The present disclosure relates to the field of battery technologies, and in particular, to a cobalt-free and nickel-free positive electrode material and a preparation method therefor, and a battery.
With the development of the new energy market, ternary positive electrode materials have attracted a lot of attention due to their high energy density, high cycle, and high safety. In the current power market, large-scale commercial ternary materials such as NCM523 and NCM622 meet the requirements of hybrid vehicles to some extent, but the endurance mileage and safety performance of the hybrid vehicles still need to be improved. Moreover, the prices of cobalt and nickel elements in NCM continue to rise, which restrains the costs of batteries. In addition, the cobalt metal easily causes harm to the environment.
The following is the summary of subject matters detailed in the present disclosure. The summary is not intended to limit the present disclosure, but provides a cobalt-free and nickel-free positive electrode material and a preparation method therefor, and a battery.
The present disclosure provides a preparation method for a cobalt-free and nickel-free positive electrode material in one embodiment, including: preparing a cobalt-free and nickel-free matrix material, and mixing the cobalt-free and nickel-free matrix material, a lithium source, and a divalent manganese compound for reaction to obtain the cobalt-free and nickel-free positive electrode material.
In one embodiment provided by the present disclosure, the divalent manganese compound is added in the preparation process to inhibit the generation of lamellar LiMnO2 and spinel LiMn2O4, promote the generation of Li2MnO3, and effectively avoid the occurrence of disproportionation reaction in the presence of Mn3+ and the Jahn-Teller effect in the presence of LiMn2O4 during charging and discharging in a cycling process, where the lamellar LiMnO2 and spinel LiMn2O4 will result in capacity loss and poor material cycle, while the lamellar Li2MnO3 can effectively improve the cycle performance, so the preparation method has the characteristics of simple preparation process, low cost, low pollution, and high cycle performance.
In one embodiment provided by the present disclosure, a general formula of the cobalt-free and nickel-free matrix material is NaxLiyMn0.75O2, where 0.8≤x≤1, and 0≤y≤0.35, for example, x is 0.80, 0.82, 0.84, 0.86, 0.88, 0.90, 0.92, 0.94, 0.96, 0.98, or 1.00, and y is 0, 0.03, 0.06, 0.09, 0.12, 0.15, 0.18, 0.21, 0.24, 0.27, 0.30, 0.33, or 0.35.
In one embodiment, the lithium source includes one of or a combination of at least two of lithium carbonate, lithium hydroxide, lithium chloride, or lithium fluoride.
In one embodiment, a preparation method for the cobalt-free and nickel-free matrix material includes: mixing a lithium salt, a manganese salt, and a sodium salt, where a molar ratio of lithium in the lithium salt, sodium in the sodium salt, and manganese in the manganese salt is (0.2-0.3): (0.9-1.1): (0.65-0.85); and heating the mixture to obtain the cobalt-free and nickel-free matrix material, where the molar ratio of lithium in the lithium salt, sodium in the sodium salt, and manganese in the manganese salt is, for example, 0.2:0.9: 0.65, 0.2:1:0.75, 0.25:1.1:0.85, 0.25:0.95 0.8, or 0.3:1.1:0.85.
In one embodiment, the lithium salt includes one of or a combination of at least two of lithium carbonate, lithium hydroxide, lithium chloride, or lithium fluoride.
In one embodiment, the manganese salt includes one of or a combination of at least two of manganese acetate, manganese carbonate, manganese oxide, manganese dioxide, or manganese tetroxide.
In one embodiment, the sodium salt includes one of or a combination of at least two of sodium carbonate, sodium acetate, sodium chloride, or sodium bicarbonate.
In one embodiment, the heating in the preparation method for the cobalt-free and nickel-free matrix material is performed in an oxygen-containing atmosphere, where the oxygen-containing atmosphere is an air atmosphere with a flow rate of 5-10 L/min, for example, the flow rate is 5.0 L/min, 5.5 L/min, 6.0 L/min, 6.5 L/min, 7.0 L/min, 7.5 L/min, 8.0 L/min, 8.5 L/min, 9.0 L/min, 9.5 L/min, or 10.0 L/min; a temperature of the heating in the preparation method for the cobalt-free and nickel-free matrix material is 500-800° C., for example, the temperature is 500° C., 520° C., 540° C., 560° C., 580° C., 600° C., 620° C., 640° C., 660° C., 680° C., 700° C., 720° C., 740° C., 760° C., 780° C., or 800° C.; and time for the heating is 8-12 h, for example, the time is 8.0 h, 8.4 h, 8.8 h, 9.2 h, 9.6 h, 10.0 h, 10.4 h, 10.8 h, 11.2 h, 11.6 h, or 12.0 h.
In one embodiment provided by the present disclosure, the cobalt-free and nickel-free matrix material, the divalent manganese compound, and the lithium source are mixed to obtain a mixture, and a molar ratio of lithium to manganese in the mixture is (0.8-1.5): 1, for example, the molar ratio is 0.8:1, 0.9:1, 1.0: 1, 1.1:1, 1.2:1, 1.3:1, 1.4:1, or 1.5:1.
In one embodiment, by controlling the addition amount of the divalent manganese compound, after the cobalt-free and nickel-free matrix material, the divalent manganese compound, and the lithium source are mixed to obtain a mixture, the molar ratio of lithium to manganese in the mixture is (0.8-1.5): 1, which effectively inhibits the formation of lamellar LiMnO2, thereby improving the cycle performance of a battery; if the molar ratio of lithium to manganese is less than 0.8:1, excessive lithium-deficient materials, such as spinel structures, will be formed, resulting in low capacity; and if the molar ratio of lithium to manganese is more than 1.5:1, cost waste will be caused, and the total alkali content of the material is too high to affect the performance of the material.
In one embodiment provided by the present disclosure, the divalent manganese compound includes one of or a combination of at least two of MnO, Mn3O4, or MnCO3.
In one embodiment, the divalent manganese compound includes a compound containing divalent manganese, such as Mn3O4, and also includes divalent manganese and trivalent manganese.
In one embodiment provided by the present disclosure, the mixing reaction is a melting reaction; a temperature of the mixing reaction is 400-800° C., for example, the temperature is 400° C., 440° C., 480° C., 520° C., 560° C., 600° C., 640° C., 680° C., 720° C., 760° C., or 800° C.; and time for the mixing reaction is 4-8 h, for example, 4.0 h, 4.4 h, 4.8 h, 5.2 h, 5.6 h, 6.0 h, 6.4 h, 6.8 h, 7.2 h, 7.6 h, or 8.0 h.
In one embodiment, the material is sequentially washed and dried after the mixing reaction.
In one embodiment, the washing step includes: adding water to the material after reaction and washing the material for 10 min while stirring, where a mass of the added water is twice that of the material.
In one embodiment, the washing is to remove residual raw materials from the material after reaction. Excessive lithium salt is added in the preparation process, resulting in high residual alkali content of the material. In addition, the sodium salt formed in the calcination process is inactive. Therefore, the washing treatment is performed to remove the sodium salt and the residual alkali from the material.
In one embodiment provided by the present disclosure, the cobalt-free and nickel-free positive electrode material obtained after the mixing reaction is further coated, and a method for the coating includes the following steps: mixing the cobalt-free and nickel-free positive electrode material obtained by the reaction with AlPO4, and performing primary calcination to obtain an AlPO4-coated positive electrode material; and mixing the AlPO4-coated positive electrode material with TiO2, and performing secondary calcination to obtain an AlPO4- and TiO2-coated cobalt-free and nickel-free positive electrode material.
In one embodiment, double-layer coating with AlPO4 and TiO2 is performed, with TiO2 as an outer coating. In the coating process, TiO2 binds to Li+ diffused from the active material to generate Li2TiO3, which is a lithium ion conductor. The Li2TiO3 generated on the surface can improve the diffusion rate of ions. In addition, AlPO4 serves as an inner coating, Al3+ diffuses into oxide lattices in the cycling process to stabilize the structure, and PO43− interacts with Li+ to generate a good lithium ion conductor Li3PO4.
In one embodiment, a temperature of the primary calcination is 300-800° C., for example, the temperature is 300° C., 350° C., 400° C., 450° C., 500° C., 550° C., 600° C., 650° C., 700° C., 750° C., or 800° C.; time for the primary calcination is 5-8 h, for example, the time is 5.0 h, 5.3 h, 5.6 h, 5.9 h, 6.2 h, 6.5 h, 6.8 h, 7.1 h, 7.4 h, 7.7 h, or 8.0 h; and an atmosphere for the primary calcination is air or oxygen.
In one embodiment, a temperature of the secondary calcination is 300-800° C., for example, the temperature is 300° C., 350° C., 400° C., 450° C., 500° C., 550° C., 600° C., 650° C., 700° C., 750° C., or 800° C.; time for the secondary calcination is 5-8 h, for example, the time is 5.0 h, 5.3 h, 5.6 h, 5.9 h, 6.2 h, 6.5 h, 6.8 h, 7.1 h, 7.4 h, 7.7 h, or 8.0 h; and an atmosphere for the secondary calcination is air or oxygen.
In one embodiment provided by the present disclosure, based on a total mass of the cobalt-free and nickel-free positive electrode material, a coating amount of the AlPO4 is 500-5000 ppm, for example, the coating amount is 500 ppm, 1000 ppm, 1500 ppm, 2000 ppm, 2500 ppm, 3000 ppm, 3500 ppm, 4000 ppm, 4500 ppm, or 5000 ppm.
In one embodiment, the coating amount of the AlPO4 is controlled to 500-5000 ppm. If the coating amount is less than 500 ppm, problems of uneven material coating and thin coating are caused, and the effect of isolation from an electrolytic solution is poor, which increases side reactions, so that the electrical performance of the battery is poor. If the coating amount is more than 5000 ppm, the coating of the material is too thick, which hinders the intercalation and deintercalation of Li+, thereby affecting the capacity and rate performance of the material.
In one embodiment, based on the total mass of the cobalt-free and nickel-free positive electrode material, a coating amount of the TiO2 is 500-5000 ppm, for example, the coating amount is 500 ppm, 1000 ppm, 1500 ppm, 2000 ppm, 2500 ppm, 3000 ppm, 3500 ppm, 4000 ppm, 4500 ppm, or 5000 ppm.
In one embodiment, the coating amount of the TiO2 is controlled to 500-5000 ppm. If the coating amount is less than 500 ppm, problems of uneven material coating and thin coating are caused, and the effect of isolation from the electrolytic solution is poor, which increases side reactions, so that the electrical performance of the battery is poor. If the coating amount is more than 5000 ppm, the coating of the material is too thick, which hinders the intercalation and deintercalation of Lit, thereby affecting the capacity and rate performance of the material.
In one embodiment, the preparation method specifically includes the following steps:
In one embodiment of the present disclosure, a cobalt-free and nickel-free positive electrode material is provided, including lamellar LiMnO3, spinel LiMn2O4, and lamellar Li2MnO3.
In one embodiment, a typical but non-limiting chemical formula of the cobalt-free and nickel-free positive electrode material is Li a MnbO2, where 0.8≤a≤1, and 0.7≤b≤0.8, for example, a is 0.80, 0.82, 0.84, 0.86, 0.88, 0.90, 0.92, 0.94, 0.96, 0.98, or 1.00, and b is 0.70, 0.71, 0.72, 0.73, 0.74, 0.75, 0.76, 0.77, 0.78, 0.79, or 0.80.
In one embodiment provided by the present disclosure, a molar ratio of the lamellar Li2MnO3 in the cobalt-free and nickel-free positive electrode material is 50-90%, such as 50%, 55%, 60%, 65%, 70%, 75%, 80%, 85%, or 90%.
In one embodiment provided by the present disclosure, the molar ratio of the lamellar Li2MnO3 in the cobalt-free and nickel-free positive electrode material is 70%.
In one embodiment provided by the present disclosure, a battery is provided, including a positive electrode, a negative electrode, and a separator, where the cobalt-free and nickel-free positive electrode material described in the foregoing embodiment is used in the positive electrode.
The accompanying drawings are used to provide a further understanding of the technical solutions of the present disclosure, constitute a part of the specification, are used together with the embodiments of the present application to explain the technical solutions of the present disclosure, and do not constitute limitations on the technical solutions of the present disclosure.
The technical solutions of the present disclosure will be further illustrated below with reference to the accompanying drawings and through specific examples.
A preparation method for a cobalt-free and nickel-free positive electrode material included the following steps:
A chemical formula of the cobalt-free and nickel-free positive electrode material prepared in this example was Li0.92Mn0.76O2, where a molar ratio of lamellar Li2MnO3 was 70%.
It can be seen from
A preparation method for a cobalt-free and nickel-free positive electrode material included the following steps:
A chemical formula of the cobalt-free and nickel-free positive electrode material prepared in this example was Li0.8Mn0.89O2, where a molar ratio of lamellar Li2MnO3 was 50%.
A preparation method for a cobalt-free and nickel-free positive electrode material included the following steps:
A chemical formula of the cobalt-free and nickel-free positive electrode material prepared in this example was Li1.05Mn0.7O2, where a molar ratio of lamellar Li2MnO3 was 87.5%.
A preparation method for a cobalt-free and nickel-free positive electrode material included the following steps:
A chemical formula of the cobalt-free and nickel-free positive electrode material prepared in this example was Li0.8Mn0.8O2, where a molar ratio of lamellar Li2MnO3 was 55%.
A preparation method for a cobalt-free and nickel-free positive electrode material included the following steps:
A chemical formula of the cobalt-free and nickel-free positive electrode material prepared in this example was Li0.98Mn0.75O2, where a molar ratio of lamellar Li2MnO3 was 78%.
Different from Example 1, the molar ratio of lithium to manganese in step (II) was changed to 0.6:1. A chemical formula of the prepared cobalt-free and nickel-free positive electrode material was Li0.5Mn0.83O2, where lamellar Li2MnO3 was not included.
Different from Example 1, the molar ratio of lithium to manganese in step (II) was changed to 1.7:1. A chemical formula of the prepared cobalt-free and nickel-free positive electrode material was Li1.2 Mn0.7O2, where a molar ratio of lamellar Li2MnO3 was 94%.
Different from Example 1, step (III) was not performed, that is, AlPO4 coating and TiO2 coating were not performed.
Different from Example 1, AlPO4 coating was not performed in step (III).
Different from Example 1, TiO2 coating was not performed in step (III).
Different from Example 1, the coating amount of AlPO4 was changed to 300 ppm and the coating amount of TiO2 was changed to 300 ppm in step (III).
Different from Example 1, the coating amount of AlPO4 was changed to 6000 ppm and the coating amount of TiO2 was changed to 6000 ppm in step (III).
Different from Example 1, MnO was not added in step (II). In the prepared cobalt-free and nickel-free positive electrode material, a molar ratio of lamellar Li2MnO3 was 20%.
Different from Example 1, MnO was replaced with MnO 2 in step (II). In the prepared cobalt-free and nickel-free positive electrode material, a molar ratio of lamellar Li2MnO3 was 25%.
The cobalt-free and nickel-free positive electrode material prepared in the examples and comparative examples provided in the present disclosure was assembled into a battery: an appropriate amount of material was coated with slurry uniformly, where the cobalt-free and nickel-free positive electrode material: Sp: PVDF gel=92:4:4, and the solid content of the PVDF gel was 6.05%; and the prepared electrode plate was assembled with a CR2032 shell to form a button battery, where Sp represented conductive carbon black, PVDF represented polyvinylidene fluoride, and CR2032 shell represented a cylindrical shell having a diameter of 20 mm and a height of 3.2 mm.
The obtained button battery was tested for cycle performance at a voltage of 2-4.6 V. The test results were shown in Table 1.
It can be seen by comparing Example 1 with Examples 6 and 7 that, by controlling the addition amount of the divalent manganese compound, after the cobalt-free and nickel-free matrix material, the divalent manganese compound, and the lithium source were mixed, the molar ratio of lithium to manganese was (0.8-1.5):1, which effectively inhibited the formation of lamellar LiMnO2, thereby improving the cycle performance of the battery; if the molar ratio of lithium to manganese was less than 0.8:1, excessive lithium-deficient materials, such as spinel structures, will be formed, resulting in low capacity; and if the molar ratio of lithium to manganese was more than 1.5:1, cost waste will be caused, and the total alkali content of the material was too high to affect the performance of the material.
It can be seen by comparing Example 1 with Examples 8, 9, and 10 that, through double-layer coating with TiO2 as an outer coating, TiO2 bound to Li′ diffused from the active material in the coating process to generate Li2TiO3, which was a lithium ion conductor; the Li2TiO3 generated on the surface can improve the diffusion rate of ions; and AlPO4 served as an inner coating, Al3+ diffused into oxide lattices in the cycling process to stabilize the structure, and PO43− interacted with Li+ to generate a good lithium ion conductor Li3PO4.
It can be seen by comparing Example 1 with Examples 11 and 12 that the coating amount of the AlPO4 was controlled to 500-5000 ppm; if the coating amount was less than 500 ppm, problems of uneven material coating and thin coating were caused, and the effect of isolation from an electrolytic solution was poor, which increased side reactions, so that the electrical performance of the battery was poor; and if the coating amount is more than 5000 ppm, the coating of the material was too thick, which hindered the intercalation and deintercalation of Lit, thereby affecting the capacity and rate performance of the material.
It can be seen by comparing Example 1 with Comparative Examples 1 and 2 that, in combination with
Number | Date | Country | Kind |
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202110621709.3 | Jun 2021 | CN | national |
Number | Date | Country | |
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Parent | PCT/CN2021/130207 | Nov 2021 | US |
Child | 18527378 | US |