the binder for negative electrode may include one or more of styrene-butadiene rubber (SBR), water-soluble unsaturated resin SR-1B, aqueous acrylic resins (e.g., polyacrylic acid PAA, polymethacrylic acid PMAA, sodium polyacrylate PAAS), polyacrylamide (PAM), polyvinyl alcohol (PVA), sodium alginate (SA), and carboxymethyl chitosan (CMCS). In some embodiments, the mass content of the binder for negative electrode is ≤5 wt. %, based on the total weight of the negative electrode film layer.
In some embodiments, the negative electrode film layer may further optionally comprises other auxiliary agents. As examples, other auxiliary agents may include thickeners, e.g., sodium carboxymethylcellulose (CMC), PTC thermistor material, etc. In some embodiments, the mass content of the other auxiliary agents is ≤2 wt. %, based on the total weight of the negative electrode film layer.
In some embodiments, the negative electrode collector may be a metal foil or a composite collector. As an example of a metal foil, a copper foil may be used. The composite current collector may include a base layer of polymeric material and a layer of metallic material formed on one or more surfaces of the base layer of polymeric material. As an example, the metal material may comprise one or more of copper, copper alloy, nickel, nickel alloy, titanium, titanium alloy, silver, and silver alloy. As an example, the base layer of polymeric material may comprise one or more of polypropylene (PP), polyethylene terephthalate (PET), polybutylene terephthalate (PBT), polystyrene (PS), polyethylene (PE), and the like.
The negative electrode film layer is usually formed by applying a negative electrode slurry on a negative electrode collector, drying and cold-pressing. The negative electrode slurry is typically formed by dispersing the negative active material, optional conductive agent, optional binder, other optional auxiliary agents in a solvent and stirring well. The solvent may be N-methylpyrrolidone (NMP) or deionized water, but is not limited thereto.
The negative electrode plate does not exclude additional functional layers other than the negative electrode film layer. For example, in some embodiments, the negative electrode plate described in the present application further comprises a conductive primer layer (such as composed of a conductive agent and a binder) sandwiched between the negative electrode current collector and the negative electrode film layer, and disposed on the surface of the negative electrode current collector. In some other embodiments, the negative electrode plate described in this application further comprises a protective layer covering the surface of the negative electrode film layer.
During the charging and discharging process of the battery, active ions are intercalated and deintercalated back and forth between the positive electrode plate and the negative electrode plate, and the electrolyte (or electrolytic solution) functions as conducting active ions between the positive electrode plate and the negative electrode plate. There is no specific limitation on the type of electrolyte in the present application, and it can be selected according to actual needs.
The electrolyte includes an electrolyte salt and a solvent. There is no specific limitation on the type of solvent and the electrolyte salt, and they can be selected according to actual needs.
When the secondary battery of the present application is a lithium ion battery, as an example, the electrolyte salt may comprise one or more of lithium hexafluorophosphate (LiPF6), lithium tetrafluoroborate (LiBF4), lithium perchlorate (LiClO4), lithium hexafluoroarsenate (LiAsF6), lithium difluorosulfimide (LiFSI), lithium bistrifluoromethanesulfonimide (LiTFSI), lithium trifluoromethanesulfonate (LiTFS), lithium difluoro (oxalate) borate (LiDFOB), bis(oxalate) borate (LiBOB), lithium difluorophosphate (LiPO2F2), lithium difluorobisoxalate phosphate (LiDFOP), and lithium tetrafluorooxalate phosphate (LiTFOP).
When the secondary battery of the present application is a sodium ion battery, as an example, the electrolyte salt may comprise, but is not limited to, one or more of sodium hexafluorophosphate (NaPF6), sodium tetrafluoroborate (NaBF4), sodium perchlorate (NaClO4), sodium hexafluoroarsenate (NaAsF6), sodium bisfluorosulfonimide (NaFSI), sodium bistrifluoromethanesulfonimide (NaTFSI), sodium trifluoromethanesulfonate (NaTFS), sodium difluoro (oxalate) borate (NaDFOB), sodium bis(oxalate) borate (NaBOB), sodium difluorophosphate (NaPO2F2), sodium difluorobisoxalate phosphate (NaDFOP) and sodium tetrafluorooxalate phosphate (NaTFOP).
As an example, the solvent may comprise, but is not limited to, one or more of ethylene carbonate (EC), propylene carbonate (PC), ethyl methyl carbonate (EMC), diethyl carbonate (DEC), dimethyl carbonate (DMC), dipropyl carbonate (DPC), methyl propyl carbonate (MPC), ethyl propyl carbonate (EPC), butylene carbonate (BC), fluoroethylene carbonate (FEC), methyl formate (MF), methyl acetate (MA), ethyl acetate (EA), propyl acetate (PA), methyl propionate (MP), ethyl propionate (EP), propyl propionate (PP), methyl butyrate (MB), ethyl butyrate (EB), 1,4-butyrolactone (GBL), sulfolane (SF), dimethylsulfone (MSM), methylethylsulfone (EMS), and diethylsulfone (ESE).
In some embodiments, the electrolytic solution may optionally comprise an additive. For example, the additives may comprise negative electrode film-forming additives, positive electrode film-forming additives, and additives that can improve certain performance of the battery, such as additives that improve overcharging performance of the battery, additives that improve high-temperature performance of the battery, and additives that improve low-temperature power/rating performance of the battery.
In some embodiments, the positive electrode plate, the separator, and the negative electrode plate may be fabricated into an electrode assembly by a winding process and/or a lamination process.
In some embodiments, the secondary battery may comprise an outer packaging. The outer packaging may be used to encapsulate the electrode assembly and the electrolyte.
In some embodiments, the outer packaging of the secondary battery may be a hard housing, such as a hard plastic housing, aluminum housing, steel housing, or the like. The outer packaging of the secondary battery may also be a soft pack, such as a pouch type soft pack. The material of the soft pack may be plastic, such as one or more of polypropylene (PP), polybutylene terephthalate (PBT), and polybutylene succinate (PBS).
The present application does not have particular limitation on the shape of the secondary battery, which may be cylindrical, square, or other arbitrary shapes.
In some embodiments, referring to
The preparation method of the secondary battery of the present application is well known. In some embodiments, a positive electrode plate, a separator, a negative electrode plate, and electrolytic solution can be assembled to form a secondary battery. As an example, the positive electrode plate, the separator, and the negative electrode plate can be formed into an electrode assembly by a winding process and/or a laminating process; the electrode assembly is placed in an outer packaging and dried, followed by injection with the electrolyte; after the processes including vacuum encapsulation, steady standing, chemical formation, and shaping, a secondary battery is obtained.
In some embodiments, the secondary battery of the present application can be assembled into a battery module, and the number of secondary batteries contained in the battery module can be multiple, and the specific number can be adjusted according to the application and capacity of the battery module.
Optionally, the battery module 4 may further include a housing having an accommodating space in which a plurality of secondary batteries 5 are accommodated.
In some embodiments, the above-mentioned battery module may also be assembled into a battery pack, and the number of battery modules contained in the battery pack can be adjusted according to the application and capacity of the battery pack.
The fourth aspect of embodiments of the present application provides an electrical device comprising one or more of the secondary battery, battery module, and battery pack of the present application. The secondary battery, battery module or battery pack can be used as a power source of the electrical device, and can also be used as an energy storage unit of the electrical device. The electrical device may be, but is not limited to, a mobile device (e.g., a mobile phone, a laptop computer, etc.), an electric vehicle (e.g., a pure electric vehicle, a hybrid electric vehicle, a plug-in hybrid electric vehicle, an electric bicycle, an electric scooter, an electric golf vehicle, an electric truck), an electric train, a ship, a satellite, an energy storage system, etc.
The electrical device may comprise the secondary battery, the battery module or the battery pack selected according to its usage requirements.
As another example, the electrical device may be a mobile phone, a tablet computer, a notebook computer, etc. The electric device is generally required to be light and thin, and a secondary battery can be used as a power source.
The following examples are intended to describe the present application more specifically, merely for the purpose of illustration. Various modifications and variations within the scope of the present application are apparent to those skilled in the related art. Unless otherwise stated, all parts, percentages, and ratios reported in the following examples are based on mass, and all reagents used in the examples are commercially available or synthesized by conventional methods, and can be directly obtained without further treatment, and the instruments used in the examples are commercially available.
After loosening the Gossypium linter and slag removal by a cotton opener, the obtained mixture was cooked at 150° C. with 5 wt. % NaOH aqueous solution for 2 hours, and then washed with water to remove impurities (3 times of water washing), bleached with sodium hypochlorite, washed with diluted hydrochloric acid to remove impurities, washed with water to remove impurities (1 time of water washing), water discharged and dried with air flow to obtain Gossypium cellulose powder with whiteness of ≥85%.
1 kg of the obtained Gossypium cellulose powder was mixed with 30 kg of 60 wt. % sulfuric acid aqueous solution, and the reaction was carried out at 55° C. to 60° C. for 1.5 h. After the reaction was completed, by washing with water (3 times of water washing), filtering, and removing acid and impurities, the cellulose nanowhiskers with sulfonic acid groups were obtained.
The pH of cellulose nanowhiskers with sulfonic acid groups was adjusted to neutral with 10 wt. % aqueous NaOH solution, and then dispersed with a grinder at high speed for 2.5 h. The grinding were carried out for 2 times, and then a high pressure homogenizer was used for nanoscale cutting, to obtain the nanocellulose C1 with sulfonic acid modifying groups having an average length of 450 nm and an average diameter of 25 nm, and the molar ratio of sulfonic acid groups to hydroxyl groups of 5:3.
Nanocellulose C2 to nanocellulose C13 were prepared in a similar manner to nanocellulose C1, with the differences detailed in Table 1. In the preparation, nanocelluloses with different average diameters and/or different average lengths can be obtained by adjusting the parameters of the grinder as well as the cutting parameters of the high-pressure homogenizer.
After loosening the Gossypium linter and slag removal by a cotton opener, the obtained mixture was cooked at 150° C. with 5 wt. % NaOH aqueous solution for 2 hours, and then washed with water to remove impurities (3 times of water washing), bleached with sodium hypochlorite, washed with diluted hydrochloric acid to remove impurities, washed with water to remove impurities (1 time of water washing), water discharged and dried with air flow to obtain Gossypium cellulose powder with whiteness of ≥85%. The obtained Gossypium cellulose powder was mixed with 20 wt. % aqueous NaOH solution at 10° C., stirred for 2 h, filtered, and washed with water twice to obtain cellulose powder.
50 g of the obtained cellulose powder and 200 g of urea were placed in a three-port reactor with an oil-water separator. After the urea was dissolved, 5 g of xylene was added, and the temperature was raised to 137° C. under stirring. The reaction was terminated after 4 hours, followed by water washing (3 times of water washing), filtering and drying, to obtain cellulose carbamate.
The obtained cellulose carbamate was dissolved in 5 wt. % aqueous NaOH solution to obtain a homogeneous cellulose carbamate solution; and the cellulose carbamate solution was then dispersed with a grinder at high speed for 2.5 h. The grinding were carried out for 2 times, and then a high pressure homogenizer was used for nanoscale cutting, to obtain the nanocellulose C14 with amine modifying groups having an average length of 450 nm and an average diameter of 25 nm, and the molar ratio of amine groups to hydroxyl groups of 4:3.
Unmodified nanocellulose having an average length of 450 nm and an average diameter of 25 nm with a product model of CNWS-50 purchased from Zhongke Leiming (Beijing) Technology Co., Ltd. was used, and can be further processed using a grinder and/or a high-pressure homogenizer to obtain nanocellulose with different average diameters and/or different average lengths.
The molar ratio of the modifying groups to hydroxyl groups in nanocelluloses C1 to C14 can be measured by the following method: according to the phthalic anhydride method in GB/T 12008.3-2009, the hydroxyl values of raw material cellulose and nanocelluloses C1 to C14 (milligrams of potassium hydroxide equivalent to the hydroxyl content per gram of sample) were respectively tested, and the obtained numerical unit was mg KOH/g, which was converted into mmol/g as the hydroxyl content. The content of the modifying group (i.e. the content of the modified hydroxyl group) can be obtained by subtracting the hydroxyl content of the nanocellulose C1 to C14 from the hydroxyl content of raw material cellulose, and thus the molar ratio of the modifying group to the hydroxyl group can be calculated.
Providing a PE porous substrate: having thickness of 4.5 μm and porosity of 42%.
Formulating a coating slurry: mixing evenly the above prepared nanocellulose C1, alumina secondary particles as filler, and an aqueous solution type polyacrylic acid as a binder at a mass ratio of 15:84.1:0.9 in an appropriate amount of deionized water as solvent to obtain a coating slurry with a solid content of 35 wt. %.
Alumina secondary particles as filler were prepared as follows: the precursor solution of alumina (such as aluminum chloride solution) was subjected to oxidation by way of high-pressure sputtering, and then heated at 830° C. for 1.2 hours to form specific small particles, and then dried at 150° C. for 45 minutes to obtain alumina secondary particles with specific morphology. The obtained alumina secondary particles had an average particle size of 150 nm, and the primary particles that constitute the secondary particles had an average particle size of 15 nm, and based on the total weight of alumina secondary particles, the contents of α, θ, γ, and η forms in the alumina secondary particles were 1.5 wt. %, 74.7 wt. %, 23.3 wt. %, and 0.5 wt. %, respectively. The transmission electron microscope (TEM) diagram of the alumina secondary particles as filler was shown in
Coating: Both surfaces of the PE porous substrate were coated with the formulated coating slurry using a coating machine, and a separator was obtained by drying and slitting steps. The coating layer on one side of PE porous substrate had a thickness of 0.8 μm.
The positive electrode active material LiNi0.8CO0.1Mn0.1O2(NCM811), carbon black (Super P) as conductive agent, and polyvinylidene fluoride (PVDF) as binder were uniformly mixed at a mass ratio of 96.2:2.7:1.1 in an appropriate amount of solvent N-methylpyrrolidone (NMP) to obtain a positive electrode slurry; the positive electrode slurry was applied on an aluminum foil as positive electrode collector, and then dried and cold-pressed, slitted, and cut, to give the positive electrode plate. The positive electrode plate had an areal density of 0.207 mg/mm2 and a compacted density of 3.5 g/cm3.
Artificial graphite as negative electrode active material, carbon black (Super P) as conductive agent, styrene butadiene rubber (SBR) as binder, and carboxymethyl cellulose sodium (CMC) were mixed at a mass ratio of 96.4:0.7:1.8:1.1 in a suitable solvent deionized water to obtain a negative electrode slurry; the negative electrode slurry was applied onto a copper foil as negative electrode current collector; and after processes including drying, cold-pressing, slitting and cutting, the negative electrode plate was obtained. The negative electrode plate had an areal density of 0.126 mg/mm2 and a compacted density of 1.7 g/cm3.
Ethylene carbonate (EC) and ethyl methyl carbonate (EMC) at a volume ratio of 30:70 were mixed to obtain an organic solvent, and then a fully dried LiPF6 was dissolved in the above organic solvent, to prepare an electrolyte with a concentration of 1 mol/L.
The positive electrode plate, the separator, and the negative electrode plate were stacked and wound in sequence to obtain an electrode assembly; the electrode assembly was placed in a outer packaging and dried, followed by injection with the electrolyte; after the processes including vacuum encapsulation, standing, chemical formation, and shaping, a secondary battery was obtained.
The secondary batteries were prepared by a method similar to that of Example 1, except that the amounts of nanocellulose and filler added in the preparation of the separators were different, and the specific parameters were detailed in Table 2.
The secondary batteries were prepared by a method similar to that of Example 1, except that the fillers used in the preparation of the separator were different.
The filler of Example 6 was prepared as follows: the precursor solution of alumina (such as aluminum chloride solution) was subjected to oxidation by way of high-pressure sputtering, and then heated at 750° C. for 1.0 hours to form specific small particles, and then dried at 250° C. for 60 minutes to obtain alumina secondary particles with specific morphology. The obtained alumina secondary particles had an average particle size of 100 nm, and the primary particles that constitute the secondary particles had an average particle size of 15 nm, and based on the total weight of alumina secondary particles, the contents of α, θ, γ, and η forms in the alumina secondary particles were 1.2 wt. %, 63.5 wt. %, 34.5 wt. %, and 0.8 wt. %, respectively.
The filler of Example 7 was prepared as follows: the precursor solution of alumina (such as aluminum chloride solution) was subjected to oxidation by way of high-pressure sputtering, and then heated at 840° C. for 1.5 hours to form specific small particles, and then dried at 200° C. for 60 minutes to obtain alumina secondary particles with specific morphology. The obtained alumina secondary particles had an average particle size of 200 nm, and the primary particles that constitute the secondary particles had an average particle size of 15 nm, and based on the total weight of alumina secondary particles, the contents of α, θ, γ, and η forms in the alumina secondary particles were 1.8 wt. %, 76.7 wt. %, 21.0 wt. %, and 0.5 wt. %, respectively.
The filler of Example 8 was prepared as follows: the precursor solution of alumina (such as aluminum chloride solution) was subjected to oxidation by way of high-pressure sputtering, and then heated at 900° C. for 2 hours to form specific small particles, and then dried at 150° C. for 45 minutes to obtain alumina secondary particles with specific morphology. The obtained alumina secondary particles had an average particle size of 300 nm, and the primary particles that constitute the secondary particles had an average particle size of 15 nm, and based on the total weight of alumina secondary particles, the contents of α, θ, γ, and η forms in the alumina secondary particles were 2.5 wt. %, 79.9 wt. %, 17.1 wt. %, and 0.5 wt. %, respectively.
The secondary batteries were prepared by a method similar to that of Example 1, except that the types of nanocellulose used during the formulation of the coating slurry in the preparation of the separators were different, and the specific parameters were detailed in Tables 1 and 2.
The secondary battery was prepared by a method similar to that of Example 1, except that in the preparation of the separator, inorganic particles with primary particle morphology were further added during the formulation of the coating slurry.
Formulating a coating slurry: mixing evenly the above prepared nanocellulose C1, alumina secondary particles as filler (prepared by the same process as in Example 1), alumina with primary particle morphology (having the average particle size of 350 nm, a crystal form including mainly α crystal form, and a mass ratio of 99.9% or higher) and an aqueous solution type polyacrylic acid as a binder at a mass ratio of 15:78.1:6:0.9 in an appropriate amount of deionized water as solvent to obtain a coating slurry with a solid content of 35 wt. %.
The secondary battery was prepared by a method similar to that of Example 1, except that in the preparation of the separator, the unmodified nanocellulose C15 was used and the used alumina had primary particle morphology, and the specific parameters were detailed in Table 2.
Formulating a coating slurry: mixing evenly the above prepared nanocellulose C15, alumina with primary particle morphology (having an average size of 650 nm, α crystal form including mainly α crystal form, and a mass ratio of 99.9% or higher) and an aqueous solution type polyacrylic acid as a binder at a mass ratio of 15:80:5 in an appropriate amount of deionized water as solvent to obtain a coating slurry with a solid content of 35 wt. %.
The secondary battery was prepared by a method similar to that of Example 1, except that in the preparation of the separator, the used alumina had primary particle morphology, and the specific parameters were detailed in Table 2.
Formulating a coating slurry: mixing evenly the above prepared nanocellulose C1, alumina with primary particle morphology (having an average size of 650 nm, a crystal form including mainly α crystal form, and a mass ratio of 99.9% or higher) and an aqueous solution type polyacrylic acid as a binder at a mass ratio of 15:80:5 in an appropriate amount of deionized water as solvent to obtain a coating slurry with a solid content of 35 wt. %.
The secondary battery was prepared by a method similar to that of Example 1, except that in the preparation of the separator, no nanocellulose was added and the alumina had primary particle morphology, and the specific parameters were detailed in Table 2.
Formulating a coating slurry: mixing evenly the alumina with primary particle morphology (having an average size of 650 nm, a crystal form including mainly α crystal form, and a mass ratio of 99.9% or higher) and an aqueous solution type polyacrylic acid as a binder at a mass ratio of 94:6 in an appropriate amount of deionized water as solvent to obtain a coating slurry with a solid content of 35 wt. %.
Sample preparation: The separator prepared above was punched into samples with a width of 50 mm and a length of 100 mm using a punching machine; and five parallel samples were placed on A4 paper and fixed; and then the A4 paper loaded with the samples was placed on corrugated paper with a thickness of from 1 mm to 5 mm.
Sample test: the A4 paper placed on the corrugated paper was placed into a blast oven which was set to the temperature of 150° C.; After the temperature reached the set temperature and stabilized for 30 minutes, timing was started until the set time (1 h in this application) was reached; the length and width of the separator were measured, and the values were marked as a and b, respectively.
Calculation of thermal shrinkage rate: machine direction (MD) heat shrinkage rate=[(100−a)/100]×100%, transverse direction (TD) thermal shrinkage rate=[(50−b)/50]×100%, and the average value of five parallel samples was taken as the test result.
Time required for 100 mL of air to pass through the separator at room temperature was tested and for the accuracy, the average value of 5 parallel samples was taken as the test result. The test instrument may be the Kumagai KRK Wangyan air permeability tester.
The secondary battery was charged with a constant current of 1 C to 4.2 V at 25° C., and continued to charge with the constant voltage until the current was ≤0.05 C, and allowed to stand for 5 minutes; then secondary battery with a fixture was tested in a DHG-9070A DHG series high-temperature oven, and raised from room temperature to 80±2° C. at a rate of 5° C./min, and held for 30 minutes; then, the temperature was raised at a heating rate of 5° C./min. Every time the temperature was raised by 5° C., the temperature was kept for 30 minutes. During the temperature rise process, the surface temperature change of the secondary battery was monitored. When the temperature starts to rise sharply, the corresponding oven temperature was recorded as the hot box failure temperature of the secondary battery. The higher hot box failure temperature of a secondary battery means the better thermal safety performance of the secondary battery. For the accuracy, the average value of 5 parallel samples was taken as the test result.
As can be seen from Table 3 and Examples 1 to 23, by disposing a coating layer comprising nanocellulose (that constitutes a three-dimensional skeleton structure) and a filler with secondary particle morphology on both surfaces of the porous substrate of the separator, the obtained separators can have the combined characteristics of low thermal shrinkage and high air permeability, and the obtained secondary batteries can have high thermal safety performance.
The filler with secondary particle morphology used in the coating layer of the separator of the present application can be overlapped with nanocellulose to form an integrated effect, which enables the separator to maintain excellent heat resistance and high bonding strength on the premise of reducing the amount of binder and reducing the thickness of the coating layer. In addition, the separator of the present application has high air permeability, and it is not easy to have hole plugging problems. Therefore, the secondary battery employing the separator of the present application can further have the combined characteristics of high energy density and long cycle life and good rate performance on the premise of high thermal safety performance.
Alumina used in the coating layers of Comparative Example 1 and Comparative Example 2 had the primary particle morphology, in which alumina and nanocellulose cannot form an integrated overlap effect, thereby resulting in very limited improvement effects on the heat resistance of the separator and the thermal safety performance of the secondary battery. Furthermore, since alumina and nanocellulose cannot form an integrated overlap effect, a higher amount of binder is further required in the preparation of the coating slurry. However, the higher amount of binder causes that the problem of pore plugging is very likely to occur, which is also detrimental to the rate performance of the secondary battery.
In Comparative Example 3 using an inorganic ceramic layer as a coating layer, since the inorganic ceramic particles are particles having a primary particle morphology with a larger particle size, the number of layers of the inorganic ceramic particles accumulated on the porous substrate during coating process is relatively small, which further leads to very limited improvement effect of the inorganic ceramic particles on the heat resistance of the separator and the thermal safety performance of the secondary battery.
From the combination of Example 1 to Example 21 with Example 22, the test results also show that when the nanocellulose has a specific type and/or specific content of the modifying group according to the present application, it helps to further improve the heat resistance of the separator and the thermal safety performance of the secondary battery.
It should be noted that the present application is not limited to the above-mentioned embodiments. The above-mentioned embodiments are merely examples, and within the scope of the technical solutions of the present application, embodiments that have substantially the same configuration as the technical idea and exert the same effects are included in the technical scope of the present application. In addition, without departing from the scope of the present application, various modifications conceivable by those skilled in the art can be introduced to the embodiments, and other forms constructed by combining some components in the embodiments are also included in the scope of the present application.
| Number | Date | Country | Kind |
|---|---|---|---|
| PCT/CN2022/101261 | Jun 2022 | WO | international |
This application is a Continuation n of International Application No. PCT/CN2022/112580 filed on Aug. 15, 2022, which claims priority to PCT Patent application PCT/CN2022/101261 filed on Jun. 24, 2022, both of which are incorporated herein by reference in their entireties.
| Number | Date | Country | |
|---|---|---|---|
| Parent | PCT/CN2022/112580 | Aug 2022 | WO |
| Child | 18991752 | US |
