Patent Application
20230327121
The present application claims priority to Chinese Patent Application No. 202210383937.6, filed on Apr. 12, 2022, which is hereby incorporated by reference in its entirety.
The present disclosure relates to the field of battery technologies, and to a binder and a battery including the binder.
The lithium ion batteries have been widely used in various fields, such as electric vehicles, consumer electronic devices and energy storage power stations, after 30 years of rapid development, since the commercialization of the lithium ion batteries in the 1990s, and the lithium ion batteries also have an exponential growth in consumption. Production and manufacturing of the lithium ion batteries are also increasingly pursuing greenness, environmental protection, health and economy.
Compared with using water as the solvent in the negative electrode slurry, the positive electrode plate of traditional lithium batteries is prepared by using N-methylpyrrolidone (NMP) as the solvent and polyvinylidene fluoride (PVDF) as the binder. However, the price of the polyvinylidene fluoride is almost five times that of sodium carboxymethylcellulose (CMC-Na) which does not include fluorine. In addition, materials need to be recovered and recycled by expensive processes during the electrode drying process, due to the toxicity of NMP. Therefore, the preparation of the batteries not only need to consider the cost of raw materials, but also need to consider additional processing costs, which make the NMP/PVDF system very expensive in general.
At present, there are many researches on the aqueous positive electrode binder, but most of the aqueous positive electrode binder are composite systems including a plurality of polymers, and it is not conducive to the stability of the slurry, due to the physical interaction between the different polymers in such composite systems. In addition, the positive electrode binder commonly used, such as the 136DL of INDIGO, has higher glass transition temperature, resulting that the positive electrode plates are hard and brittle, and easy to crack during the applying and drying processes.
In view of the shortcomings in the present aqueous positive electrode binder, the present disclosure provides a binder and a battery comprising the binder. The binder is an aqueous positive electrode binder, which is obtained by copolymerizing a plurality of functional monomers. The binder has the characteristics of good dispersibility, good self cross-linking, strong bonding performance and good flexibility. When the binder is applied to the positive electrode, the positive electrode has the characteristics of good processability and stable viscosity of the solid content in slurry. Meanwhile, the positive electrode plate obtained by applying the slurry has high peeling force and good cyclic stability, and the rate capability is superior to that of the PVDF binder. Moreover, the binder is green and environmental friendly, and it is expected to replace the PVDF in the batteries and achieve large-scale application.
In order to achieve the object, the specific technical solutions are as follows:
A binder is provided, where the binder includes at least one polymer, and the polymer includes at least one repeating unit shown in Formula 1, at least one repeating unit shown in Formula 2, and at least one repeating unit shown in Formula 3:
where R1 is a dispersion group, R2 is a flexible group, and R3 is a self cross-linkable group; R is the same or different, and is independently selected from C1-6 alkyl or hydrogen; * is a connecting end.
According to an embodiment of the present disclosure, Rs are the same or different, and are independently selected from C1-3 alkyl or hydrogen.
According to an embodiment of the present disclosure, Rs are the same or different, and are independently selected from CH3 or hydrogen.
According to an embodiment of the present disclosure, the dispersion group refers to a group with dispersion performance, and is specifically a group with dispersion performance in the water system. The introduction of the dispersion group may make the binder have good aqueous dispersion characteristics, so that the binder fully wets an active material, which realize the effect of infiltrating the surface of the active material. In addition, the introduction of the dispersion group may also make a slurry containing the positive active material stable in water without settlement, so as to ensure the stability of the applying process and bonding.
According to an embodiment of the present disclosure, the dispersion group, that is R1, is selected from pyrrolidone group
imidazolyl
pyridyl
CONHR′, (R′ is H or C1-6 alkyl), —CN, —COOH, —COOLi, or —COONa.
R1 is derived from a polymerizable monomer with dispersion performance, preferably, is derived from the polymerizable monomer including a carbon-carbon double bond and having dispersion performance, and the polymerizable monomer is capable of forming the repeating unit shown in Formula 1; and the polymerizable monomer shown in Formula 1 is selected from at least one of: 1-vinyl-2-pyrrolidone, 1-vinylimidazole, vinylpyridine, methacrylamide, methacrylonitrile, methacrylic acid, lithium methacrylate, sodium methacrylate, acrylamide, vinyl cyanide, propenoic acid, lithium acrylate, and sodium acrylate.
According to an embodiment of the present disclosure, the flexible group refers to a group with flexibility, and a glass transition temperature Tg of a homopolymer obtained by the polymerizable monomer containing the flexible group is less than or equal to 25° C. The introduction of the flexible group may make the binder have good flexibility, so that the elongation at break is significantly improved, and the toughness is improved, thereby achieving the effect of improving the flexibility of a electrode plate.
According to an embodiment of the present disclosure, the flexible group, that is R2, is selected from —COOR4, —COO—(CH2CH2O)n—CH3, or —COO—R5—OH; where R4 is C1-6 alkyl, R5 is C1-6 alkylene, and n is an integer selected from 1 to 15.
R2 is derived from a flexible polymerizable monomer, preferably, is derived from the flexible polymerizable monomer including a carbon-carbon double bond, and the polymerizable monomer is capable of forming the repeating unit shown in Formula 2; and the polymerizable monomer is selected from at least one of: methyl acrylate, ethyl acrylate, propyl acrylate, butyl acrylate, pentyl acrylate, hydroxyethyl acrylate, and poly(ethylene glycol) methyl ether methacrylate.
According to an embodiment of the present disclosure, the self cross-linkable group refers to a group with self cross-linking performance under a certain condition, and specifically a group that may realize cross-linking by external heating without introducing a catalyst and only requiring a anhydrous condition. The introduction of the self cross-linkable group may make the binder have good self cross-linking performance, so that a cross-linked network is formed, and realize the effect of improving the stability and the peeling force of the electrode plate.
According to an embodiment of the present disclosure, the self cross-linkable group, that is R3, is selected from —C(OH)═N—R6—OH,
and R6 is C1-6 alkylene.
R3 is derived from a polymerizable monomer with self cross-linking performance, preferably, is derived from the polymerizable monomer including a carbon-carbon double bond and having self cross-linking performance, and the polymerizable monomer is capable of form the repeating unit shown in Formula 3; and the polymerizable monomer is selected from at least one of: acetoacetoxyethyl methacrylate, N-hydroxymethyl acrylamide, N-hydroxyethyl acrylamide and diacetone acrylamide.
According to an embodiment of the present disclosure, the polymer is a copolymer polymerized by at least one repeating unit shown in Formula 1, at least one repeating unit shown in Formula 2, and at least one repeating unit shown in Formula 3. Specifically, the polymer is a random copolymer or a block copolymer, preferably, is a random copolymer.
According to an embodiment of the present disclosure, the repeating unit shown in Formula 1 accounts for 40 mol % to 80 mol % of the total mole of the copolymer (For example, 40 mol %, 50 mol %, 60 mol %, 70 mol %, 80 mol %). The repeating unit shown in Formula 2 accounts for 20 mol % to 50 mol % of the total mole of the copolymer (For example, 20 mol %, 30 mol %, 40 mol %, 50 mol %). The repeating unit shown in Formula 3 accounts for 0.1 mol % to 10 mol % of the total mole of the copolymer (For example, 0.1 mol %, 1 mol %, 5 mol %, 8 mol %, 10 mol %). By regulating the molar ratio of the repeating unit shown in Formula 1, the repeating unit shown in Formula 2 and the repeating unit shown in Formula 3, the performance of the binder may be adjusted.
According to an embodiment of the present disclosure, the weight-average molecular weight of the polymer ranges from 3000 Da to 2 million Da (For example, 3000 Da, 5000 Da, 10,000 Da, 50,000 Da, 100,000 Da, 500,000 Da, 1 million Da, 2 million Da). The polymer with the weight-average molecular weight in this range may satisfy the controllable adjustment of the bonding force. When the weight-average molecular weight of the polymer is too low, the cohesion between molecules is reduced, and the bonding force is too low. When the weight-average molecular weight of the polymer is too high, for example, higher than 2 million, the molecules are seriously wound in a using process, which is not conducive to the bonding of active materials.
According to an embodiment of the present disclosure, a decomposition temperature of the polymer is greater than 300° C. That is, the polymer will not decompose at a temperature below 300° C., which indicates that the polymer has a high thermal stability. The glass transition temperature of the polymer is less than 60° C. (DSC test), that is, the polymer has a high bonding strength, and may enable the binder to have good toughness, so that the electrode plate may maintain a certain toughness.
According to an embodiment of the present disclosure, a maximum stress of the polymer ranges from 0.1 MPa to 1000 MPa (For example, 0.1 MPa, 1 MPa, 10 MPa, 50 MPa, 100 MPa, 500 MPa, 800 MPa, 1000 MPa).
According to an embodiment of the present disclosure, the elongation at break of the polymer ranges from 5% to 600% (For example, 5%, 50%, 100%, 200%, 400%, 600%).
According to an embodiment of the present disclosure, the binder further includes a solvent component, and the solvent component is selected from water, such as deionized water. When the water is selected as the solvent component, the binder system has the characteristics of no solvent releasing, environmental friendly, non-combustion, low production costs, safe application and the like.
According to an embodiment of the present disclosure, an addition amount of the solvent component is not particularly defined, as long as the binder having a specific solid content, viscosity and pH value can be prepared.
According to an embodiment of the present disclosure, the solid content of the binder ranges from 0.1 wt % to 10 wt % (For example, 0.1 wt %, 0.3 wt %, 0.5 wt %, 1 wt %, 2 wt %, 3 wt %, 4 wt %, 5 wt %, 8 wt %, 10 wt %), preferably, ranges from 0.3 wt % to 5 wt %.
According to an embodiment of the present disclosure, the viscosity of the binder ranges from 100 mPa s to 30000 mPa s (For example, 100 mPa s, 500 mPa s, 1000 mPa s, 5000 mPa s, 10000 mPa s, 20000 mPa s, 30000 mPa s), preferably, ranges from 3000 mPa s to 15000 mPa s.
According to an embodiment of the present disclosure, the pH value of the binder ranges form 5 to 7.
A research find that selecting a binder with the above-mentioned solid content, viscosity and pH value may achieve better bonding performance. For example, the binder may be suitable for different active materials, and also helpful in thickening and dispersin g the slurry.
According to an embodiment of the present disclosure, the polymer of the binder have a structural formula as shown in the following formula I:
where, x:y:z is (40 mol %-80 mol %):(20 mol %-50 mol %):(0.1 mol %-10 mol %); and the definition of R1, R2, and R3 are the same as above.
According to an embodiment of the present disclosure, the polymer of the binder have a structural formula as shown in the following formula II:
where, the definitions of x, y, and z are the same as above.
The polymer as shown in Formula II is obtained by copolymerizing 1-vinyl-2-pyrrolidone, butyl acrylate and N-hydroxyethyl acrylamide, where 1-vinyl-2-pyrrolidone plays a role in dispersing, butyl acrylate plays a role in improving flexibility, and N-hydroxyethyl acrylamide that is cross-linked in a dehydration process plays a role in cross-linking, so that the cross-linking network is formed, and the effect of improving the stability of the electrode plate is realized.
According to an embodiment of the present disclosure, the binder is cross-linked in the dehydration process (drying process) to form the cross-linking network, so that the stability of the electrode plate is improved.
The present disclosure further provides a method for preparing the binder, and the method includes the following steps:
Dissolving the polymerizable monomer containing R1 group, the polymerizable monomer containing R2 group and the polymerizable monomer containing R3 group in water, selecting a suitable initiator and a suitable catalyst depending on the polymer system, and performing a copolymerization reaction to obtain the binder.
According to an embodiment of the present disclosure, the copolymerization method may selected from radical polymerization, oxidation-reduction system polymerization, reversible addition-fragmentation chain-transfer polymerization (RAFT), atom transfer radical polymerization (ATRP) or oxidation-reduction system polymerization and the like.
According to an embodiment of the present disclosure, the reaction is performed under the protection of inert gas, and the inert gas is high-purity nitrogen or argon.
According to an embodiment of the present disclosure, a temperature of the copolymerization reaction ranges from 30° C. to 100° C. (For example, 30° C., 40° C., 50° C., 60° C., 70° C., 80° C., 100° C.), preferably from 40° C. to 80° C.
According to an embodiment of the present disclosure, the copolymerization reaction is performed under a stirring, and the stirring speed ranges from 300 rpm to 1000 rpm, preferably from 500 rpm to 800 rpm.
According to an embodiment of the present disclosure, the initiator is selected from at least one of: potassium persulfate, ammonium persulfate, sodium persulfate, potassium permanganate, a mixture of sodium persulfate and sodium bisulfite, a mixture of ferrous sulfate and hydrogen peroxide, a mixture of ammonium persulfate and tetramethylethylenediamine, and a mixture of ammonium persulfate and sodium sulfite. The addition amount of the initiator ranges from 0.1 wt % to 2 wt % (For example, 0.1 wt %, 0.5 wt %, 1 wt %, 1.5 wt %, 2 wt %) of the total mass of a comonomer.
The present disclosure further provides an application of the binder in batteries.
According to an embodiment of the present disclosure, the binder is used as a binder in the positive electrode of the batteries.
The present disclosure provides a positive electrode plate, where the positive electrode plate includes the binder mentioned above.
According to an embodiment of the present disclosure, the positive electrode plate includes a positive current collector and a positive active material layer applied to at least one side surface of the positive current collector, and the positive active material layer includes the binder mentioned above.
According to an embodiment of the present disclosure, the addition amount of the binder accounts for 0.2 wt % to 25 wt % (For example, 0.2 wt %, 1 wt %, 5 wt %, 10 wt %, 15 wt %, 20 wt %, 25 wt %) of the total mass of the positive active material layer, for example, 0.5 wt % to 15 wt %, and for example, 1 wt % to 5 wt %.
According to an embodiment of the present disclosure, the positive active material layer further includes a positive active material and a conductive agent.
According to an embodiment of the present disclosure, the positive current collector is a single-sided smooth aluminum foil, a double-sided smooth aluminum foil or a porous aluminum foil.
According to an embodiment of the present disclosure, the positive active material is at least one of: lithium iron phosphate, ternary positive electrode material (such as NCM622, NCM811, and NCA), lithium cobaltate, and lithium manganate.
According to an embodiment of the present disclosure, the conductive agent is at least one of: graphite, carbon black, acetylene black, graphene, and carbon nanotubes.
According to an embodiment of the present disclosure, an average peeling strength of the positive electrode plate including the binder ranges from 0.1 N/m to 30 N/m (For example, 0.1 N/m, 1 N/m, 5 N/m, 10 N/m, 15 N/m, 20 N/m, 25 N/m, 30 N/m).
The present disclosure further provides a method for preparing the positive electrode plate, including the following steps:
According to an embodiment of the present disclosure, the method for preparing the positive electrode plate includes the following steps:
The present disclosure further provides an application of the positive electrode plate in the batteries.
The present disclosure provides a battery, where the battery includes the binder mentioned above.
According to an embodiment of the present disclosure, the battery includes the positive electrode plate mentioned above.
According to an embodiment of the present disclosure, the battery is obtained by assembling a positive electrode plate, a separator, a negative electrode plate and electrolyte. For example, assembling the positive electrode plate, the negative electrode plate and the separator by means of common winding manner or laminating manner in the art to obtain a cell, packaging by an aluminum-plastic film, baking, injecting the electrolyte, chemical formatting, and secondary sealing sequentially to obtain a lithium ion battery.
According to an embodiment of the present disclosure, a negative active material in the negative electrode plate includes at least one of: monatomic silicon, silicon monoxide, natural graphite, artificial graphite, mesophase carbon fiber, mesocarbon microbeads, soft carbon, and hard carbon.
The beneficial effects of the present disclosure are as follows:
A novel aqueous binder with self cross-linking performance, strong bonding performance, and good flexibility is obtained by copolymerizing a plurality of functional monomers. When the binder is applied to a positive electrode, the positive electrode has the characteristics of good processability and high solid content of the slurry; the positive electrode plate obtained by applying the slurry has high peeling force and good cyclic stability; the rate capability is superior to that of the PVDF binder; the binder is green and environmental friendly; and it is expected to replace the PVDF in the batteries and achieve large-scale application.
The present disclosure will be further described in detail with reference to specific embodiments hereinafter. It should be understood that the following embodiments are only illustratively explicating and explaining the present disclosure, and should not be interpreted as limiting the protection scope of the present disclosure. All technologies implemented based on the foregoing contents of the present disclosure fall with the scope intended to protect by the present disclosure.
The experiment methods used in the following examples are conventional methods unless otherwise specified; and the reagents, materials, or the like, used in the following examples may be all obtained from commercial sources unless otherwise specified.
Synthesis of Binder 1: dissolving 1-vinyl-2-pyrrolidone (6.66 g, 60 mmol), butyl acrylate (3.84 g, 30 mmol), N-hydroxyethyl acrylamide (1.15 g, 10 mmol), ammonium persulfate (0.1 g), and sodium bisulfite (0.03 g) in water, reacting the mixture at a temperature of 65° C. for 6 h in a vacuum to obtain an aqueous positive electrode binder.
Synthesis of Binder 2: dissolving N-vinylimidazole (5.64 g, 60 mmol), butyl acrylate (3.84 g, 30 mmol), N-hydroxyethyl acrylamide (1.15 g, 10 mmol), ammonium persulfate (0.1 g), and sodium bisulfite (0.03 g) in water, reacting the mixture at a temperature of 65° C. for 6 h in a vacuum to obtain an aqueous positive electrode binder.
Synthesis of Binder 3: dissolving acrylamide (4.27 g, 60 mmol), ethyl acrylate (3.0 g, 30 mmol), N-hydroxyethyl acrylamide (1.15 g, 10 mmol), ammonium persulfate (0.1 g), and sodium bisulfite (0.03 g) in water, reacting the mixture at a temperature of 65° C. for 6 h in a vacuum to obtain an aqueous positive electrode binder.
(1) Preparation of a Positive Electrode Plate
Mixing a positive active material lithium cobaltate (LCO), a binder and a conductive agent acetylene black in a mass ratio of 97:1.5:1.5, adding the mixture into a solvent (where, PVDF uses N-methylpyrrolidone (NMP) as the solvent, and the other binders use water as the solvent), stirring under a vacuum mixer until the mixture system forming a positive electrode slurry with uniform fluidity; evenly applying the positive electrode slurry to a current collector aluminum foil (the thickness of the aluminum foil was 10 μm); baking the applied aluminum foil through an oven, and then drying it in an oven at a temperature of 120° C. for 8 h, followed by rolling and cutting it to obtain the required positive electrode plate.
Peeling Force Test of the Positive Electrode Plate:
the preparation of samples: firstly cutting the rolled positive electrode plate into strips with the length of 170 mm and the width of 30 mm using a flat paper cutter; then wiping a scale-free steel ruler cleanly using degreased gauze, without leaving stains or dust; then horizontally pasting a 60 mm width transparent adhesive tape to the bottom of the air-dried scale-free steel ruler, with the end face of the transparent adhesive tape flush with the end face of the scale-free steel ruler; and then, pasting a 25 mm width double-sided adhesive tap to the transparent adhesive tape, with the same length as the width of the transparent adhesive tape, and the center position; and finally, bonding the test samples on the double-sided adhesive tap with the end face of the test samples flush with the end face of the double-sided adhesive tap, and rolling on the surface of the positive electrode plate up and down using a pressing wheel (2 kg) with a diameter of 84 mm and a height of 45 mm.
Test of peeling force: folding the free end of the positive electrode plate of the test samples by 180°; then clamping the above folded positive electrode plate on the upper clamp holder of the AG-X plus electronic universal material testing machine; clamping the scale-free steel ruler on the lower clamp holder; preparing a plurality of positive electrode plates with the width of 30 mm at a temperature ranging from 22° C. to 28° C. and a humidity less than 25%, making the stretching speed of the electrode plate 50 mm/min, and testing the average value at the stretching of 25 mm to 80 mm; peeling the positive electrode plate, and reading the test result of the peeling strength of the coating when the current collector and the coating were completely separated. The calculation method of the peeling strength is: Peeling Strength=Peeling Force÷Electrode Plate Width.
(2) Preparation of a Negative Electrode Plate
Mixing a negative active material graphite, a thickener sodium carboxymethylcellulose (CMC-Na), a binder (ZEON 451B), and a conductive agent acetylene black in a mass ratio of 96%:1.2%:1.8%:1%, and adding the mixture into deionized water, stirring under a vacuum mixer to obtain a negative electrode slurry; evenly applying the negative electrode slurry to a high-strength copper foil coated with carbon (the thickness of the copper foil was 6 μm) to obtain a electrode plate; and airing the obtained electrode plate at room temperature, then transferring the electrode plate into an oven at a temperature of 80° C. and drying for 10 h, followed by rolling and cutting to obtain the negative electrode plate.
(3) Preparation of Electrolyte
In a glove box filled with inert gas (argon) (H2O<0.1 ppm, O2<0.1 ppm), mixing EC (ethylene carbonate), EMC (methyl ethyl carbonate), DEC (diethyl carbonate); FEC (fluorinated ethylene carbonate) in a mass ratio of 20:50:20:10 to prepare a solution, then adding fully dried lithium hexafluorophosphate (LiPF6) and lithium bis(fluorosulfonyl) imide (LiFSI) into the solution rapidly, where the mass fraction of the LiPF6 and the LiFSI in the system was 11.4% and 3.1% respectively; dissolving in a non-aqueous organic solvent, and evenly stirring. After the test results of the moisture and the residual acid were passed, the electrolyte was obtained.
(4) Preparation of a Separator
Selecting a separator coated by (5+3) ZhuoGao mixture layer with a thickness of 8 μm.
(5) Preparation of a Lithium Ion Battery
Stacking the prepared positive electrode plate, separator, and negative electrode plate in sequence to ensure the separator was located between the positive electrode plate and the negative electrode plate and plays a role in isolation, then winding to obtain a bare cell without electrolyte, placing the bare cell in an outer packaging foil, injecting the prepared corresponding electrolyte into the dried bare cell, followed by vacuum packaging, standing, chemical conversion, shaping, sorting and other processes to obtain a lithium ion battery.
A commercial oil-based PVDF (model: ARKEMA HSV 900) was used as the binder, and the cell was prepared as described in Preparation Example 4.
A commercial aqueous binder (model: INDIGO 136 D) was used as the binder, and the cell was prepared as described in Preparation Example 4.
A commercial polyvinyl pyrrolidone (Mw: 40000, purchased from Sigma-aldrich) was used as the binder, and the cell was prepared as described in Preparation Example 4.
A commercial polyvinyl imidazole (Mw: 400000, purchased from Innochem) was used as the binder, and the cell was prepared as described in Preparation Example 4.
A commercial polyacrylamide (Mw: 600000, purchased from Innochem) was used as the binder, and the cell was prepared as described in Preparation Example 4.
The Binder 1 was used as the binder, and the cell was prepared as described in Preparation Example 4.
The Binder 2 was used as the binder, and the cell was prepared as described in Preparation Example 4.
The Binder 3 was used as the binder, and the cell was prepared as described in Preparation Example 4.
Mechanical Performance Test of the Binder:
Preparing the binders in the Comparative Examples and Examples into strip samples having size of length×width×height was 32 mm×12 mm×1 mm, respectively, stretching on a universal stretching testing machine with a stretching rate of 50 mm/min under a condition of 22° C. to 28° C. and a humidity of 30%, and the specific data is shown in Table 1.
It can be seen from Table 1 that the maximum stretching strength of the binder PVDF in Comparative Example 1 is lower than that of Comparative Examples 2 to 5, but the elongation at break is much higher than that of Comparative Examples 2 to 5, indicating that the PVDF has better flexibility, so that the electrode plate is not easy to crack in the drying process, and the risk of dropping powder in the winding process is reduced.
However, the maximum stretching strength of the binder in Examples 1-3 is higher than that of Comparative Example 1, which is mainly due to the reason that the self cross-linking group is introduced in the synthesis process to form the cross-linked network, thereby improving the cohesion of the binder and further improving the maximum stretching strength. In addition, the elongation at break of the binders in Examples 1 to 3 are also superior to that of Comparative Example 1, which is mainly due to the introduction of part of the flexible groups into the binders, thereby improving the flexibility of the binders, and the elongation at break is superior to that of the traditional PVDF binder.
Performance Test of the Lithium Ion Battery
The Comparative Examples 1 to 5 use the commercial oil-based PVDF, the aqueous 136D, the polyvinyl pyrrolidone, the polyvinyl imidazole, and the polyacrylamide as the positive electrode binder respectively. From the data of the stretching strength of the rolled positive electrode plate, it can be seen that the average peeling strength of the aqueous 136D is greater than that of the conventional oil-based binder PVDF, while the average peeling strength of the polyvinyl pyrrolidone, the polyvinyl imidazole and the polyacrylamide are less than that of PVDF.
However, the peeling strength of the binders in Examples 1 to 3 are superior to that of PVDF, which is mainly due to the distribution of the binder is more uniform caused by the dispersion monomer, and the flexibility and motion capability of the binder is improved by the flexibility monomer, so that the interaction between the main materials is improved. The self cross-linking monomer constructs the cross-linked network, leading to improving the interaction between the binders, and achieving the improvement of the peeling strength.
In addition, in terms of the cell capacity retention ratio, the PVDF binder of Comparative Example 1 is superior to those of Comparative Examples 2 to 5, which is related to the good dispersibility to the positive active material and its own good flexibility, while the capacity retention rates in Examples 1 to 3 are superior than that of Comparative Example 1, especially in Example 1, the capacity retention rate performance is optimal.
It can be seen from Table 3 that the constant-current charging ratio at different charging rate in Examples 1 to 3 using the aqueous binders are superior to that of Comparative Example 1 using the traditional oil-based PVDF binder, indicating that the aqueous binder has better rate charging performance.
Electrochemical Impedance Test: letting the battery stand at a constant environment at 45° C., and constant charging to 4.45 V at 1 C with a 0.05 C cut-off current. Performing EIS Test with the fully charged batteries. The specific data is shown in Table 4 and
/mΩ
It can be seen from Table 4 and
In summary, it can be seen that the aqueous positive electrode binder provided by the present disclosure has self cross-linking performance, strong bonding performance and good flexibility. The binder is applied to the positive active materials such as lithium iron phosphate and lithium cobaltate, resulting that the processability is good, the solid content of the slurry is high, the peeling force of the applied electrode plate is high, the cyclic stability is good, the rate performance is superior to that of the PVDF binder, the binder is green and environment-friendly, and it is expected to replace the PVDF in the batteries and achieve large-scale application.
The implementations of the present disclosure have been illustrated above. However, the present disclosure is not limited to the above-mentioned implementations. Any modification, equivalent replacement, improvement, or the like, made within the spirit and principles of the present disclosure shall fall within the protection scope of the present disclosure.
| Number | Date | Country | Kind |
|---|---|---|---|
| 202210383937.6 | Apr 2022 | CN | national |
