Patent Application
20250023093
This application claims the priority benefit of China application serial no. 202310858153.9, filed on Jul. 13, 2023. The entirety of each of the above-mentioned patent applications is hereby incorporated by reference herein and made a part of this specification.
The disclosure relates to the technical field of lithium-ion batteries, and in particular to a lithium-ion battery and an application thereof.
Currently, the rapid development of lithium-ion batteries in the fields of electric vehicles and large-scale energy storage has made the lithium-ion battery market size to expand considerably. In particular, lithium iron phosphate batteries have become the mainstream in the development of lithium-ion batteries because they are characterized in low cost and long cycle life. However, the specific capacity of current lithium iron phosphate substances is close to its theoretical value, and therefore the energy density of lithium iron phosphate batteries has nearly reached the limit.
Lithium iron manganese phosphate is obtained by replacing part of the iron in lithium iron phosphate with manganese, thereby increasing the energy density of lithium iron manganese phosphate without increasing the cost of the positive electrode active material. However, the conductivity of lithium iron manganese phosphate is poor. In lithium-ion batteries, the dynamics performance of battery is poor, which in turn leads to the attenuation of cycle performance. During the cycle of lithium iron manganese phosphate batteries, due to the dissolution of manganese ions, the solid electrolyte interphase (SEI) is destructed, which causes the increase of consumption of active lithium in the battery and increase of the resistance of the negative electrode SEI film, and the cycle life of the battery is affected accordingly.
The present disclosure provides a lithium-ion battery and an application thereof.
Through the lithium-ion battery and the application thereof provided by the present disclosure, the stability of the electrolyte may be improved, the cycle performance of the lithium-ion battery may be enhanced, and the performance of lithium-ion batteries at high temperatures may be increased.
In order to solve the above technical problems, the present disclosure provides a lithium-ion battery, which at least includes the following ingredients:
In an embodiment of the present disclosure, the molecular formula of the lithium iron manganese phosphate is LixMnyFe1-yPO4, where 0.95≤x≤1.05 and 0.4≤y≤0.7.
In an embodiment of the present disclosure, the mass fraction of the ethylene carbonate accounts for 15 wt %˜30 wt % in the non-aqueous solvent.
In an embodiment of the present disclosure, the electrolyte further includes a positive electrode film-forming additive, the positive electrode film-forming additive includes 1,3-propane sultone, and the mass content of the positive electrode film-forming additive accounts for 0.01 wt˜5 wt % in the electrolyte.
In an embodiment of the present disclosure, the electrolyte further includes a negative electrode film-forming additive, the negative electrode film-forming additive includes vinylene carbonate, and the mass content of the negative electrode film-forming additive accounts for 0.1 wt˜10 wt % in the electrolyte.
In an embodiment of the present disclosure, the non-aqueous solvent further includes any one or a combination of at least two of dimethyl carbonate, ethyl methyl carbonate, propylene carbonate or diethyl carbonate.
In an embodiment of the present disclosure, the non-aqueous solvent further includes ethyl methyl carbonate and dimethyl carbonate, and the mass ratio of ethylene carbonate, ethyl methyl carbonate and dimethyl carbonate is (0.5-4.5):(2.75-4.75):(2.75-4.75).
In an embodiment of the present disclosure, the mass content of the non-aqueous solvent accounts for 60 wt %˜85 wt % in the electrolyte.
In an embodiment of the present disclosure, the electrolyte further includes a lithium salt, and the lithium salt includes any one or a combination of at least two of LiPF6, LiBF4, LiFSI, LiTFSI, LiBOB, LIODFP, LiODFB, LiPO2F2 or CF3SO3Li.
In an embodiment of the present disclosure, the concentration of the lithium salt in the electrolyte is 0.1 mol/L˜2 mol/L.
The present disclosure further provides an electrochemical device, including the above-mentioned lithium-ion battery.
In summary, the present disclosure provides a lithium-ion battery and an application thereof, which may improve the conductivity of the electrolyte, ensure the oxidation stability of the electrolyte, enhance the dynamics of the lithium-ion battery, and increase the cycle performance. A dense CEI film may be generated on the surface of the positive electrode to reduce the oxidative decomposition of the electrolyte. A dense SEI film may be generated on the negative electrode, and the SEI film may repaired continuously during the cycle, thereby reducing the damage to the SEI film of the negative electrode caused by the dissolution of manganese ions, and effectively improving the cycle life of lithium iron manganese phosphate batteries. By controlling the type and content of solvents, positive electrode additives, and negative electrode additives, the stability of the electrolyte is improved, the cycle performance of the lithium-ion battery is enhanced, and the performance of the lithium-ion battery at high temperatures is increased.
In order to explain the embodiments of the present disclosure or the technical solutions in the related art more clearly, the drawings needed to be used in the description of the embodiments or the related art will be briefly introduced below. Clearly, the drawings in the following description are only some embodiments of the present disclosure. For those of ordinary skill in the art, other drawings may be obtained based on these drawings without exerting creative efforts.
The FIGURE is a schematic structural view of a lithium-ion battery in an embodiment of the present disclosure.
The following describes the implementation of the present disclosure through specific examples. Those skilled in the art can easily understand other advantages and effects of the present disclosure from the contents disclosed in this specification. The present disclosure can also be implemented or applied through other different specific implementations. Various details in this specification can also be modified or changed in various ways based on different viewpoints and applications without departing from the spirit of the present disclosure.
It should be understood that the disclosure may be embodied in different forms and should not be construed as limited to the embodiments set forth herein. Rather, these embodiments are provided so that this disclosure will be thorough and complete, and will fully convey the scope of the disclosure to those skilled in the art.
The technical solution of the present disclosure will be further described in detail below with reference to several embodiments and drawings. Clearly, the described embodiments are only some of the embodiments of the present disclosure, rather than all of the embodiments. Based on the embodiments of the present disclosure, all other embodiments obtained by those of ordinary skill in the art without any creative work fall within the scope of protection of the present disclosure.
Please refer to the FIGURE. The present disclosure provides a lithium-ion battery, including a positive electrode sheet 10, a negative electrode sheet 20, a separator 30 and an electrolyte 40. The separator 30 is located between the positive electrode sheet 10 and the negative electrode sheet 20. Electrolyte 40 is filled between the positive electrode sheet 10, the negative electrode sheet 20 and separator 30. The present disclosure does not limit the type and shape of the lithium-ion battery. In an embodiment of the present disclosure, the lithium-ion battery is a primary battery or a secondary battery. The secondary battery is, for example, a soft-pack battery, a hard-housing battery or a cylindrical battery. In this embodiment, a soft-packed secondary battery is taken as an example for explanation.
Please refer to the FIGURE. In an embodiment of the present disclosure, the positive electrode sheet 10 includes a positive electrode current collector and a positive electrode active material layer coated on one side of the positive electrode current collector. The positive electrode active material layer includes a positive electrode active material, a binder, a conductive agent and so on. The positive electrode current collector may be, for example, a foil substance formed by nickel, titanium, aluminum, nickel, silver, stainless steel, or carbon processed through surface treatment. In addition to foil substances, the positive electrode current collector may also be adopted in various forms including any one of or multiple combinations of film, mesh, pore, foam or non-woven fabric. The thickness of the positive electrode current collector is, for example, 8 μm to 15 μm. In this embodiment, the positive electrode current collector is, for example, aluminum foil.
In an embodiment of the present disclosure, the positive electrode active material is selected from lithium iron manganese phosphate, for example, and the molecular formula of lithium iron manganese phosphate is LixMnyFe1-yPO4, where 0.95≤x≤1.05 and 0.4≤y≤0.7. The binder is, for example, selected from any one or more polyvinylidene fluoride (PVDF), polyamide (PA), polyacrylonitrile (PAN), polyacrylate, polyvinylether, polymethyl methacrylate (PMMA), ethylene-propylene-diene terpolymer (EPDM), polyhexafluoropropylene, or polymerized styrene butadiene rubber (SBR). The conductive agent is, for example, selected from any one or more of conductive carbon black (super P, SP), acetylene black, carbon nanotubes, graphene, and the like.
Please refer to the FIGURE. In an embodiment of the present disclosure, the positive electrode active material is LiMn0.6Fe0.4PO4, the binder is selected from polyvinylidene fluoride, and the conductive agent is selected from acetylene black, for example. After the positive electrode active material, acetylene black and polyvinylidene fluoride are mixed in a weight ratio of 95:3:2, for example, an organic solvent is added and stirred until the system becomes homogeneous to obtain a positive electrode slurry. The organic solvent is, for example, selected from N-Methylpyrrolidone (NMP). After the positive electrode slurry is evenly coated on the aluminum foil for drying, and then the dried aluminum foil is subjected to processes such as cold pressing to obtain the positive electrode sheet 10. In this embodiment, the double-sided density of the positive electrode sheet is greater than or equal to 35 mg/cm2.
Please refer to the FIGURE. In an embodiment of the present disclosure, the negative electrode sheet 20 includes, for example, a negative electrode current collector and a negative electrode active material layer coated on at least one side of the negative electrode current collector. The negative electrode active material layer includes a negative electrode active material, a binder, a conductive agent and a thickener, etc. The negative electrode current collector is, for example, selected from one of a copper foil current collector, a composite copper foil current collector, a carbon current collector, a foamed copper current collector, a stainless steel current collector, etc., and the thickness of the negative electrode current collector is, for example, 8 μm˜15 μm.
Please refer to the FIGURE. In an embodiment of the present disclosure, the negative electrode active material is selected from any one or a combination of at least two of a soft carbon, a hard carbon, an artificial graphite, a natural graphite, a silicon, a silicon oxide compound, a silicon carbon compound, or a lithium titanate. The binder is, for example, selected from any one or more of polyvinylidene fluoride, polyamide, polypropylene, polyacrylate, polyvinyl ether, polymethylmethacrylate, polyhexafluoropropylene or styrene-butadiene rubber. The conductive agent is, for example, selected from any one or more of a conductive carbon black, an acetylene black, a carbon nanotube, a graphene, and the like. In an embodiment of the present disclosure, the negative electrode current collector is selected from a copper foil, for example; the negative electrode active material is selected from graphite, for example; the conductive agent is selected from an acetylene black, for example; the binder is selected from a styrene-butadiene rubber, for example; and the thickener is selected from sodium carboxymethyl cellulose, for example. In an embodiment of the present disclosure, the graphite, the acetylene black, the styrene-butadiene rubber and the sodium carboxymethyl cellulose are mixed at a mass ratio of, for example, 96:2:1:1, deionized water is added, and the mixture is fully stirred to obtain a negative electrode slurry. The negative electrode slurry is evenly coated on the copper foil, and processes such as drying and cold pressing are carried out to obtain the negative electrode sheet 20.
Please refer to the FIGURE. In an embodiment of the present disclosure, the separator 30 is, for example, a polyethylene (PE) film, a polypropylene (PP) film, a fiberglass film, a polyethylene film or a composite film, and the thickness of the separator is, for example, 9 μm˜15 μm. In this embodiment, polyethylene in a thickness of 8 μm˜10 μm is selected as the base film for the separator, and a nano-alumina coating with a thickness of 2 μm˜4 μm is coated on the base film to obtain the separator 30.
Please refer to the FIGURE. In an embodiment of the present disclosure, the electrolyte 40 at least includes a non-aqueous solvent, a lithium salt, and an additive. When the double-sided density of the positive electrode sheet 10 is greater than or equal to 35 mg/cm2, the non-aqueous solvent includes ethylene carbonate (EC) with a high dielectric constant, and the mass fraction of ethylene carbonate accounts for 10 wt %˜35 wt % in the non-aqueous solvent, or for example, 15 wt %˜30 wt %, to improve the conductivity of the electrolyte. If the content of EC is too low, it may not be ensured that the electrolyte 40 has a high conductivity, and the dynamics performance of the high-density lithium iron manganese phosphate battery may not be improved. If the content of EC is too high, the oxidation stability of the electrolyte 40 will be reduced, and irreversible oxidative decomposition reaction will occur in the positive electrode, and therefore the cycle performance of the battery will be deteriorated. Therefore, by adding and controlling the content of ethylene carbonate in the electrolyte, the conductivity of the electrolyte may be improved; in the meantime, the amount of added ethylene carbonate may be controlled to prevent the deterioration of the oxidation stability of the electrolyte.
Please refer to the FIGURE. In an embodiment of the present disclosure, the non-aqueous solvent further includes, for example, any one or a combination of at least two of dimethyl carbonate (DMC), ethyl methyl carbonate (EMC), propylene carbonate (PC) or diethyl carbonate (DEC). Non-aqueous solvents include, for example, ethyl methyl carbonate and dimethyl carbonate, and the mass ratio of ethylene carbonate, ethyl methyl carbonate and dimethyl carbonate is (0.5-4.5):(2.75-4.75):(2.75-4.75). In an embodiment of the present disclosure, the mass content of the non-aqueous solvent accounts for 60%˜85% in the electrolyte 40, for example. When preparing the electrolyte, when the content of nitrogen in the glove box is 99.999%, the actual content of oxygen in the glove box is less than or equal to 0.1 ppm, and the content of moisture is less than or equal to 0.1 ppm, after mixing the battery-grade ethylene carbonate, ethyl methyl carbonate and dimethyl carbonate are mixed evenly, the fully dried lithium salt is added to the above-mentioned non-aqueous solvent, and an additive is added to prepare the non-aqueous electrolyte of the lithium-ion battery.
Please refer to the FIGURE. In an embodiment of the present disclosure, the additive further include a positive electrode film-forming additive and a negative electrode film-forming additive. The positive electrode film-forming additive includes 1,3-propanesultone (PS), and the mass content of the positive electrode film-forming additive accounts for 0.01 wt˜5 wt % in the electrolyte 40, for example, or 0.1 wt˜2 wt %, for example. The positive electrode film-forming additive may generate a dense cathode-electrolyte interface (CEI) on the surface of the positive electrode, thus reducing the oxidative decomposition of the electrolyte 40. If the mass content of the positive electrode film-forming additive is too low, a dense CEI film cannot be formed on the positive electrode to prevent oxidative decomposition of the electrolyte 40. If the content of the positive electrode film-forming additive is too high, an excessively thick CEI film will be formed, which increases the interface resistance of the positive electrode and results in a decrease in dynamics performance and cycle life of the battery. Therefore, the mass content of the positive electrode film-forming additive is controlled to ensure the stability of the positive electrode, reduce the decomposition of the electrolyte, and improve the cycle performance of the lithium-ion battery.
Please refer to the FIGURE. In an embodiment of the present disclosure, the negative electrode film-forming additive includes vinylene carbonate (VC), and the mass content of the negative electrode film-forming additive accounts for 0.1 wt˜10 wt % in the electrolyte 40, or 0.5 wt %˜3 wt %, for example, to form a high-quality SEI film on the negative electrode. If the mass content of VC is too low, a dense SEI film may not be formed, and the SEI film may not be continuously repaired in time during the cycle. Under the circumstances, the manganese ions dissolved from the positive electrode will rapidly deteriorate the negative electrode interface, causing loss of lithium and destruction of dynamics performance of the negative electrode, and the cycle life of the battery will decay rapidly. If the mass percentage of VC is too high, the viscosity of the electrolyte will increase rapidly, causing the conductivity of the electrolyte 40 to drop and deteriorating the dynamics performance of the lithium-ion battery. Therefore, controlling the content of VC enables VC to form a dense SEI film on the negative electrode, and allow the SEI film to be repaired continuously during the cycle, thus reducing the damage to the SEI film of the negative electrode caused by the dissolution of manganese ions. Through the use of EC, PS and VC altogether, the dynamic performance of the lithium-ion battery is improved, and the cycle life of the lithium iron manganese phosphate battery may be increased effectively.
Please refer to the FIGURE. In an embodiment of the present disclosure, the electrolyte 40 further includes a lithium salt. The lithium salt is selected from, for example, any one or a combination of at least two of lithium hexafluorophosphate (LiPF6), lithium tetrafluoroborate (LiBF4), lithium bisfluorosulfonimide (LiFSI), lithium bistrifluoromethanesulfonimide (LiTFSI), lithium bisoxaloborate (LiBOB), lithium difluorobisoxalate phosphate (LiODFP), lithium difluorooxalateborate (LiODFB), lithium difluorophosphate (LiPO2F2) or lithium triflate (LiCF3SO3). In an embodiment of the present disclosure, the concentration of the lithium salt in the electrolyte 40 is 0.1 mol/L˜2 mol/L.
Please refer to the FIGURE. In an embodiment of the present disclosure, the above-mentioned positive electrode sheet 10, the separator 30, and the negative electrode sheet 20 are stacked in order, so that the separator 30 is located between the positive electrode sheet 10 and the negative electrode sheet 20 to separate them, and they are laminated to obtain a bare battery cell. The bare battery cell is put into the aluminum plastic film, then baked at 80° C. to remove water, the electrolyte 40 is injected thereto and sealed. Thereafter, the sealed bare battery cell is kept standing and subjected to hot and cold pressing, formation, clamping and volume division to obtain the finished soft-packed lithium-ion battery.
Hereinafter, the present disclosure will be explained more specifically by referring to examples, which should not be construed as limiting. Appropriate modifications can be made within the scope consistent with the gist of the present disclosure, and the modifications shall all fall within the technical scope of the present disclosure.
Preparation of positive electrode sheet: The positive electrode active material selected from LiMn0.6Fe0.4PO4, the conductive agent selected from acetylene black and the binder selected from polyvinylidene fluoride were mixed in a mass ratio of 95:3:2. After the positive electrode active material, the binder and the conductive agent were mixed evenly, the solvent selected from N-Methylpyrrolidone was added and stirred until the mixture was uniform and transparent to obtain a positive electrode slurry. The positive electrode slurry was evenly coated on the aluminum foil and dried, and then cold pressed to obtain a positive electrode sheet. The double-sided density of the positive electrode sheet is 38 mg/cm2.
Preparation of negative electrode sheet: The negative active material selected from graphite, the conductive agent selected from acetylene black, the binder selected from styrene-butadiene rubber and the thickener selected from sodium carboxymethyl cellulose were mixed in a mass ratio of 96:2:1:1, and deionized water was added and stirred thoroughly to obtain the negative electrode slurry. The negative electrode slurry was evenly coated on the copper foil and dried, and then cold pressed to obtain the negative electrode sheet.
Preparation of electrolyte: Under the conditions that the content of nitrogen in the glove box was 99.999%, the actual content of oxygen in the glove box was 0.1 ppm, and the content of moisture was 0.1 ppm, the non-aqueous solvent was composed of ethylene carbonate, ethyl methyl carbonate and carbonic acid in a mass ratio of 2:4:4. Taking the total mass of the electrolyte as 100%, the lithium salt and the additive were added such that the concentration of lithium hexafluorophosphate was 1 mol/L, the mass percentage of PS was 1 wt % in content, and the mass percentage of VC was 2 wt % in content, and the electrolyte was obtained.
Selection of separator: 9 μm of polyethylene was selected as the base film, and a nano-alumina coating having a thickness of 3 μm was coated on the base film to obtain a separator.
Preparation of the battery: The positive electrode sheet, the separator, and the negative electrode sheet were stacked in order, so that the separator was between the positive electrode sheet and the negative electrode sheet to separate them, and they were laminated to obtain a bare battery cell. The bare battery cell was wrapped with an aluminum plastic film, then baked at 80° C. to remove water, the electrolyte 40 was injected thereto and sealed. Thereafter, the sealed bare battery cell was kept standing and subjected to hot and cold pressing, formation, clamping and volume division to obtain the lithium-ion battery.
In the electrolyte, the mass ratio of ethylene carbonate, ethyl methyl carbonate and dimethyl carbonate was 0.5:4.75:4.75, and other steps were the same as those described in Example 1.
In the electrolyte, the mass ratio of ethylene carbonate, ethyl methyl carbonate and dimethyl carbonate was 1:4.5:4.5, and other steps were the same as those described in Example 1.
In the electrolyte, the mass ratio of ethylene carbonate, ethyl methyl carbonate and dimethyl carbonate was 1.5:4.25:4.25, and other steps were the same as those described in Example 1.
In the electrolyte, the mass ratio of ethylene carbonate, ethyl methyl carbonate and dimethyl carbonate was 3:3.5:3.5, and other steps were the same as those described in Example 1.
In the electrolyte, the mass ratio of ethylene carbonate, ethyl methyl carbonate and dimethyl carbonate was 3.5:3.25:3.25, and other steps were the same as those described in Example 1.
In the electrolyte, the mass ratio of ethylene carbonate, ethyl methyl carbonate and dimethyl carbonate was 4.5:2.75:2.75, and other steps were the same as those described in Example 1.
In the electrolyte, the mass percentage of PS was 0.005 wt %, and other steps were the same as those described in Example 1.
In the electrolyte, the mass percentage of PS was 0.01 wt %, and other steps were the same as those described in Example 1.
In the electrolyte, the mass percentage of PS was 0.1 wt %, and other steps were the same as those described in Example 1.
In the electrolyte, the mass percentage of PS was 3 wt %, the concentration of LiFSI was 0.6 mol/L, and other steps were the same as those described in Example 1.
In the electrolyte, the mass percentage of PS was 5 wt %, and other steps were the same as those described in Example 1.
In the electrolyte, the mass percentage of PS was 8 wt %, and other steps were the same as those described in Example 1.
In the electrolyte, the mass percentage of VC was 0.05 wt %, and other steps were the same as those described in Example 1.
In the electrolyte, the mass percentage of VC was 0.1 wt %, and other steps were the same as those described in Example 1.
In the electrolyte, the mass percentage of VC was 0.5 wt %, and other steps were the same as those described in Example 1.
In the electrolyte, the mass percentage of VC was 3 wt %, and other steps were the same as those described in Example 1.
In the electrolyte, the mass percentage of VC was 10 wt %, and other steps were the same as those described in Example 1.
In the electrolyte, the mass percentage of VC was 15 wt %, and other steps were the same as those described in Example 1.
In the electrolyte, the mass ratio of ethylene carbonate, ethyl methyl carbonate and dimethyl carbonate was 0:5:5, and other operations were the same as those described in Example 1.
In the electrolyte, PS was not added, and other operations were the same as those described in Example 1.
In the electrolyte, VC was not added, and other operations were the same as those described in Example 1.
In the present disclosure, performance tests were performed on the lithium-ion batteries obtained in Examples 1 to 19 and Comparative Examples 1 to 3, such as tests on the capacity retention rate of the lithium-ion battery after cycles at the normal temperature and the capacity retention rate of the lithium-ion battery after cycles at high temperatures. The results are shown in Table 1.
In an embodiment of the present disclosure, the test on capacity retention rate after cycles at the normal temperature was carried out as follows. The lithium-ion battery was charged at a constant current of 1C to 4.2V at a temperature of 25° C., and then charged at a constant voltage of 4.2V until the current was less than 0.05C. After standing for 10 minutes, the lithium-ion battery was discharged to 2.5V at a constant current of 1C. The discharge capacity of the lithium-ion battery was tested under the circumstances, and the result was used as the discharge capacity of the first cycle. The above process was performed on the battery for multiple cycles, and the capacity retention rate of the battery after 400 cycles was calculated. Relative capacity retention rate after cycles was calculated according to the following formula:
In an embodiment of the present disclosure, the test on capacity retention rate for cycles under high temperatures was carried out as follows. The lithium iron manganese phosphate battery was charged at a constant current of 1C to 4.2V at 45° C., then charged at a constant voltage of 4.2V until the current was less than 0.05C. After standing for 10 minutes, the lithium iron manganese phosphate battery was discharged to 2.5V at a constant current of 1C, and the discharge capacity of the lithium iron manganese phosphate battery was tested under the circumstances, and the result was used as the discharge capacity of the first cycle. The above process was performed on the battery for multiple cycles, and the capacity retention rate of the battery after 400 cycles was calculated. Relative capacity retention rate after cycles was calculated according to the following formula:
Please refer to Table 1. Comparing Examples 1 to 19 with Comparative Example 1, it can be seen that by adding ethylene carbonate to the electrolyte and controlling the amount of ethylene carbonate, the retention rate of the lithium-ion battery after cycles at normal temperature and the retention rate of the lithium-ion battery after cycles at high temperatures may be improved simultaneously. That is, by adding ethylene carbonate, the conductivity of the electrolyte may be increased, and the cycle performance of high-density lithium-ion batteries may be enhanced, and by controlling the content of ethylene carbonate, it is possible to prevent the deterioration of electrolyte stability caused by excessive content. Comparing Examples 1 to 19 with Comparative Example 2, it can be seen that by adding the positive electrode additive PS, a dense CEI film may be formed on the positive electrode, and the dynamics performance and cycle performance of lithium-ion batteries may be enhanced. Comparing Examples 1 to 19 with Comparative Example 3, it can be seen that by adding the negative electrode additive VC, a dense SEI film may be formed on the negative electrode, and the SEI film may be continuously repaired during the cycle, so as to reduce the damage to the negative electrode SEI film caused by the dissolution of manganese ions. In this way, it is possible to effectively improve the cycle life of lithium iron manganese phosphate batteries.
Please refer to Table 1. Comparative Examples 1 to 7 show that as the content of ethylene carbonate increases, the capacity retention rate at room temperature and high temperature first increases and then decreases. When ethylene carbonate accounts for 30 wt % of the non-aqueous solvent, the capacity retention rate is the highest, which shows that as the content of dimethyl carbonate increases, the dynamics performance of the lithium-ion battery improves, but when the content of dimethyl carbonate is too much, the oxidation stability of the electrolyte becomes poor, causing rapid capacity decay. Therefore, it is necessary to control the amount of the ethylene carbonate to ensure the performance of lithium-ion battery.
Please refer to Table 1. Comparing Example 1 with Examples 8 to 13, it can be seen that as the content of positive electrode additive PS increases, the capacity retention rate after cycles first increases and then decreases, and the capacity retention rate after cycles at normal temperature and the capacity retention rate after cycles at high temperatures change synchronously. When the content of PS is 3 wt %, the comprehensive performance of the lithium-ion battery is the optimal, which shows that as the content of PS increases, a dense CEI film may be formed on the positive electrode to prevent the oxidative decomposition of the electrolyte. However, if the content of PS is too high, the CEI film will be too thick, resulting in an increase in the interface resistance of the positive electrode, resulting in reduction of dynamics performance and cycle life of the lithium-ion battery.
Please refer to Table 1. Comparing Example 1 with Examples 14 to 19, it can be seen that as the content of negative electrode additive VC increases, the capacity retention rate after cycles first increases and then decreases. When the of content VC is between 0.5 wt % and 3 wt %, the comprehensive performance of lithium-ion battery reaches the optimal level, which shows that as the content of VC increases, a dense SEI film may be formed on the negative electrode, and the SEI film may be continuously repaired during the cycles, thus reducing the damage to the SEI film of the negative electrode caused by the dissolution of manganese ions, so as to effectively improve the cycle life of lithium manganese iron phosphate batteries. In the meantime, it is possible to prevent problems such as SEI damage or excessive impedance that occurs when the content of VC is too high or too low. That is, by adding ethylene carbonate, PS and VC to the electrolyte and controlling the content thereof, it is possible to improve the performance of lithium iron manganese phosphate batteries and enhance the cycle performance of the battery.
In summary, the present disclosure provides a lithium-ion battery and an application thereof. By selecting the ingredients of the non-aqueous solvent, the conductivity of the electrolyte may be improved, the oxidation stability of the electrolyte may be ensured, the dynamics performance of the lithium-ion battery may be enhanced, and the cycle performance may be improved. By controlling the positive electrode additives and the content thereof, a dense CEI film may be formed on the surface of the positive electrode to reduce oxidative decomposition of the electrolyte. By controlling the negative electrode additives and the content thereof, a dense SEI film may be formed on the negative electrode, and the SEI film may be continuously repaired during the cycles, thereby reducing the damage to the negative electrode SEI film caused by dissolution of manganese ion, and effectively improving the cycle life of lithium manganese iron phosphate batteries. By controlling the type and content of solvents, positive electrode additives, and negative electrode additives, it is possible to improve the stability of the electrolyte, enhance the cycle performance of the lithium-ion battery, and improve the performance of the lithium-ion battery at high temperatures.
The above description is only a preferred embodiment of the present disclosure and an explanation of the technical principles used. Those skilled in the art should understand that the scope of the disclosure involved in the present disclosure is not limited to technical solutions formed by specific combinations of the above technical features, and should also cover other technical solutions formed by any combination of the above technical features or their equivalent features without departing from the inventive concept, such as a technical solution formed by replacing the above features with technical features disclosed in this disclosure (but not limited to) with similar functions.
Except for the technical features described in the description, the remaining technical features are known to those skilled in the art. In order to highlight the innovative features of the present disclosure, the remaining technical features will not be described in detail here.
| Number | Date | Country | Kind |
|---|---|---|---|
| 202310858153.9 | Jul 2023 | CN | national |
