SECONDARY BATTERY

DE602019063878T2Active Publication Date: 2024-12-25CONTEMPORARY AMPEREX TECHNOLOGY (HONG KONG) LIMITED
View PDF 0 Cites 0 Cited by

Patent Information

Application Number
DE602019063878
Authority / Receiving Office
DE · DE
Patent Type
Patents
Current Assignee / Owner
Priority Date
2018-10-17
Filing Date
2019-06-07
Publication Date
2024-12-25
Estimated Expiration
2039-06-07

AI Technical Summary

Technical Problem

Rechargeable batteries face challenges in achieving high energy density and fast charging capability without compromising safety and cycle life, as the design of the negative electrode plate affects both energy density and charging speed, leading to heat issues during fast charging.

Method used

A secondary battery design featuring a negative electrode plate with a specific negative active material, such as graphite, tested under controlled conditions to optimize capacity ratios and coating weights, combined with a positive electrode plate using materials like lithium nickel cobalt manganese oxide, to balance energy density and charging speed.

Benefits of technology

The optimized battery achieves long cycle life, high energy density, and fast charging capability simultaneously, improving dynamics performance and reducing polarization, thus enhancing safety and efficiency.

✦ Generated by Eureka AI based on patent content.
Patent Text Reader
Need to check novelty before this filing date? Find Prior Art

Description

RELATED APPLICATIONS

[0001] The present application claims priority to Chinese patent application No. CN201811209254.9, filed on October 17, 2018.FIELD OF THE PRESENT INVENTION

[0002] The present invention relates to the field of battery, and particularly relates to a secondary battery as specified in any of claims 1-12.BACKGROUND OF THE PRESENT INVENTION

[0003] Rechargeable batteries are widely used in the field such as mobile phones, computers, household electric appliances, electric power tools and the like due to significant characteristics of light weight, high energy density, no pollution, none memory effect, long service life and the like. The charging time has got more and more attention from end consumers and is also one of the key factors limiting the popularizion of the rechargeable batteries.

[0004] From the viewpoint of technical principle, a core affecting the charging speed of the battery lies in the negative electrode plate. In order to obtain a battery having high energy density, the weight of the active material coated on the unit area of the current collector generally increases when the negative electrode plate is designed, however, the charging capability of the battery often does not meet the requirements; when the charging capability of the battery is satisfied by reducing the weight of the active material coated on the unit area of the current collector, the energy density of the battery does not meet the requirements. Moreover, there is a serious heat problem during the fast charging process of the battery, which also affects the service safety of the end consumers. WO 2017 / 104145 A1 relates to a lithium ion secondary battery provided with a positive electrode, a negative electrode and a separator. US 2010 / 233543 Al describes a non-aqueous secondary battery comprising a positive electrode which has a positive electrode active material layer.

[0005] Therefore, how to obtain a battery having high safety performance and fast charging capability without compromising the energy density is the key in the design and the engineering of the negative electrode plate.SUMMARY OF THE PRESENT INVENTION

[0006] In view of the problem existing in the background, an object of the present invention is to provide a secondary battery as specified in the independent claim 1, which has the characteristics of long cycle life, high energy density and fast charging capability at the same time. Preferred embodiments are defined in dependent claims 2-12.

[0007] The present invention provides a secondary battery, which comprises a positive electrode plate, a negative electrode plate, an electrolyte and a separator, the negative electrode plate comprises a negative current collector and a negative film, the negative film is provided on at least one surface of the negative current collector and comprises a negative active material. The negative active material comprises graphite, and the negative active material is obtained by the process of being tested in a button half battery: the button half battery is discharged to 5 mV at a constant current of 0.05 C, and the obtained capacity is recorded as X; then the button half battery is discharged to 5 mV at a constant current of 50 µA, and the obtained capacity is recorded as A; then the button half battery is discharged to 5 mV at a constant current of 10 µA, and the obtained capacity is recorded as B; and 0.02≤(A+B) / X≤0.50; the negative electrode plate satisfies a relationship: 0.05≤(A / X)×CW≤2.00, CW represents a coating weight of the negative electrode plate per unit area with a unit of mg / cm 2< ; wherein the positive electrode plate comprises a positive current collector and a positive film, the positive film is provided on at least one surface of the positive current collector and comprises a positive active material, the positive active material is one or more selected from a group consisting of lithium nickel cobalt manganese oxide, lithium nickel cobalt aluminum oxide and olivine-type lithium-containing phosphate.

[0008] Preferably, when the negative active material is tested in a button half battery, the negative active material satisfies a relationship: 0.02≤(A+B) / X≤0.27. More preferably, when the negative active material is tested in a button half battery, the negative active material satisfies a relationship: 0.02 ≤ A + B / X ≤ 0.05 .

[0009] The negative electrode plate satisfies a relationship: 0.08≤(A / X)×CW≤0.32. 0.01≤A / X≤0.25. Preferably, 0.01≤A / X≤0.04.

[0010] The coating weight of the negative electrode plate per unit area represented by CW is 4 mg / cm 2< ~15 mg / cm 2< . Preferably, the coating weight of the negative electrode plate per unit area represented by CW is 8.0 mg / cm 2< ~15 mg / cm 2< .

[0011] A particle size of the negative active material represented by D50 is 4 µm~18 µm. Preferably, the particle size of the negative active material represented by D50 is 4 µm~16 µm.

[0012] An active specific surface area of the negative electrode plate is 2 cm 2< / g~12 cm 2< / g.

[0013] The graphite is one or more selected from a group consisting of artificial graphite and natural graphite.

[0014] The negative active material further comprises one or more selected from a group consisting of soft carbon, hard carbon and silicon-based material. Preferably, the negative active material further comprises silicon-based material, the silicon-based material is one or more selected from a group consisting of elemental silicon, silicon oxide, silicon carbon composite and silicon alloy.

[0015] Compared with the existing technologies, the present invention at least includes the following beneficial effects: in the present invention, by selecting a negative active material having good dynamics performance, a secondary battery having long cycle life, high energy density and fast charging capability at the same time is obtained.DETAILED DESCRIPTION

[0016] Hereinafter a negative electrode plate and a secondary battery according to the present invention are described in detail.

[0017] Firstly, a negative electrode plate according to a first aspect of the present invention is described. The negative electrode plate comprises a negative current collector and a negative film, the negative film is provided on at least one surface of the negative current collector and comprises a negative active material.

[0018] The negative active material satisfies the following characteristics when the negative active material is tested in a button half battery: the button half battery is discharged to 5 mV at a constant current of 0.05 C (which corresponds to the intercalating process with respect to the active ions into the negative active material), and the obtained capacity is recorded as X; then the button half battery is discharged to 5 mV at a constant current of 50 µA, and the obtained capacity is recorded as A; then the button half battery is discharged to 5 mV at a constant current of 10 µA, and the obtained capacity is recorded as B; and 0.02≤(A+B) / X≤0.50.

[0019] It should be noted that, the preparation of the button half battery may refer to national standards or industry standards. For example, the selected negative active material, a binder commonly used in the industry and a conductive agent commonly used in the industry are used to prepare an electrode plate, and a round metal sheet (such as a lithium sheet, a sodium sheet and the like) is used as a counter electrode, so a button half battery is prepared.

[0020] Specifically, the button half battery may be prepared as follows: the selected negative active material, super P and polyvinylidene fluoride (PVDF) according to a certain mass ratio (for example 92:3:5) are uniformly mixed with N-methylpyrrolidone (NMP, solvent) to obtain a slurry; then the slurry is coated on an aluminum foil, drying is then performed to remove the solvent, which is then followed by plate cutting and pressing, then a round electrode plate is obtained; then the round electrode plate and a round lithium sheet used as the counter electrode are assembled into a button half battery in a glove box, here the electrolyte salt used in the button half battery may be LiPF 6 , the concentration of the electrolyte salt may be 1 mol / L, the organic solvent used in the button half battery may be a mixture of ethylene carbonate and ethyl methyl carbonate according to a volume ratio of 1:1; then the button half battery is discharged to 5 mV at a constant current of 0.05 C, and the obtained capacity is recorded as X; then the button half battery is discharged to 5 mV at a constant current of 50 µA, and the obtained capacity is recorded as A; then the button half battery is discharged to 5 mV at a constant current of 10 µA, and the obtained capacity is recorded as B.

[0021] The negative electrode plate needs to undergo the following three electrochemical processes during the charging process of the battery: (1) the active ions (such as lithium ions, sodium-ions and the like) deintercalate from the positive active material and enter into the electrolyte, and then enter into the channels of the porous negative electrode plate along with the electrolyte, so that a liquid phase conduction process of the active ions in the channels of the porous negative electrode plate is completed; (2) the active ions exchange charges with the electrons on the surface of the negative active material; (3) the active ions enter into the bulk structure of the negative active material from the surface of the negative active material through a solid phase conduction process.

[0022] The solid phase conduction process with respect to the active ions in the negative active material has a very impormant effect on improving the fast charging capability of the battery. The better the dynamics performance of the negative active material is, the smaller the solid phase conduction resistance with respect to the active ions in the negative active material is, the higher the weight of the negative active material coated on the unit area of the negative current collector can be maintained, therefore the battery can have long cycle life, high energy density and fast charging capability at the same time.

[0023] The inventors has done a large number of researches and found that, when the negative active material is tested in the button half battery and the obtained capacities of the button half battery satisfy a relationship 0.02≤(A+B) / X≤0.50, the battery can have fast charging capability and long cycle life at the same time without compromising the high energy density.

[0024] The reaction with respect to the active ions to intercalate into the negative active material usually is incomplete during the discharging process of the button half battery, a part of the active ions cannot intercalate into the negative active material, when under the same condition, the more the amount of active ions failing to intercalate into the negative active material is, the larger the polarization of the negative active material is, however, the larger the polarization of the negative active material is, the more difficult it is to improve the fast charging capability of the battery.

[0025] The inventors found that, the polarization of the negative active material can be characterized by (A+B) / X, the smaller the value of (A+B) / X is, the smaller the polarization of the negative active material is, the better the dynamics performance of the negative active material is, the higher the weight of the negative active material coated on the unit area of the negative current collector can be maintained, and the higher the energy density of the battery is. If the value of (A+B) / X is too small, for example the value of (A+B) / X is less than 0.02, although the polarization of the negative active material is very small, which may better improve the fast charging capability of the battery, the active ions are prone to transfer onto the surface of this kind of negative active material during the standby process of the battery, the problems that the self-discharge increases and the side reactions between this kind of negative active material and the electrolyte increase easily occur, therefore the requirement on long cycle life of the battery cannot be satisfied. And moreover, the value of (A+B) / X cannot be too large, the inventors found that, when the value of (A+B) / X is more than 0.50, the polarization of this kind of negative active material is too large, the negative active material can only accept the active ions under a smaller current, therefore it is very difficult to improve the fast charging capability of the battery; and the negative film needes to be both thin and light in order to make the battery have a fast charging capability, which will compromise the high energy density of the battery.

[0026] In some embodiments of the present invention, a lower limit value of (A+B) / X may be 0.02, 0.03, 0.04, 0.05 and 0.06; an upper limit value of (A+B) / X may be 0.06, 0.08, 0.10, 0.12, 0.14, 0.16, 0.18, 0.20, 0.22, 0.24, 0.26, 0.28, 0.30, 0.35, 0.40, 0.45 and 0.50.

[0027] Preferably, when the negative active material is tested in a button half battery, the negative active material satisfies a relationship: 0.03≤(A+B) / X≤0.35.

[0028] The liquid phase conduction process with respect to the active ions in the channels of the porous negative electrode plate also has a very important effect on improving the fast charging capability of the battery, and the liquid phase conduction capability with respect to the active ions in the channels of the porous negative electrode plate is related with the coating weight of the negative electrode plate. Generally, the larger the coating weight of the negative electrode plate per unit area is, the more difficult the liquid phase conduction process with respect to the active ions in the channels of the porous negative electrode plate is. A / X is also an index for characterizing the polarization of the negative active material, the larger the value of A / X is, the larger the polarization of the negative active material is, the more difficult the active ions enter into the bulk structure of the negative active material, and the worse the dynamics performance of the negative active material is.

[0029] The inventors has done a large number of researches and found that, when the polarization of the negative active material characterizd by A / X and the coating weight of the negative electrode plate per unit area represented by CW satisfy a relationship 0.05≤(A / X)×CW≤4.50, the solid phase conduction speed with respect to the active ions in the bulk structure of the negative active material and the liquid phase conduction speed with respect to the active ions in the channels of the porous negative electrode plate both are optimal, therefore the battery can have higher fast charging capability without compromising the energy density. CW represents a coating weight of the negative electrode plate per unit area with a unit of mg / cm 2< .

[0030] If the value of (A / X)×CW is more than 4.50, the dynamics performance of the negative active material may be worse or the coating weight of the negative electrode plate per unit area may be higher. When the dynamics performance of the negative active material is worse, the charge exchange process with respect to the active ions on the surface of the negative active material and the solid phase conduction process with respect to the active ions in the bulk structure of the negative active material both become difficult, the fast charging capability of the battery is worse; when the coating weight of the negative electrode plate per unit area is higher, the energy density of the battery is higher, however, the liquid phase conduction process with respect to the active ions in the channels of the porous negative electrode plate becomes difficult, therefore the improvement on the fast charging capability of the battery is smaller.

[0031] If the value of (A / X)×CW is less than 0.05, the dynamics performance of the negative active material may be better or the coating weight of the negative electrode plate per unit area may be smaller. When the dynamics performance of the negative active material is better, the polarization of the negative active material is smaller, which improves the fast charging capability of the battery, however, the surface of this kind of negative active material is not stable, the active ions are prone to transfer onto the surface of this kind of negative active material, the problems that the self-discharge increases and the side reactions between this kind of negative active material and the electrolyte increase easily occur, thereby affecting the cycle life of the battery; when the coating weight of the negative electrode plate per unit area is smaller, the contact area between the unstable surface of the negative active material and the electrolyte increases, which further affects the improvement on the cycle life of the battery, and it is also difficult to make the battery have better fast charging capability and higher energy density at the same time.

[0032] In some embodiments of the present invention, a lower limit value of (A / X)×CW may be 0.05, 0.06, 0.07, 0.08, 0.09, 0.10, 0.12, 0.14 and 0.16; an upper limit value of (A / X)×CW may be 0.10, 0.20, 0.40, 0.60, 0.80, 1.00, 1.20, 1.50, 1.80, 2.00, 2.20, 2.50, 2.80, 3.00, 3.20, 3.50, 3.80, 4.00, 4.20 and 4.50.

[0033] Preferably, 0.07≤(A / X)×CW≤3.50.

[0034] Preferably, the negative active material satisfies a relationship 0.01≤A / X≤0.45. A lower limit value of A / X may be 0.01, 0.02, 0.03, 0.04, 0.05, 0.06, 0.07 and 0.08; an upper limit value of A / X may be 0.06, 0.08, 0.10, 0.12, 0.14, 0.16, 0.18, 0.20, 0.22, 0.24, 0.26, 0.28, 0.30, 0.32, 0.35, 0.38, 0.40, 0.42 and 0.45. More preferably, the negative active material satisfies a relationship 0.02≤A / X≤0.30. When the dynamics parameter of the negative active material falls within the above preferred ranges thereof, the negative electrode plate has higher homogeneity, which can preventing the negative active material having good dynamics performance from generating more side reactions with the electrolyte and in turn excessively affect the cycle life of the battery due to the high surface instability of the negative active material, and also preventing the negative active material having worse dynamics performance and larger polarization from excessively affect the improvement on the fast charging capability of the battery by hindering the charge exchange process with respect to the active ions on the surface of the negative active material and the solid phase conduction process with respect to the active ions in the bulk structure of the negative active material.

[0035] Preferably, the coating weight of the negative electrode plate per unit area represented by CW is 3 mg / cm 2< ~20 mg / cm 2< . More preferably, the coating weight of the negative electrode plate per unit area represented by CW is 4 mg / cm 2< ~15 mg / cm 2< . When the coating weight of the negative electrode plate per unit area falls within the above preferred ranges thereof, the negative electrode plate can have high volume energy density while maintaining good dynamics performance, in turn the battery can have high energy density while maintaining better fast charging capability.

[0036] In the negative electrode plate of the present invention, preferably, a particle size of the negative active material represented by D50 is 4 µm~18 µm. More preferably, the particle size of the negative active material represented by D50 is 4 µm~16 µm. When the particle size of the negative active material represented by D50 falls within the above preferred ranges thereof, the negative electrode plate has higher homogeneity, which can avoid the negative active material with too small particle size from affecting the performances of the battery by generating more side reactions with the electrolyte, and also avoid the negative active material with too large particle size from affecting the performances of the battery by hindering the solid phase conduction process with respect to the active ions in the bulk structure of the negative active material.

[0037] In the negative electrode plate of the present invention, preferably, an active specific surface area of the negative electrode plate is 2 cm 2< / g~12 cm 2< / g. More preferably, the active specific surface area of the negative electrode plate is 3 cm 2< / g~10 cm 2< / g. When the active specific surface area of the negative electrode plate is larger, the electrochemical activity of the negative electrode plate is higher, the side reactions between the negative electrode plate and the electrolyte increases, the thickness of the SEI membrane on the surface of the negative electrode plate increases, the resistance with respect to the active ions to pass through the SEI membrane on the surface of the negative electrode plate and enter into the negative electrode plate increases, the dynamics performance of the negative electrode plate decreases, which affects the improvement on the fast charging capability of the battery. When the active specific surface area of the negative electrode plate is smaller, the amount of the active sites in the negative electrode plate is less, which also affects the improvement on the fast charging capability of the battery. Therefore when the active specific surface area of the negative electrode plate falls within the above preferred ranges thereof, the negative electrode plate can have better dynamics performance, and in turn the battery can have higher fast charging capability.

[0038] The test process of the active specific surface area of the negative electrode plate is described as follows.

[0039] The negative electrode plate of the present invention with a weight of m is used as a cathode, a lithium metal sheet is used as an anode, ferrocene with a concentration of 50 mmol / L is added into an electrolyte, then the cathode, the anode and the electrolyte are assembled into a button half battery. Four half button batteries used as parallel samples are scanned respectively at scanning rates v of 0.1 mV / s, 0.3 mV / s, 0.5 mV / s and 1 mV / s to obtain a series of cyclic voltammetry curves under the different scanning rates, then a peak current i p of each cyclic voltammetry curve is extracted using a EC-Lab software. A linear graph of i p and v is obtained where the square root of the scanning rate v ( v ) is used as X-coordinate and the peak current i p is used as Y-coordinate, and then the slope K of the linear graph is obtained.

[0040] In a Randles-Sevick equation, i p = 2.69 × 10 5 n 3 2 Ac D v , therefore the slope is obtained according to an equation K = 2.69 × 10 5 n 3 2 Ac D . n representes an electron transfer number of the electrode reaction and the value thereof is related with the specific type of the probe, and here the value thereof is 1; c representes a concentration of ferrocene, here the value thereof is 50 mmol / L; D representes a diffusion coefficient of the probe ferrocene, here the value thereof is 2.1×10 -6< cm 2< / s; A representes an active surface area of the negative electrode plate, and is obtained according to an equation A = K / 2.69 × 10 5 n 3 2 c D . The active specific surface area of the negative electrode plate is a ratio of the active surface area of the negative electrode plate represented by A to the weight of the negative electrode plate represented by m.

[0041] In the negative electrode plate of the present invention, the type of the negative active material is not specifically limited and may be selected based on actual demands. Preferably, the negative active material may be one or more selected from a group consisting of carbon-based material, silicon-based material, tin-based material and lithium titanate. The carbon-based material may be one or more selected from a group consisting of graphite, soft carbon, hard carbon, carbon fiber and mesocarbon microbeads; the graphite may be one or more selected from a group consisting of artificial graphite and natural graphite. The silicon-based material may be one or more selected from a group consisting of elemental silicon, silicon oxide, silicon carbon composite and silicon alloy. The tin-based material is one or more selected from a group consisting of elemental tin, tin oxide compound and tin alloy. More preferably, the negative active material may be one or more selected from a group consisting of carbon-based material and silicon-based material.

[0042] In the negative electrode plate of the present invention, the negative film may be provided on one of the surfaces of the negative current collector or the negative film may be provided on both surfaces of the negative current collector. The negative film may further comprise a conductive agent and a binder, the types and the contents of the conductive agent and the binder are not specifically limited and may be selected based on actual demands. The type of the negative current collector is not specifically limited and may be selected based on actual demands.

[0043] It should be noted that, when the negative film is provided on both surfaces of the negative current collector, as long as the negative film provided on any one of the surfaces of the negative current collector satisfies the present invention, it is considered that the negative electrode plate falls within the protection scope of the present invention.

[0044] Next a secondary battery according to a second aspect of the present invention is described, the secondary battery comprises the negative electrode plate according to the first aspect of the present invention.

[0045] Moreover, the secondary battery of the present invention further comprises a positive electrode plate, an electrolyte and a separator.

[0046] In the secondary battery of the present invention, the positive electrode plate may comprise a positive current collector and a positive film, the positive film is provided on at least one surface of the positive current collector and comprises a positive active material, the type and the specific composition of the positive electrode plate are not specifically limited and may be selected based on actual demands. The positive film may be provided on one of the surfaces of the positive current collector or the positive film may be provided on both surfaces of the positive current collector. The positive film may further comprise a conductive agent and a binder, the types and the contents of the conductive agent and the binder are not specifically limited and may be selected based on actual demands. The type of the positive current collector is not specifically limited and may be selected based on actual demands.

[0047] It should be noted that, the secondary battery according to the second aspect of the present invention may be a lithium-ion battery, a sodium-ion battery and any other battery using the negative electrode plate according to the first aspect of the present invention.

[0048] When the secondary battery is the lithium-ion battery, the positive active material may be selected from lithium cobalt oxide, lithium nickel oxide, lithium manganese oxide, lithium nickel manganese oxide, lithium nickel cobalt manganese oxide, lithium nickel cobalt aluminum oxide and olivine-type lithium-containing phosphate, but the present invention is not limited thereto, other conventionally known materials that can be used as the positive active material of the lithium-ion battery can also be used. These positive active materials may be used alone or may be used as two or more of them in combination. Preferably, the positive active material may be one or more selected from a group consisting of LiCoO 2 , LiNiO 2 , LiMnO 2 , LiMn 2 O 4 , LiNi 1 / 3 Co 1 / 3 Mn 1 / 3 O 2 (NCM333), LiNi 0.5 Co 0.2 Mn 0.3 O 2 (NCM523), LiNi 0.6 Co 0.2 Mn 0.2 O 2 (NCM622), LiNi 0.8 Co 0.1 Mn 0.1 O 2 (NCM811), LiNi 0.85 Co 0.15 Al 0.05 O 2 , LiFePO 4 (LFP) and LiMnPO 4 .

[0049] When the secondary battery is the sodium-ion battery, the positive active material may be selected from transition metal oxide Na x MO 2 (M represents transition metal, preferably, M is one or more selected from a group consisting of Mn, Fe, Ni, Co, V, Cu and Cr, 0<x≤1), polyanion-type material (phosphate-type, fluorophosphate-type, pyrophosphate-type, sulfate-type) and prussian blue material, but the present invention is not limited thereto, other conventionally known materials that can be used as the positive active material of the sodium-ion battery can also be used. These positive active materials may be used alone or may be used as two or more of them in combination. Preferably, the positive active material may be one or more selected from a group consisting of NaFeO 2 , NaCoO 2 , NaCrO 2 , NaMnO 2 , NaNiO 2 , NaNi 1 / 2 Ti 1 / 2 O 2 , NaNi 1 / 2 Mn 1 / 2 O 2 , Na 2 / 3 Fe 1 / 3 Mn 2 / 3 O 2 , NaNi 1 / 3 Co 1 / 3 Mn 1 / 3 O 2 , NaFePO 4 , NaMnPO 4 , NaCoPO 4 , prussian blue material and a material with a general formula of A a M b (PO 4 ) c O x Y 3-x (A is one or more selected from a group consisting of H +< , Li +< , Na +< , K +< and NH 4 +< ; M represents transition metal cation, preferably, M is one or more selected from a group consisting of V, Ti, Mn, Fe, Co, Ni, Cu and Zn; Y represents anion of halogen, preferably, Y is one or more selected from a group consisting of F, Cl and Br; 0<a≤4, 0<b≤2, 1≤c≤3, 0≤x≤2).

[0050] In the secondary battery of the present invention, the separator is provided between the positive electrode plate and the negative electrode plate and functions to separate the positive electrode plate from the negative electrode plate. The type of the separator is not specifically limited, the separator may be any separator used in existing batteries, for example, the separator may be a polyethylene membrane, a polypropylene membrane, a polyvinylidene fluoride membrane and a multilayer composite membrane thereof, but the present invention is not limited thereto.

[0051] In the secondary battery of the present invention, generally, the electrolyte comprises an electrolyte salt and an organic solvent, the specific type and the specific component of the electrolyte salt and the organic solvent are not specifically limited and may be selected based on actual demands. The electrolyte may also comprise an additive, and the type of the additive is not specifically limited. The additive may be a negative film formation additive; the additive may also be a positive film formation additive; the additive may also be an additive used for improving one certain performance of the battery, such as an additive used for improving the overcharge performance of the battery, an additive used for improving the high-temperature performance of the battery, an additive used for improving the low-temperature performance of the battery and the like.

[0052] Hereinafter the present invention will be described in detail taking a lithium-ion battery as an example in combination with specific examples. It should be noted that, the examples described in the present invention are only used for explaining the present invention, and are not intended to limit the scope of the present invention.Example 1(1) Preparation of a positive electrode plate

[0053] The positive active material shown in table 1, super P (conductive agent) and polyvinylidene fluoride (PVDF, binder) according to a mass ratio of 96:2:2 were uniformly mixed with N-methylpyrrolidone (NMP, solvent), which then became homogeneous under stirring via a vacuum mixer, a positive slurry was obtained; then the positive slurry was uniformly coated on an aluminum foil (positive current collector), drying was then performed under room temperature and continual drying was performed in an oven, which was then followed by cold pressing and plate cutting, finally the positive electrode plate was obtained.(2) Preparation of a negative electrode plate

[0054] The negative active material shown in table 1, super P (conductive agent), carboxymethyl cellulose (CMC, thickening agent) and styrene butadiene rubber (SBR, binder) according to a mass ratio of 94.5:1.5:1.5:2.5 were uniformly mixed with deionized water (solvent), which then became homogeneous under stirring via a vacuum mixer, a negative slurry was obtained; then the negative slurry was uniformly coated on a copper foil (negative current collector) with a coating weight per unit area represented by CW of 8 mg / cm 2< , drying was then performed under room temperature and continual drying was performed in an oven, which was then followed by cold pressing and plate cutting, finally the negative electrode plate was obtained.

[0055] When the negative active material was tested in the button half battery, the obtained capacities of the button half battery satisfied the following characteristics: (A+B) / X was 0.02, A / X was 0.01.(3) Preparation of an electrolyte

[0056] Ethylene carbonate (EC), ethyl methyl carbonate (EMC) and diethyl carbonate (DEC) according to a volume ratio of 1:1:1 were mixed together to obtain an organic solvent, then sufficiently dried LiPF 6 (lithium salt) was dissolved into the mixed organic solvent to obtain an electrolyte, and a concentration of the electrolyte was 1 mol / L.(4) Preparation of a separator

[0057] The separator was a polyethylene membrane.(5) Preparation of a lithium-ion battery

[0058] The positive electrode plate, the separator and the negative electrode plate were laminated in order, the separator was positioned between the positive electrode plate and the negative electrode plate so as to separate the positive electrode plate from the negative electrode plate, then the positive electrode plate, the separator and the negative electrode plate were wound together to form an electrode assembly, then the electrode assembly was put into a case, which was followed by baking, electrolyte injection, vacuum packaging, standby, formation, shaping and the like, finally a lithium-ion battery was obtained.

[0059] Preparation of the lithium-ion batteries of examples 2-18 and comparative examples 1-6 was similiar to that in example 1, and the specific differences were shown in table 1. Thereby, examples 7, 8, 10-12 and 14 in Table 1 do not form part of this invention and are regarded as comparative examples.

[0060] Hereinafter test processes of the lithium-ion batteries were described.(1) Test of the dynamics performance

[0061] At 25 °C, the lithium-ion batteries prepared in the examples and the comparative examples were first fully charged at a constant current of x C, and then fully discharged at a constant current of 1 C for 10 cycles, then the lithium-ion batteries were fully charged at a constant current of x C, then the negative electrode plates were disassembled from the lithium-ion batteries, and the lithium precipitation on the surface of each negative electrode plate was observed. If the lithium precipitation was not observed on the surface of the negative electrode plate, the test process was repeated with a charge rate x C increased in increments of 0.1 C, until the lithium precipitation was observed on the surface of the negative electrode plate, and the test process was stopped, the charge rate x C at this time minus 0.1 C was the maximum charge rate of the lithium-ion battery.(2) Test of the cycle performance

[0062] At 25 °C, the lithium-ion batteries prepared in the examples and the comparative examples were charged at a constant current of 3 C and discharged at a constant current of 1 C, the fully charging and discharging process was repeated until the capacity of the lithium-ion battery decayed to 80% of the initial capacity, and the cycle number of the lithium-ion battery was recorded.(3) Test of the measured energy density

[0063] At 25 °C, the lithium-ion batteries prepared in the examples and the comparative examples were fully charged at a constant current of 1 C and fully discharged at a constant current of 1 C, the measured discharge capacity at this time was recorded; at 25 °C, the lithium-ion batteries were weighed by an electronic balance. And the measured energy density of the lithium-ion battery was a ratio of the measured discharge capacity of the lithium-ion battery diacharged at 1 C to the weight of the lithium-ion battery.

[0064] When the measured energy density was less than 80% of the targeted energy density, the measured energy density of the battery was considered to be very low; when the measured energy density was more than or equal to 80% of the targeted energy density and less than 95% of the targeted energy density, the measured energy density of the battery was considered to be lower; when the measured energy density was more than or equal to 95% of the targeted energy density and less than 105% of the targeted energy density, the measured energy density of the battery was considered to be moderate; when the measured energy density was more than or equal to 105% of the targeted energy density and less than 120% of the targeted energy density, the measured energy density of the battery was considered to be higher; when the measured energy density was more than or equal to 120% of the targeted energy density, the measured energy density of the battery was considered to be very high. Table 1: Parameters and test results of examples 1-18 and comparative examples 1-6Positive active materialNegative active material(A+B) / XA / XCW (mg / cm 2< )(A / X) ×CWMaximum charge rateCycle numb erMeasured energy densityExample 1LFPgraphite0.020.018.00.084.1C3300moderateExample 2LFPgraphite0.030.028.00.164.3C3600moderateExample 3LFPgraphite0.050.048.00.324.2C3100moderateExample 4LFPgraphite0.180.158.01.204.0C5000moderateExample 5LFPgraphite0.270.238.01.844.0C5500moderateExample 6LFPgraphite0.350.258.02.003.6C3200moderateExample 7LFPgraphite0.450.408.03.203.2C3100moderateExample 8LFPgraphite0.500.428.03.363.1C2600moderateExample 9LFPgraphite0.020.015.00.054.5C5100moderateExample 10LFPgraphite0.270.2315.03.453.9C4300very highExample 11LFPgraphite0.270.2318.04.143.7C4100very highExample 12LFPgraphite0.270.2319.54.493.6C4000very highExample 13LFPgraphite0.020.014.00.043.6C2300lowerExample 14LFPgraphite0.350.3320.06.603.0C2400very highExample 15LFPhard carbon0.030.028.00.164.0C3500moderateExample 16LFPhard carbon0.500.208.01.603.0C3300moderateExample 17NCM 811mixture of graphite and silicon oxide with a mass ratio of 8:20.030.018.00.084.3C1650moderateExample 18NCM 811mixture of graphite and silicon oxide with a mass ratio of 8:20.500.468.03.683.3C1500moderateComparative example 1LFPgraphite0.010.0078.00.063.6C450moderateComparative example 2LFPgraphite0.600.358.02.801.2C180moderateComparative example 3LFPhard carbon0.010.0058.00.043.6C350moderateComparative example 4LFPhard carbon0.600.408.03.201.2C160moderateComparative example 5NCM 811mixture of graphite and silicon oxide with a mass ratio of 8:20.010.0088.00.063.6C280moderateComparative example 6NCM 811mixture of graphite and silicon oxide with a mass ratio of 8:20.600.408.03.201.2C130moderate

[0065] It could be seen from the test results of table 1: when the selected negative active materials of the lithium-ion batteries prepared in examples 1-18 were tested in a button half battery, the selected negative active materials all satisfied a relationship 0.02≤(A+B) / X≤0.50, the polarization of the negative active material was smaller, the negative active material had better dynamics performance, the solid phase conduction process with respect to the lithium ions in the negative active material was easier, the weight of the negative active material coated on the unit area of the negative current collector could be maintained at a higher level, therefore the battery could have long cycle life, high energy density and fast charging capability at the same time.

[0066] Compared with examples 1-18, the obtained values of (A+B) / X from the selected negative active materials of comparative examples 1-6 were not fall within the range (that was 0.02≤(A+B) / X≤0.50) when the selected negative active materials were tested in a button half battery, the battery could not have long cycle life, high energy density and fast charging capability at the same time.

[0067] As could be seen from the comparison among examples 15-18 and comparative examples 3-6, when the battery selected different kinds of positive active materials and different kinds of negative active materials, as long as the selected negative active material satisfied a relationship 0.02≤(A+B) / X≤0.50 while being tested in a button half battery, the battery could have long cycle life, high energy density and fast charging capability at the same time.

[0068] Moreover, when the polarization of the negative active material was smaller and the dynamics performance of the negative active material was better, if the polarization of the negative active material characterized by A / X and the coating weight of the negative electrode plate per unit area represented by CW were further reasonably adjusted to satisfy a relationship 0.05≤(A / X) × CW≤4.50, the battery could have higher fast charging capability without compromising the energy density.

Claims

1. A secondary battery comprising a positive electrode plate, a negative electrode plate, an electrolyte and a separator, the negative electrode plate comprising a negative current collector and a negative film, the negative film being provided on at least one surface of the negative current collector and comprising a negative active material; wherein the negative active material comprises graphite; the negative active material is obtained by the process of being tested in a button half battery: the button half battery is discharged to 5 mV at a constant current of 0.05 C, and the obtained capacity is recorded as X; then the button half battery is discharged to 5 mV at a constant current of 50 µA, and the obtained capacity is recorded as A; then the button half battery is discharged to 5 mV at a constant current of 10 µA, and the obtained capacity is recorded as B; and the polarisation of the negative active material satisfies 0.02≤(A+B) / X≤0.50; wherein the negative electrode plate satisfies a relationship: 0.05≤(A / X)×CW≤2.00, CW represents a coating weight of the negative electrode plate per unit area with a unit of mg / cm2; and wherein the positive electrode plate comprises a positive current collector and a positive film, the positive film is provided on at least one surface of the positive current collector and comprises a positive active material, the positive active material is one or more selected from a group consisting of lithium nickel cobalt manganese oxide, lithium nickel cobalt aluminum oxide and olivine-type lithium-containing phosphate.

2. The secondary battery according to Claim 1, wherein when the negative active material is tested in a button half battery, the negative active material satisfies a relationship: 0.02 ≤ A + B / X ≤ 0.27 .

3. The secondary battery according to Claim 2, wherein when the negative active material is tested in a button half battery, the negative active material satisfies a relationship: 0.02 ≤ A + B / X ≤ 0.05 .

4. The secondary battery according to Claim 1, wherein the negative electrode plate satisfies a relationship: 0.08≤(A / X)×CW≤0.32.

5. The secondary battery according to Claim 1, wherein 0.01≤A / X≤0.25.

6. The secondary battery according to Claim 5, wherein 0.01≤A / X≤0.04.

7. The secondary battery according to any one of Claims 1 or 4, wherein the coating weight of the negative electrode plate per unit area represented by CW is 4 mg / cm2~15 mg / cm2.

8. The secondary battery according to Claim 7, wherein the coating weight of the negative electrode plate per unit area represented by CW is 8.0 mg / cm2~15 mg / cm2.

9. The secondary battery according to Claim 1, wherein an active specific surface area of the negative electrode plate is 2 cm2 / g~12 cm2 / g.

10. The secondary battery according to Claim 1, wherein the graphite is one or more selected from a group consisting of artificial graphite and natural graphite.

11. The secondary battery according to Claim 1, wherein the negative active material further comprises one or more selected from a group consisting of soft carbon, hard carbon and silicon-based material.

12. The secondary battery according to Claim 11, wherein the negative active material further comprises silicon-based material, the silicon-based material is one or more selected from a group consisting of elemental silicon, silicon oxide, silicon carbon composite and silicon alloy.