Patent Application
20200127278
The present application claims priority to Chinese patent application No. CN201811209254.9, filed on Oct. 17, 2018, which is incorporated herein by reference in their entirety.
The present disclosure relates to the field of battery, and particularly relates to a secondary battery.
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.
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.
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.
In view of the problem existing in the background, an object of the present disclosure is to provide a secondary battery, which has the characteristics of long cycle life, high energy density and fast charging capability at the same time.
The present disclosure 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 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, 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.
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.
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. Preferably, 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.
The coating weight of the negative electrode plate per unit area represented by CW is 4 mg/cm2˜15 mg/cm2. Preferably, the coating weight of the negative electrode plate per unit area represented by CW is 8.0 mg/cm2˜15 mg/cm2.
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.
An active specific surface area of the negative electrode plate is 2 cm2/g˜12 cm2/g.
The graphite is one or more selected from a group consisting of artificial graphite and natural graphite.
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.
The positive electrode plate 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 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.
Compared with the existing technologies, the present disclosure at least includes the following beneficial effects: in the present disclosure, 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.
Hereinafter a negative electrode plate and a secondary battery according to the present disclosure are described in detail.
Firstly, a negative electrode plate according to a first aspect of the present disclosure 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.
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.
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.
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 LiPF6, 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.
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.
The solid phase conduction process with respect to the active ions in the negative active material has a very important 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.
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.
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.
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.
In some embodiments of the present disclosure, 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.
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.
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.
The inventors has done a large number of researches and found that, when 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 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/cm2.
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.
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.
In some embodiments of the present disclosure, 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.
Preferably, 0.07≤(A/X)×CW≤3.50.
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.
Preferably, the coating weight of the negative electrode plate per unit area represented by CW is 3 mg/cm2˜20 mg/cm2. More preferably, the coating weight of the negative electrode plate per unit area represented by CW is 4 mg/cm2˜15 mg/cm2. 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.
In the negative electrode plate of the present disclosure, preferably, a particle size of the negative active material represented by D50 is 4 μm˜18 More preferably, the particle size of the negative active material represented by D50 is 4 μm˜16 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.
In the negative electrode plate of the present disclosure, preferably, an active specific surface area of the negative electrode plate is 2 cm2/g˜12 cm2/g. More preferably, the active specific surface area of the negative electrode plate is 3 cm2/g˜10 cm2/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.
The test process of the active specific surface area of the negative electrode plate is described as follows.
The negative electrode plate of the present disclosure 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 ip of each cyclic voltammetry curve is extracted using a EC-Lab software. A linear graph of ip and √{square root over (v)} is obtained where the square root of the scanning rate v (√{square root over (v)}) is used as X-coordinate and the peak current ip is used as Y-coordinate, and then the slope K of the linear graph is obtained.
In a Randles-Sevick equation, ip=2.69×105 n3/2Ac√{square root over (D)}√{square root over (v)}, therefore the slope is obtained according to an equation K=2.69×105n3/2Ac√{square root over (D)}. n represents 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 represents a concentration of ferrocene, here the value thereof is 50 mmol/L; D represents a diffusion coefficient of the probe ferrocene, here the value thereof is 2.1×10−6 cm2/s; A represents an active surface area of the negative electrode plate, and is obtained according to an equation A=K/(2.69×105n3/2c√{square root over (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.
In the negative electrode plate of the present disclosure, 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.
In the negative electrode plate of the present disclosure, 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.
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 disclosure, it is considered that the negative electrode plate falls within the protection scope of the present disclosure.
Next a secondary battery according to a second aspect of the present disclosure is described, the secondary battery comprises the negative electrode plate according to the first aspect of the present disclosure.
Moreover, the secondary battery of the present disclosure further comprises a positive electrode plate, an electrolyte and a separator.
In the secondary battery of the present disclosure, 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.
It should be noted that, the secondary battery according to the second aspect of the present disclosure 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 disclosure.
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 disclosure 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 LiCoO2, LiNiO2, LiMnO2, LiMn2O4, LiN1/3Co1/3Mn1/3O2 (NCM333), LiNi0.5Co0.2Mn0.3O2 (NCM523), LiNi0.6Co0.2Mn0.2O2 (NCM622), LiNi0.8Co0.1Mn0.1O2 (NCM811), LiNi0.85Co0.15Al0.05O2, LiFePO4 (LFP) and LiMnPO4.
When the secondary battery is the sodium-ion battery, the positive active material may be selected from transition metal oxide NaxMO2 (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 disclosure 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 NaFeO2, NaCoO2, NaCrO2, NaMnO2, NaNiO2, NaNi1/2Ti1/2O2, NaNi1/2Mn1/2O2, Na2/3Fe1/3Mn2/3O2, NaNi1/3Co1/3Mn1/3O2, NaFePO4, NaMnPO4, NaCoPO4, prussian blue material and a material with a general formula of AaMb(PO4)cOxY3-x (A is one or more selected from a group consisting of H+, Li+, Na+, K+ and NH4+; 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).
In the secondary battery of the present disclosure, 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 disclosure is not limited thereto.
In the secondary battery of the present disclosure, 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.
Hereinafter the present disclosure 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 disclosure are only used for explaining the present disclosure, and are not intended to limit the scope of the present disclosure.
(1) Preparation of a Positive Electrode Plate
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
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/cm2, 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.
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
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 LiPF6 (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
The separator was a polyethylene membrane.
(5) Preparation of a Lithium-Ion Battery
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.
Preparation of the lithium-ion batteries of examples 2˜18 and comparative examples 1-6 was similar to that in example 1, and the specific differences were shown in table 1.
Hereinafter test processes of the lithium-ion batteries were described.
(1) Test of the Dynamics Performance
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
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
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 discharged at 1 C to the weight of the lithium-ion battery.
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.
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.
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.
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.
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.
According to the foregoing disclosure and teachings of the present disclosure, a person skilled in the art may also make variations and modifications to the above implementing manners. Therefore, the present disclosure is not limited to the specific implementing manners disclosed and described in the above, modifications and variations of the present disclosure will also be fallen within the scope of the claims of the present disclosure. Furthermore, although specific terminologies are used in the present disclosure, these terminologies are merely for convenience of description, and are not intended to limit the present disclosure.
| Number | Date | Country | Kind |
|---|---|---|---|
| 201811209254.9 | Oct 2018 | CN | national |
