A modified ternary cathode material and its preparation method and application
By coating the ternary positive electrode material with cobalt hydroxide and low-temperature oxygen plasma treatment, an aluminum hydroxide/poly(TA) composite layer was constructed, which solved the problem of poor lithium diffusion and ionic conductivity of the ternary positive electrode material at low temperatures, and achieved high-performance low-temperature large-scale charge and discharge.
Patent Information
- Application Number
- CN202411368379.1
- Authority / Receiving Office
- CN · China
- Patent Type
- Patents(China)
- Current Assignee / Owner
- Filing Date
- 2024-09-29
- Publication Date
- 2025-09-02
- Estimated Expiration
- 2044-09-29
AI Technical Summary
The existing ternary positive electrode materials have poor lithium diffusion and ionic conductivity under low temperature conditions, resulting in poor battery power performance and increased internal polarization resistance of lithium-ion batteries, limiting their application at low temperatures.
By performing cobalt hydroxide coating and dopant treatment on the ternary precursor, combined with low-temperature oxygen plasma surface treatment and polymerization reaction, an aluminum hydroxide/poly(TA) composite layer coated ternary positive electrode material is constructed to optimize particle size and interface structure, and improve lithium diffusion and ionic conductivity.
Under low temperature conditions, the lithium diffusion and ionic conductivity of lithium-ion batteries are significantly improved, the polarization internal resistance is reduced, and the excellent large-scale charge and discharge performance is shown.
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Abstract
Description
Technical Field
[0001] The present invention belongs to the field of lithium-ion batteries, and in particular relates to a modified ternary cathode material and a preparation method and application thereof. Background Art
[0002] In the era of electric vehicles (EVs), lithium-ion batteries (LIBs) play a vital role. x Co y M 1-x-y (OH)2 cathode materials are the primary cathode materials for future electric vehicle batteries. However, with the rapid expansion of the electric vehicle market, issues related to electric vehicles are becoming increasingly prominent. One of the most serious issues is the battery's poor power performance at low temperatures (<-5°C), resulting in prolonged charging times at low temperatures.
[0003] To improve low-temperature power performance of batteries, researchers have long sought to increase the Ni content and reduce the Co content in cathode materials, while also modifying them with heterogeneous doping elements. However, the low lithium diffusion coefficient and poor reaction kinetics of common intercalation-based composite cathodes limit their power performance at low temperatures, further restricting their widespread application at low temperatures.
[0004] Therefore, it is urgent to develop a Ni x Co y M 1-x-y (OH)2 ternary positive electrode material has high lithium diffusivity and ionic conductivity under low temperature conditions. The polarization internal resistance of the lithium-ion battery used in it does not increase significantly, and it exhibits excellent high-rate charge and discharge performance. Summary of the Invention
[0005] In order to solve the technical problems of poor lithium diffusion and ionic conductivity of the above-mentioned positive electrode materials under low temperature conditions, as well as the significant increase in polarization internal resistance of the lithium-ion batteries used, and poor high-rate charge and discharge performance, the present invention provides a preparation method and application of high-performance modified ternary positive electrode materials.
[0006] In order to solve the above technical problems, the present invention adopts the following technical solutions:
[0007] In a first aspect, the present invention provides a method for preparing a high-performance modified ternary cathode material.
[0008] The method for preparing the high-performance modified ternary cathode material provided by the present invention comprises the following steps:
[0009] 1) mixing a ternary precursor, a cobalt hydroxide-coated ternary precursor, a dopant, and a lithium source, and sintering the mixed material to prepare an intermediate sample of a ternary positive electrode material;
[0010] 2) coating the surface of the intermediate sample of the ternary cathode material in step 1 with aluminum hydroxide, then reacting it with lipoic acid (TA) in the first step, and then adding solvent I to carry out the second step reaction to obtain an aluminum hydroxide / poly (TA) composite layer coated ternary cathode material; the solvent I is selected from at least one of dichloromethane, methanol, and chloroform;
[0011] 3) subjecting the aluminum hydroxide / poly (TA) composite layer coated ternary cathode material described in step 2 to a low-temperature oxygen plasma surface treatment to obtain a modified aluminum hydroxide / poly (TA) composite layer coated ternary cathode material;
[0012] 4) The modified aluminum hydroxide layer and the poly (TA) film layer composite layer coated ternary positive electrode material described in step 3 are polymerized with diisocyanate and α, ω-diisocyanate polyethylene glycol to obtain a polyurea-modified aluminum hydroxide / poly (TA) composite layer coated modified ternary positive electrode material, which is the modified ternary positive electrode material.
[0013] In step 1 of the above method, preferably, the chemical formula of the ternary precursor is Ni x Co y M 1-x-y (OH)2, wherein 0<x<1, 0<y<1, 1-xy>0, M is at least one of Mn, Al,
[0014] According to one embodiment of the present invention, the chemical formula of the ternary precursor is Ni 0.7 Co 0.1 Al 0.2 (OH)2;
[0015] According to one embodiment of the present invention, the chemical formula of the ternary precursor is Ni 0.8 Co 0.1 Mn 0.1 (OH)2;
[0016] According to one embodiment of the present invention, the chemical formula of the ternary precursor is Ni 0.9 Co 0.02 Mn 0.08 (OH)2;
[0017] According to one embodiment of the present invention, the chemical formula of the ternary precursor is Ni 0.6 Co 0.2 Mn 0.2 (OH)2.
[0018] In step 1 of the above method, preferably, the lithium source is at least one of lithium hydroxide, lithium perchlorate, lithium hexafluorophosphate, and lithium carbonate; preferably, the dopant is at least one of tungstic acid, tungsten oxide, strontium carbonate, strontium oxide, aluminum oxide, zirconium oxide, niobium oxide, boric acid, vanadium dioxide, and molybdenum trioxide.
[0019] In step 1 of the above method, preferably, the particle size of the ternary precursor is in the range of 1.2 to 9 μm; preferably, the particle size of the cobalt hydroxide-coated ternary precursor is in the range of 1.3 to 6.8 μm.
[0020] In step 1 of the above method, preferably, the preparation method of the cobalt hydroxide-coated ternary precursor comprises the following steps: taking the ternary precursor dust collection material and the coating agent I and adding them to a stirred reactor filled with deionized water, stirring and mixing at 100-300 r / min for 20-120 min to obtain slurry I, then adding the precipitant I to the slurry I to adjust the pH value to 9-11, aging at 30-65 ° C for 4-16 h, and then filtering, washing, and drying to obtain a coated precursor;
[0021] More preferably, the coating agent I is cobalt sulfate; more preferably, the mass ratio of the ternary precursor dust collecting material, coating agent I, and deionized water is 1:0.01~0.05:3~5; more preferably, the precipitant I is ammonia water and / or sodium hydroxide.
[0022] In the above method, the ternary precursor dust material is the dust material collected during the ternary precursor feeding process. Preferably, the particle size of the precursor dust material ranges from 1.2 to 6.4 μm.
[0023] In step 1 of the above method, preferably, the mass ratio of the ternary precursor, the cobalt hydroxide-coated ternary precursor, the dopant, and the lithium source is (0.3-1):3:(0.0001-0.012):(1.43-1.92).
[0024] In step 1 of the above method, preferably, the sintering is carried out in a kiln, and the internal pressure of the kiln is set to 200-500 Pa during the sintering; the sintering temperature is 700-950° C., and the sintering time is 10-30 hours.
[0025] In step 1 of the above method, preferably, the total number of particles W1 with a particle size of 1.2 to 2.9 μm in the intermediate sample of the ternary positive electrode material accounts for 20.8 to 31.2% of the total number of particles W0; the particle ratio here is tested using a Malvern MS3000 laser particle size analyzer to determine the particle size range of different particle sizes, and the target particle size ratio range is determined by the particle size test results of the MS3000.
[0026] Preferably, the particle size distribution dispersion of the intermediate sample of the ternary positive electrode material is 2.4 to 4;
[0027] Preferably, the mass proportion of lithium hydroxide in the residual alkali (LiOH and Li2CO3) in the intermediate sample of the ternary positive electrode material is 0.1-0.25%, and the mass proportion of lithium carbonate is 0.1-0.2%.
[0028] In step 2 of the above method, preferably, the aluminum hydroxide coating method comprises the following steps: adding the intermediate sample of the ternary positive electrode material and the coating agent II to a stirred reactor filled with deionized water, stirring and mixing at 400-800 r / min for 60-120 min to obtain slurry II, then adding a precipitant II to the slurry II to adjust the pH value to 9-11, aging at 40-75° C. for 2-12 h, and then filtering, washing, and drying to obtain the slurry;
[0029] More preferably, the coating agent II is aluminum sulfate; more preferably, the mass ratio of the intermediate sample of the ternary positive electrode material, the coating agent II, and deionized water is 1:0.03~0.06:5~8; more preferably, the precipitant II is ammonia water and / or sodium hydroxide.
[0030] In step 2 of the above method, preferably, the mass ratio of the aluminum hydroxide-coated ternary positive electrode material, thioctic acid (TA), and solvent I is (2066.46~25756.94): (3.6~25.76):1; specifically 3066.46:6.8:1, 18062.2:16.8:1, 2066.46:3.6:1, 4078.12:13.6:1, or 25756.94:25.76:1.
[0031] More preferably, the reaction temperature of the first step reaction is 100-120° C., the stirring speed is 50-100 r / min, and the stirring reaction time is 2-6 h; more preferably, the stirring reaction time of the second step reaction is 30-60 min.
[0032] In step 3 of the above method, preferably, the low-temperature oxygen plasma surface treatment is carried out in a low-temperature plasma surface treatment machine. Before treatment, the low-temperature plasma surface treatment machine needs to be evacuated, and then a certain amount of oxygen is introduced into the treatment machine to reach the required treatment pressure; more preferably, the vacuum degree of the evacuation is 5 to 10 Pa; more preferably, the treatment pressure is 20 to 100 Pa.
[0033] In step 3 of the above method, preferably, the step of low-temperature oxygen plasma surface treatment is: setting the frequency of the low-temperature oxygen plasma surface treatment machine to 10-40 Hz, setting the input power to 200-800 W, fixing the spray gun nozzle to 10-15 mm from the sample, and using a bow-shaped reciprocating treatment for 5-25 seconds.
[0034] In step 4 of the above method, preferably, the polymerization is carried out in a reaction solution, wherein the reaction solution is obtained by stirring and mixing the diisocyanate, the α,ω-diisocyanate polyethylene glycol and the solvent II in a mass ratio of 1:0.21 to 0.34:0.5;
[0035] More preferably, the α,ω-diisocyanate polyethylene glycol has the following structural formula: 500≤n≤1000;
[0036] More preferably, the diisocyanate is at least one of toluene diisocyanate, diphenylmethane diisocyanate, and 1,5-naphthalene diisocyanate;
[0037] More preferably, the solvent II is acetone and / or N,N-dimethylformamide.
[0038] More preferably, the mass ratio of the modified aluminum hydroxide / poly (TA) composite layer coated ternary positive electrode material to the reaction solution is 1:0.17-0.24.
[0039] In step 4 of the above method, the polymerization reaction is a two-step temperature polymerization, that is, a stirring reaction is first performed, and then a second stirring reaction is performed after the reaction temperature is lowered; preferably, the first stirring reaction and the second stirring reaction are both performed in a coulter dryer.
[0040] More preferably, the primary stirring reaction is to maintain the internal temperature of the coulter dryer cavity at 110-130°C through a heat transfer medium, set the spindle speed to 100-200r / min, and the reaction time is 30-60min; more preferably, the secondary stirring reaction is to maintain the internal temperature of the coulter dryer cavity at 30-50°C through a heat transfer medium, set the spindle speed to 50-100r / min, and the reaction time is 1-2h.
[0041] In a second aspect, the present invention also protects the high-performance modified ternary positive electrode material prepared by the above method.
[0042] In a third aspect, the present invention also protects the application of the high-performance modified ternary positive electrode material prepared by the above method.
[0043] The application is the application of the high-performance modified ternary positive electrode material in the preparation of lithium-ion batteries.
[0044] In a fourth aspect, the present invention protects a lithium-ion battery.
[0045] The lithium-ion battery comprises a positive electrode, a negative electrode, a separator and an electrolyte, and the material of the positive electrode comprises the above-mentioned high-performance modified ternary positive electrode material.
[0046] Compared with the prior art, the present invention has the following beneficial effects:
[0047] 1) The present invention coats the dust collected during the precursor feeding process with cobalt hydroxide, and then mixes it with the uncollected precursor, dopant, and lithium source in a certain proportion, and sintering in one step to obtain an intermediate sample of the ternary positive electrode material. In the above preparation method, the present invention coats the dust precursor with cobalt hydroxide. The doping of cobalt during the sintering process can effectively promote the growth of the primary particles of the dust precursor. The high furnace pressure sintering conditions and the synergistic effect of the dopant are then set to allow the small and medium particles (particles with a particle size of 1.2 to 2.9 μm) of the intermediate sample of the prepared ternary positive electrode material to account for 20.8 to 31.2%. The mixing of large and small primary particles synergistically balances the electrochemical reaction differences of the primary particles of the intermediate sample of the ternary positive electrode material, and effectively inhibits the cation reduction of the transition metal layer.
[0048] 2) The present invention selectively uses solvents such as dichloromethane, methanol, and chloroform, and adopts a heating and stirring method to simply and effectively construct a layer of poly (TA) film on the surface of the intermediate sample of the ternary positive electrode material. By selecting the reaction solvent, the constructed poly (TA) film layer has excellent flexibility and ductility under high and low temperature environments, which can effectively reduce interfacial side reactions and improve the lithium diffusion and ionic conductivity of the material under low temperature conditions.
[0049] 3) The present invention constructs a hydroxyl group-modified aluminum hydroxide layer outside the poly (TA) film layer through hydrolysis and low-temperature oxygen plasma modification technology. This modified aluminum hydroxide layer is combined with the poly (TA) film layer to effectively slow down the precipitation of lattice oxygen under long-cycle conditions of the ternary positive electrode material to produce NiO phase and oxygen-containing byproduct Li2O, effectively improving the long-cycle performance of the lithium-ion battery used in the application under high and low temperature conditions.
[0050] 4) In addition, the present invention also prepares a polyurea-modified aluminum hydroxide / poly (TA) composite layer-coated modified ternary positive electrode material by coating a ternary positive electrode material with a composite layer of modified aluminum hydroxide layer and poly (TA) film layer with diisocyanate and α, ω-diisocyanate-based polyethylene glycol twice at a stepped temperature. The addition of diisocyanate and α, ω-diisocyanate-based polyethylene glycol and the synergistic effect of the two stepped temperature polymerizations reduce the rigidity of the polyurea chain segment, effectively improve the lithium diffusivity and ionic conductivity of the material under low temperature conditions, and the polarization internal resistance of the applied lithium-ion battery does not increase significantly, showing excellent high-rate charge and discharge performance. BRIEF DESCRIPTION OF THE DRAWINGS
[0051] Figure 1 This is a microscopic morphology image of Example 1 at 10,000 times magnification;
[0052] Figure 2 This is a microscopic morphology image of comparative example 1 magnified 10,000 times. DETAILED DESCRIPTION
[0053] The present invention will be further described in detail below in conjunction with specific embodiments. The examples provided are only for illustrating the present invention and are not intended to limit the scope of the present invention. The examples provided below can serve as a guide for further improvements by those skilled in the art and are not intended to limit the present invention in any way.
[0054] Unless otherwise specified, the experimental methods in the following examples are conventional methods and were performed according to the techniques or conditions described in the literature in the field or according to the product instructions. The materials and reagents used in the following examples, unless otherwise specified, were all commercially available.
[0055] The α,ω-diisocyanate polyethylene glycol used in the following examples has the following structural formula:
[0056] 500≤n≤1000.
[0057] The residual alkali test method in the following examples is as follows: weigh the sample according to the table below to an accuracy of 0.0001 g, place the weighed sample in a 100 mL beaker, add 50 mL of deionized water, place magnetic beads in the beaker and seal it with plastic wrap, then place the beaker on a magnetic stirrer and stir for about 10-15 minutes before removing it; let it stand for 5 minutes, filter it using a glass funnel, and the filtered clear liquid is the test solution.
[0058] Table 1 Residual alkali test method
[0059]
[0060] Accurately transfer the solution to be tested into a 100mL beaker, place a stirring rotor, control the sample volume to approximately 50mL (make up with water if less than 50mL), place the beaker on the magnetic stirrer of the automatic potentiometric titrator, add phenolphthalein dropwise for 2d, select HCl standard solution according to the table and titrate until it changes from red to colorless. The instrument will record the volume Ep1 (V1) of HCl standard solution consumed at the stoichiometric point and the pH; then add methyl orange dropwise for 2d, continue titrating until it changes from yellow to orange, and the instrument will record the volume Ep2 (V2) of HCl standard solution consumed at the stoichiometric point and the pH.
[0061] Analysis result calculation:
[0062] (1) When 2V1>V2, containing LiOH and Li2CO3, the calculation formula is as follows:
[0063]
[0064] (2) When 2V1<V2, it contains Li2CO3 and LiHCO3, and the calculation formula is as follows:
[0065]
[0066] (3) When 2V1=V2, only Li2CO3 is contained, and the calculation formula is as follows:
[0067]
[0068] In the above formula: c: concentration of HCl standard solution (mol / L); V1(Ep1): volume of HCl standard solution consumed at the first equivalence point (mL); V2(Ep2): volume of HCl standard solution consumed at the second equivalence point (including the first equivalence point) (mL); V': volume of the test solution (mL); V: volume of the sample (mL); 23.95: molar mass of LiOH (g / mol); 73.89: molar mass of Li2CO3 g / mol; 67.96: molar mass of LiHCO3 g / mol; m: mass of the sample (g).
[0069] Example 1
[0070] A method for preparing a high-performance modified ternary cathode material, the preparation steps of which are as follows:
[0071] 1. Preparation of intermediate samples of ternary cathode materials
[0072] (1) Preparation of cobalt hydroxide-coated ternary precursor:
[0073] Take the ternary precursor dust collection material Ni 0.7 Co 0.1 Mn 0.2 (OH)2 (particle size 1.2 ~ 6.4μm) and cobalt sulfate were added to a stirred reactor filled with deionized water, stirred at 300r / min for 20min to obtain slurry I, and then ammonia water was added to the slurry I to adjust the pH value to 9-11. The slurry was aged at 65℃ for 16h, and then filtered, washed and dried to obtain the cobalt hydroxide-coated precursor Co(OH)2-Ni 0.7 Co 0.1 Mn 0.2 (OH)2 (particle size 1.3 ~ 6.8μm); In the above preparation method, the precursor dust collecting material Ni 0.7 Co 0.1 Mn 0.2 The mass ratio of (OH)2, cobalt sulfate, and deionized water is 1:0.01:5;
[0074] (2) Preparation of intermediate samples of ternary cathode materials:
[0075] The ternary precursor Ni 0.7 Co 0.1 Mn0.2 (OH)2 (particle size 1.2 ~ 9μm), coated ternary precursor Co(OH)2-Ni 0.7 Co 0.1 Mn 0.2 (OH)2, tungstic acid, and lithium hydroxide were mixed in a mass ratio of 0.3:3:0.012:1.43. The mixture was sintered in a furnace at a pressure of 500 Pa and a temperature of 950°C for 10 hours. The mixture was then crushed and sieved to produce an intermediate sample of the ternary cathode material. The total number of particles (W1) with a particle size of 1.2-2.9 μm in the intermediate sample, representing 31.2% of the total number of particles (W0), was 31.2%. The particle size distribution dispersion ((D90-D10) / D50) was 4. The residual alkali in the resulting material consisted of 0.25% by weight of lithium hydroxide and 0.14% by weight of lithium carbonate. The residual alkali was determined by titration.
[0076] 2. Preparation of modified aluminum hydroxide / poly (TA) composite layer coated ternary positive electrode material
[0077] (1) Preparation of aluminum hydroxide coated ternary positive electrode material:
[0078] The intermediate sample of the ternary cathode material prepared in 1 and aluminum sulfate were added to a stirred reactor filled with deionized water, and stirred at 800 r / min for 120 min to obtain slurry II. Ammonia water was then added to the slurry II to adjust the pH value to 9-11, and the slurry was aged at 75°C for 5 h, and then filtered, washed, and dried to obtain slurry II. In the above preparation method, the mass ratio of the ternary cathode material, aluminum sulfate, and deionized water was 1:0.05:5.
[0079] (2) Preparation of aluminum hydroxide / poly (TA) composite layer coated ternary positive electrode material:
[0080] Aluminum hydroxide-coated ternary cathode material and thioctic acid (TA) were added to a reactor simultaneously, the reaction temperature was set at 105°C, the stirring speed was 80 r / min, and the reaction was stirred for 5.5 hours. Dichloromethane was then added and the stirring reaction was continued for 60 minutes before cooling to room temperature to obtain an aluminum hydroxide / poly (TA) composite layer coated ternary cathode material; in the above preparation method, the mass ratio of the aluminum hydroxide-coated ternary cathode material intermediate sample, thioctic acid (TA), and dichloromethane was 3066.46:6.8:1;
[0081] (3) Preparation of modified aluminum hydroxide / poly (TA) composite layer coated ternary positive electrode material
[0082] The low-temperature plasma surface treatment machine was evacuated to a vacuum degree of 10Pa, and then a certain amount of oxygen was introduced into the treatment machine to make the treatment pressure reach 24Pa, and an aluminum hydroxide / poly (TA) composite layer-coated ternary positive electrode material was added thereto for low-temperature oxygen plasma surface treatment to obtain a modified aluminum hydroxide / poly (TA) composite layer-coated ternary positive electrode material; in the above preparation method, the low-temperature oxygen plasma surface treatment step is: setting the frequency of the low-temperature oxygen plasma surface treatment machine to 19Hz, setting the input power to 560W, fixing the spray gun nozzle to 10mm away from the sample, and using a bow-shaped reciprocating treatment for 12s.
[0083] 3. Preparation of high-performance modified ternary cathode materials
[0084] The internal temperature of the coulter dryer cavity is maintained at 120°C by circulating heating oil, the main shaft speed is set to 120r / min, and the modified aluminum hydroxide / poly (TA) composite layer coated ternary positive electrode material is added to the reaction liquid and stirred for 60 minutes. Then, the internal temperature of the coulter dryer cavity is maintained at 42°C by reducing the circulating heating oil temperature, the main shaft speed is set to 82r / min, and the stirring reaction time is continued for 1.5 hours. After cooling to room temperature, it is sieved and demagnetized to obtain a polyurea modified aluminum hydroxide / poly (TA) composite layer coated ternary positive electrode material, which is the high-performance positive electrode material; in the above preparation method, the mass ratio of the modified aluminum hydroxide / poly (TA) composite layer coated ternary positive electrode material to the reaction liquid is 1:0.2; the reaction liquid is obtained by stirring and mixing toluene diisocyanate, α, ω-diisocyanate polyethylene glycol, and acetone in a mass ratio of 1:0.24:0.5.
[0085] Example 2
[0086] A method for preparing a high-performance modified ternary cathode material, the preparation steps of which are as follows:
[0087] 1. Preparation of intermediate samples of ternary cathode materials
[0088] (1) Preparation of cobalt hydroxide-coated ternary precursor:
[0089] Take the ternary precursor dust collection material Ni 0.7 Co 0.1 Al 0.2 (OH)2 (particle size 1.3 ~ 6μm) and cobalt sulfate were added to a stirred reactor filled with deionized water, stirred and mixed at 140r / min for 80min to obtain slurry I, and then ammonia water was added to the slurry I to adjust the pH value to 9-11, aged at 50℃ for 10h, and then filtered, washed and dried to obtain cobalt hydroxide-coated precursor Co(OH)2-Ni 0.7 Co 0.1 Al 0.2 (OH)2 (particle size 1.4 ~ 6.5μm); In the above preparation method, the precursor dust collecting material Ni0.7 Co 0.1 Al 0.2 The mass ratio of (OH)2, cobalt sulfate, and deionized water is 1:0.04:3;
[0090] (2) Preparation of intermediate samples of ternary cathode materials:
[0091] The ternary precursor Ni 0.7 Co 0.1 Al 0.2 (OH)2 (particle size 1.3 ~ 8μm), coated ternary precursor Co(OH)2-Ni 0.7 Co 0.1 Al 0.2 (OH)2, strontium carbonate, and lithium hexafluorophosphate are mixed in a mass ratio of 0.4:3:0.012:1.63. The internal pressure of the kiln is set to 300Pa and the temperature is set to 800℃. The mixed material is sintered for 15 hours, and then crushed and sieved to obtain an intermediate sample of the ternary positive electrode material. Among them, the total number of particles W1 with a particle size of 1.2 to 2.9μm in the intermediate sample of the ternary positive electrode material accounts for 21.4% of the total number of particles W0, and the particle size distribution dispersion is 3.2. In the residual alkali of the obtained material, the mass proportion of lithium hydroxide is 0.18%, and the mass proportion of lithium carbonate is 0.1%.
[0092] 2. Preparation of modified aluminum hydroxide / poly (TA) composite layer coated ternary positive electrode material
[0093] (1) Preparation of aluminum hydroxide coated ternary positive electrode material:
[0094] The intermediate sample of the ternary cathode material prepared in 1 and aluminum sulfate were added to a stirred reactor filled with deionized water, and stirred at 600 r / min for 80 min to obtain slurry II. Sodium hydroxide was then added to the slurry II to adjust the pH value to 9-11, and the slurry was aged at 62°C for 3.8 h, and then filtered, washed, and dried to obtain slurry II. In the above preparation method, the mass ratio of the ternary cathode material, aluminum sulfate, and deionized water was 1:0.04:6.5;
[0095] (2) Preparation of aluminum hydroxide / poly (TA) composite layer coated ternary positive electrode material:
[0096] Aluminum hydroxide-coated ternary cathode material and thioctic acid (TA) were added to a reactor simultaneously, the reaction temperature was set at 110°C, the stirring speed was 66 r / min, and the reaction was stirred for 2.5 hours. Methanol was then added and the stirring reaction was continued for 50 minutes before cooling to room temperature to obtain an aluminum hydroxide / poly (TA) composite layer coated ternary cathode material; in the above preparation method, the mass ratio of the aluminum hydroxide-coated ternary cathode material intermediate sample, thioctic acid (TA), and methanol was 18062.2:16.8:1;
[0097] (3) Preparation of modified aluminum hydroxide / poly (TA) composite layer coated ternary positive electrode material
[0098] The low-temperature plasma surface treatment machine was evacuated to a vacuum degree of 8 Pa, and then a certain amount of oxygen was introduced into the treatment machine to make the treatment pressure reach 60 Pa, and an aluminum hydroxide / poly (TA) composite layer-coated ternary positive electrode material was added thereto for low-temperature oxygen plasma surface treatment to obtain a modified aluminum hydroxide / poly (TA) composite layer-coated ternary positive electrode material; in the above preparation method, the low-temperature oxygen plasma surface treatment step is: setting the frequency of the low-temperature oxygen plasma surface treatment machine to 32 Hz, setting the input power to 660 W, fixing the spray gun nozzle to 12 mm from the sample, and using a bow-shaped reciprocating treatment for 10 s.
[0099] 3. Preparation of high-performance ternary cathode materials
[0100] The internal temperature of the coulter dryer cavity is maintained at 112°C by circulating heating oil, the main shaft speed is set to 105r / min, and the modified aluminum hydroxide / poly (TA) composite layer coated ternary positive electrode material is added to the reaction liquid and stirred for 40 minutes. Then, the internal temperature of the coulter dryer cavity is maintained at 45°C by reducing the temperature of the circulating heating oil, the main shaft speed is set to 90r / min, and the stirring reaction time is continued for 1.2 hours. After cooling to room temperature, the material is sieved and demagnetized to obtain a polyurea modified aluminum hydroxide / poly (TA) composite layer coated ternary positive electrode material, which is the high-performance positive electrode material. In the above preparation method, the mass ratio of the modified aluminum hydroxide / poly (TA) composite layer coated ternary positive electrode material to the reaction liquid is 1:0.22; the reaction liquid is obtained by stirring and mixing diphenylmethane diisocyanate, α,ω-diisocyanate polyethylene glycol, and N,N-dimethylformamide in a mass ratio of 1:0.3:0.5.
[0101] Example 3
[0102] A method for preparing a high-performance modified ternary cathode material, the preparation steps of which are as follows:
[0103] 1. Preparation of intermediate samples of ternary cathode materials
[0104] (1) Preparation of cobalt hydroxide-coated ternary precursor:
[0105] Take the ternary precursor dust collection material Ni 0.8 Co 0.1 Mn 0.1 (OH)2 (particle size 1.4-6 μm) and cobalt sulfate were added to a stirred reactor filled with deionized water, stirred at 100 r / min for 20 min to obtain slurry I, and then ammonia water was added to the slurry I to adjust the pH value to 9-11. The slurry was aged at 30 ° C for 4 h, and then filtered, washed and dried to obtain the cobalt hydroxide-coated precursor Co(OH)2-Ni 0.8 Co0.1 Mn 0.1 (OH)2 (particle size 1.4 ~ 6μm); In the above preparation method, the precursor dust collecting material Ni 0.8 Co 0.1 Mn 0.1 The mass ratio of (OH)2, cobalt sulfate, and deionized water is 1:0.01:3;
[0106] (2) Preparation of intermediate samples of ternary cathode materials:
[0107] The ternary precursor Ni 0.8 Co 0.1 Mn 0.1 (OH)2 (particle size 1.5 ~ 8μm), coated ternary precursor Co(OH)2-Ni 0.8 Co 0.1 Mn 0.1 (OH)2, strontium oxide, and lithium carbonate are mixed in a mass ratio of 0.3:3:0.012:1.43, and the internal pressure of the kiln is set to 200Pa and the temperature is set to 700℃. The mixed material is sintered for 10 hours, and then crushed and sieved to obtain an intermediate sample of the ternary positive electrode material; among them, the total number of particles W1 with a particle size of 1.2 to 2.9μm in the intermediate sample of the ternary positive electrode material accounts for 20.8% of the total number of particles W0, and the particle size distribution dispersion is 2.4. In the residual alkali of the obtained material, the mass proportion of lithium hydroxide is 0.1%, and the mass proportion of lithium carbonate is 0.1%.
[0108] 2. Preparation of modified aluminum hydroxide / poly (TA) composite layer coated ternary positive electrode material
[0109] (1) Preparation of aluminum hydroxide coated ternary positive electrode material:
[0110] The intermediate sample of the ternary cathode material prepared in 1 and aluminum sulfate were added to a stirred reactor filled with deionized water, and stirred at 400 r / min for 60 min to obtain slurry II. Sodium hydroxide was then added to the slurry II to adjust the pH value to 9-11, and the slurry was aged at 40°C for 2 h, and then filtered, washed, and dried to obtain slurry II. In the above preparation method, the mass ratio of the intermediate sample of the ternary cathode material, aluminum sulfate, and deionized water was 1:0.03:5;
[0111] (2) Preparation of aluminum hydroxide / poly (TA) composite layer coated ternary positive electrode material:
[0112] Aluminum hydroxide-coated ternary cathode material and thioctic acid (TA) were added to a reactor at the same time, the reaction temperature was set at 100°C, the stirring speed was 50 r / min, and the reaction was stirred for 2 hours. Chloroform was then added and the stirring reaction was continued for 30 minutes, and then the temperature was cooled to room temperature to obtain an aluminum hydroxide / poly (TA) composite layer coated ternary cathode material. In the above preparation method, the mass ratio of aluminum hydroxide-coated ternary cathode material, thioctic acid (TA), and chloroform was 2066.46:3.6:1.
[0113] (3) Preparation of modified aluminum hydroxide / poly (TA) composite layer coated ternary positive electrode material
[0114] The low-temperature plasma surface treatment machine was evacuated to a vacuum degree of 5Pa, and then a certain amount of oxygen was introduced into the treatment machine to make the treatment pressure reach 20Pa, and an aluminum hydroxide / poly (TA) composite layer-coated ternary positive electrode material was added thereto for low-temperature oxygen plasma surface treatment to obtain a modified aluminum hydroxide / poly (TA) composite layer-coated ternary positive electrode material; in the above preparation method, the low-temperature oxygen plasma surface treatment step is: setting the frequency of the low-temperature oxygen plasma surface treatment machine to 10Hz, setting the input power to 200W, fixing the spray gun nozzle to 10mm away from the sample, and using a bow-shaped reciprocating treatment for 5s.
[0115] 3. Preparation of high-performance ternary cathode materials
[0116] The internal temperature of the coulter dryer cavity is maintained at 110°C by circulating heating oil, the main shaft speed is set to 100r / min, and the modified aluminum hydroxide / poly (TA) composite layer coated ternary positive electrode material is added to the reaction liquid and stirred for 30 minutes. Then, the internal temperature of the coulter dryer cavity is maintained at 30°C by reducing the circulating heating oil temperature, the main shaft speed is set to 50r / min, and the stirring reaction time is continued for 1 hour. After cooling to room temperature, the material is sieved and demagnetized to obtain a polyurea modified aluminum hydroxide / poly (TA) composite layer coated ternary positive electrode material, which is the high-performance positive electrode material. In the above preparation method, the mass ratio of the modified aluminum hydroxide / poly (TA) composite layer coated ternary positive electrode material to the reaction liquid is 1:0.17; the reaction liquid is obtained by stirring and mixing 1,5-naphthalene diisocyanate, α,ω-diisocyanate polyethylene glycol, and acetone in a mass ratio of 1:0.21:0.5.
[0117] Example 4
[0118] A method for preparing a high-performance ternary cathode material, the preparation steps of which are as follows:
[0119] 1. Preparation of intermediate samples of ternary cathode materials
[0120] (1) Preparation of cobalt hydroxide-coated ternary precursor:
[0121] Take the ternary precursor dust collection material Ni 0.9 Co0.02 Mn 0.08 (OH)2 (particle size 1.2-5 μm) and cobalt sulfate were added to a stirred reactor filled with deionized water, stirred at 124 r / min for 72 min to obtain slurry I, and then sodium hydroxide was added to slurry I to adjust the pH value to 9-11. The slurry was aged at 55 ° C for 8.4 h, and then filtered, washed and dried to obtain the cobalt hydroxide-coated precursor Co(OH)2-Ni 0.9 Co 0.02 Mn 0.08 (OH)2 (particle size 1.3 ~ 5.5μm); In the above preparation method, the precursor dust collecting material Ni 0.9 Co 0.02 Mn 0.08 The mass ratio of (OH)2, cobalt sulfate, and deionized water is 1:0.027:4.2;
[0122] (2) Preparation of intermediate samples of ternary cathode materials:
[0123] The ternary precursor Ni 0.9 Co 0.02 Mn 0.08 (OH)2 (particle size 1.2 ~ 9μm), coated ternary precursor Co(OH)2-Ni 0.9 Co 0.02 Mn 0.08 (OH)2, zirconium oxide, and lithium perchlorate are mixed in a mass ratio of 0.78:3:0.0016:1.73, and the internal pressure of the kiln is set to 340Pa and the temperature is set to 880℃. The mixed material is sintered for 18 hours, and then crushed and sieved to obtain an intermediate sample of the ternary positive electrode material; among them, the total number of particles W1 with a particle size of 1.2 to 2.9μm in the intermediate sample of the ternary positive electrode material accounts for 28.8% of the total number of particles W0, and the particle size distribution dispersion is 3.7. In the residual alkali of the obtained material, the mass proportion of lithium hydroxide is 0.192%, and the mass proportion of lithium carbonate is 0.184%.
[0124] 2. Preparation of modified aluminum hydroxide / poly (TA) composite layer coated ternary positive electrode material
[0125] (1) Preparation of aluminum hydroxide coated ternary positive electrode material:
[0126] The intermediate sample of the ternary cathode material prepared in 1 and aluminum sulfate were added to a stirred reactor filled with deionized water, and stirred at 640 r / min for 105 min to obtain slurry II. Ammonia water was then added to the slurry II to adjust the pH value to 9-11, and the slurry was aged at 72°C for 12 h, and then filtered, washed, and dried to obtain slurry II. In the above preparation method, the mass ratio of the intermediate sample of the ternary cathode material, aluminum sulfate, and deionized water was 1:0.043:5.8;
[0127] (2) Preparation of aluminum hydroxide / poly (TA) composite layer coated ternary positive electrode material:
[0128] Aluminum hydroxide-coated ternary cathode material and thioctic acid (TA) were added to a reactor at the same time, the reaction temperature was set at 118°C, the stirring speed was 87 r / min, and the reaction was stirred for 4.2 hours. Dichloromethane was then added and the stirring reaction was continued for 45 minutes before cooling to room temperature to obtain an aluminum hydroxide / poly (TA) composite layer coated ternary cathode material; in the above preparation method, the mass ratio of aluminum hydroxide-coated ternary cathode material, thioctic acid (TA), and dichloromethane was 4078.12:13.6:1;
[0129] (3) Preparation of modified aluminum hydroxide / poly (TA) composite layer coated ternary positive electrode material
[0130] The low-temperature plasma surface treatment machine was evacuated to a vacuum degree of 6.4 Pa, and then a certain amount of oxygen was introduced into the treatment machine to make the treatment pressure reach 68 Pa, and an aluminum hydroxide / poly (TA) composite layer-coated ternary positive electrode material was added thereto for low-temperature oxygen plasma surface treatment to obtain a modified aluminum hydroxide / poly (TA) composite layer-coated ternary positive electrode material; in the above preparation method, the low-temperature oxygen plasma surface treatment step is: setting the frequency of the low-temperature oxygen plasma surface treatment machine to 38 Hz, setting the input power to 720 W, fixing the spray gun nozzle to 12.8 mm from the sample, and using a bow-shaped reciprocating treatment for 24 seconds.
[0131] 3. Preparation of high-performance ternary cathode materials
[0132] The internal temperature of the coulter dryer cavity was maintained at 121°C by circulating heating oil, the spindle speed was set to 118r / min, and the modified aluminum hydroxide / poly (TA) composite layer coated ternary positive electrode material was added to the reaction liquid and stirred for 53 minutes. The internal temperature of the coulter dryer cavity was then maintained at 38°C by reducing the circulating heating oil temperature, the spindle speed was set to 85r / min, and the stirring reaction time was continued for 1.8 hours. After cooling to room temperature, the material was sieved and demagnetized to obtain a polyurea modified aluminum hydroxide / poly (TA) composite layer coated ternary positive electrode material, which is the high-performance positive electrode material. In the above preparation method, the mass ratio of the modified aluminum hydroxide / poly (TA) composite layer coated ternary positive electrode material to the reaction liquid is 1:0.21; the reaction liquid is obtained by stirring and mixing diphenylmethane diisocyanate, α,ω-diisocyanate polyethylene glycol, and acetone in a mass ratio of 1:0.28:0.5.
[0133] Example 5
[0134] A method for preparing a high-performance modified ternary cathode material, the preparation steps of which are as follows:
[0135] 1. Preparation of intermediate samples of ternary cathode materials
[0136] (1) Preparation of cobalt hydroxide-coated ternary precursor:
[0137] Take the ternary precursor dust collection material Ni 0.6 Co 0.2 Mn 0.2 (OH)2 (particle size 1.5-5 μm) and cobalt sulfate were added to a stirred reactor filled with deionized water, stirred at 300 r / min for 120 min to obtain slurry I, and then sodium hydroxide was added to slurry I to adjust the pH value to 9-11. The slurry was aged at 65 ° C for 16 h, and then filtered, washed and dried to obtain the cobalt hydroxide-coated precursor Co(OH)2-Ni 0.6 Co 0.2 Mn 0.2 (OH)2 (particle size 1.55 ~ 5.5μm); In the above preparation method, the precursor dust collecting material Ni 0.6 Co 0.2 Mn 0.2 The mass ratio of (OH)2, cobalt sulfate, and deionized water is 1:0.05:5;
[0138] (2) Preparation of intermediate samples of ternary cathode materials:
[0139] The ternary precursor Ni 0.6 Co 0.2 Mn 0.2 (OH)2 (particle size 1.2 ~ 8μm), coated ternary precursor Co(OH)2-Ni 0.6 Co 0.2 Mn 0.2 (OH)2, molybdenum trioxide, and lithium perchlorate are mixed in a mass ratio of 1:3:0.0001:1.92, and the internal pressure of the kiln is set to 500Pa and the temperature is set to 950℃. The mixed material is sintered for 30 hours, and then crushed and sieved to obtain an intermediate sample of the ternary positive electrode material; among them, the total number of particles W1 with a particle size of 1.2 to 2.9μm in the intermediate sample of the ternary positive electrode material accounts for 31.2% of the total number of particles W0, and the particle size distribution dispersion is 4. In the residual alkali of the obtained material, the mass proportion of lithium hydroxide is 0.25%, and the mass proportion of lithium carbonate is 0.2%.
[0140] 2. Preparation of modified aluminum hydroxide / poly (TA) composite layer coated ternary positive electrode material
[0141] (1) Preparation of aluminum hydroxide coated ternary positive electrode material:
[0142] The intermediate sample of the ternary cathode material prepared in step 1 and aluminum sulfate were added to a stirred reactor filled with deionized water, and stirred at 800 r / min for 120 min to obtain slurry II. Ammonia water was then added to the slurry II to adjust the pH value to 9-11, and the slurry was aged at 75°C for 12 h, and then filtered, washed, and dried to obtain slurry II. In the above preparation method, the mass ratio of the intermediate sample of the ternary cathode material, aluminum sulfate, and deionized water was 1:0.06:8.
[0143] (2) Preparation of aluminum hydroxide / poly (TA) composite layer coated ternary positive electrode material:
[0144] Aluminum hydroxide-coated ternary cathode material and thioctic acid (TA) were added to a reactor at the same time, the reaction temperature was set at 120°C, the stirring speed was 100 r / min, and the reaction was stirred for 6 hours. Dichloromethane was then added and the stirring reaction was continued for 60 minutes, and then the temperature was cooled to room temperature to obtain an aluminum hydroxide / poly (TA) composite layer coated ternary cathode material; in the above preparation method, the mass ratio of aluminum hydroxide-coated ternary cathode material, thioctic acid (TA), and dichloromethane was 25756.94:25.76:1;
[0145] (3) Preparation of modified aluminum hydroxide / poly (TA) composite layer coated ternary positive electrode material
[0146] The low-temperature plasma surface treatment machine was evacuated to a vacuum degree of 10Pa, and then a certain amount of oxygen was introduced into the treatment machine to make the treatment pressure reach 100Pa, and an aluminum hydroxide / poly (TA) composite layer-coated ternary positive electrode material was added thereto for low-temperature oxygen plasma surface treatment to obtain a modified aluminum hydroxide / poly (TA) composite layer-coated ternary positive electrode material; in the above preparation method, the low-temperature oxygen plasma surface treatment step is: setting the frequency of the low-temperature oxygen plasma surface treatment machine to 40Hz, setting the input power to 800W, fixing the spray gun nozzle to 15mm from the sample, and using a bow-shaped reciprocating treatment for 25s.
[0147] 3. Preparation of high-performance ternary cathode materials
[0148] The internal temperature of the coulter dryer cavity is maintained at 130°C by circulating heating oil, the spindle speed is set to 200r / min, and the modified aluminum hydroxide / poly (TA) composite layer coated ternary positive electrode material is added to the reaction liquid and stirred for 60 minutes. Then, the internal temperature of the coulter dryer cavity is maintained at 50°C by reducing the circulating heating oil temperature, the spindle speed is set to 100r / min, and the stirring reaction time is continued for 2 hours. After cooling to room temperature, it is sieved and demagnetized to obtain a polyurea modified aluminum hydroxide / poly (TA) composite layer coated ternary positive electrode material, which is the high-performance positive electrode material; in the above preparation method, the mass ratio of the modified aluminum hydroxide / poly (TA) composite layer coated ternary positive electrode material to the reaction liquid is 1:0.24; the reaction liquid is obtained by stirring and mixing diphenylmethane diisocyanate, α,ω-diisocyanate polyethylene glycol, and acetone in a mass ratio of 1:0.34:0.5.
[0149] Comparative Example 1
[0150] This comparative example provides a positive electrode material with mixed large and small particles, and the specific preparation steps are as follows:
[0151] (1) Preparation of cobalt hydroxide-coated ternary precursor:
[0152] Take the ternary precursor dust collection material Ni 0.7 Co 0.1 Mn 0.2 (OH)2 (particle size 1.0-6.4 μm) and cobalt sulfate were added to a stirred reactor filled with deionized water, stirred at 300 r / min for 20 min to obtain slurry I, and then ammonia water was added to the slurry I to adjust the pH value to 9-11. The slurry was aged at 65 ° C for 16 h, and then filtered, washed and dried to obtain the cobalt hydroxide-coated precursor Co(OH)2-Ni 0.7 Co 0.1 Mn 0.2 (OH)2 (particle size 1.1 ~ 6.8μm); In the above preparation method, the precursor dust collecting material Ni 0.7 Co 0.1 Mn 0.2 The mass ratio of (OH)2, cobalt sulfate, and deionized water is 1:0.01:5;
[0153] (2) Preparation of ternary cathode materials:
[0154] The ternary precursor Ni 0.7 Co 0.1 Mn 0.2 (OH)2 (particle size 1.1 ~ 9μm), coated ternary precursor Co(OH)2-Ni 0.7 Co 0.1 Mn 0.2(OH)2, tungstic acid and lithium hydroxide are mixed in a mass ratio of 0.3:1:0.012:1.43, the internal pressure of the kiln is set to 500Pa and the temperature is set to 950℃, the mixed material is sintered for 10 hours, and then crushed and sieved to obtain a ternary positive electrode material; among them, the total number of particles W1 with a particle size of 1.2 to 2.9μm in the ternary positive electrode material accounts for 31.2% of the total number of particles W0, the particle size distribution discreteness is 4, the mass proportion of lithium hydroxide is 0.25%, and the mass proportion of lithium carbonate is 0.14%.
[0155] Comparative Example 2
[0156] A method for preparing a high-performance modified ternary cathode material, the preparation steps of which are as follows:
[0157] 1. Preparation of intermediate samples of ternary cathode materials
[0158] (1) Preparation of cobalt hydroxide-coated ternary precursor:
[0159] Take the ternary precursor dust collection material Ni 0.7 Co 0.1 Al 0.2 (OH)2 (particle size 1.3 ~ 6μm) and cobalt sulfate were added to a stirred reactor filled with deionized water, stirred and mixed at 140r / min for 80min to obtain slurry I, and then ammonia water was added to the slurry I to adjust the pH value to 9-11, aged at 50℃ for 10h, and then filtered, washed and dried to obtain cobalt hydroxide-coated precursor Co(OH)2-Ni 0.7 Co 0.1 Al 0.2 (particle size 1.4 ~ 6.5μm); in the above preparation method, the precursor dust collecting material Ni 0.7 Co 0.1 Al 0.2 The mass ratio of (OH)2, cobalt sulfate, and deionized water is 1:0.04:3;
[0160] (2) Preparation of intermediate samples of ternary cathode materials:
[0161] The ternary precursor Ni 0.7 Co 0.1 Al 0.2 (OH)2 (particle size 1.3 ~ 8μm), coated ternary precursor Co(OH)2-Ni 0.7 Co 0.1 Al 0.2(OH)2, strontium carbonate, and lithium hexafluorophosphate are mixed in a mass ratio of 0.4:3:0.012:1.63. The internal pressure of the kiln is set to 300Pa and the temperature is set to 800℃. The mixed material is sintered for 15 hours, and then crushed and sieved to obtain an intermediate sample of the ternary positive electrode material. Among them, the total number of particles W1 with a particle size of 1.2 to 2.9μm in the intermediate sample of the ternary positive electrode material accounts for 21.4% of the total number of particles W0, and the particle size distribution dispersion is 3.2. In the residual alkali of the obtained material, the mass proportion of lithium hydroxide is 0.18%, and the mass proportion of lithium carbonate is 0.1%.
[0162] 2. Preparation of modified aluminum hydroxide / poly (TA) composite layer coated ternary positive electrode material
[0163] (1) Preparation of aluminum hydroxide coated ternary positive electrode material:
[0164] The intermediate sample of the ternary cathode material prepared in 1 and aluminum sulfate were added to a stirred reactor filled with deionized water, and stirred at 600 r / min for 80 min to obtain slurry II. Sodium hydroxide was then added to the slurry II to adjust the pH value to 9-11, and the slurry was aged at 62°C for 3.8 h, and then filtered, washed, and dried to obtain slurry II. In the above preparation method, the mass ratio of the ternary cathode material, aluminum sulfate, and deionized water was 1:0.04:6.5;
[0165] (2) Preparation of aluminum hydroxide / poly (TA) composite layer coated ternary positive electrode material:
[0166] Aluminum hydroxide coated ternary cathode material and thioctic acid (TA) were added to a reactor simultaneously, the reaction temperature was set at 110°C, the stirring speed was 66 r / min, and the reaction was stirred for 2.5 hours. Methanol was then added and the stirring reaction was continued for 50 minutes before cooling to room temperature to obtain an aluminum hydroxide / poly (TA) composite layer coated ternary cathode material. In the above preparation method, the mass ratio of aluminum hydroxide coated ternary cathode material, thioctic acid (TA), and methanol was 18062.2:16.8:1.
[0167] (3) Preparation of modified aluminum hydroxide / poly (TA) composite layer coated ternary positive electrode material
[0168] The low-temperature plasma surface treatment machine was evacuated to a vacuum degree of 8 Pa, and then a certain amount of oxygen was introduced into the treatment machine to make the treatment pressure reach 60 Pa, and an aluminum hydroxide / poly (TA) composite layer-coated ternary positive electrode material was added thereto for low-temperature oxygen plasma surface treatment to obtain a modified aluminum hydroxide / poly (TA) composite layer-coated ternary positive electrode material; in the above preparation method, the low-temperature oxygen plasma surface treatment step is: setting the frequency of the low-temperature oxygen plasma surface treatment machine to 32 Hz, setting the input power to 660 W, fixing the spray gun nozzle to 12 mm from the sample, and using a bow-shaped reciprocating treatment for 10 s.
[0169] Comparative Example 3
[0170] A method for preparing a high-performance ternary cathode material, the preparation steps of which are as follows:
[0171] 1. Preparation of intermediate samples of ternary cathode materials
[0172] (1) Preparation of cobalt hydroxide-coated ternary precursor:
[0173] Take the ternary precursor dust collection material Ni 0.8 Co 0.1 Mn 0.1 (OH)2 (particle size 1.4 ~ 6μm) and cobalt sulfate were added to a stirred reactor filled with deionized water, stirred at 100r / min for 20min to obtain slurry I, and then ammonia water was added to the slurry I to adjust the pH value to 9-11. The slurry was aged at 30℃ for 4h, and then filtered, washed and dried to obtain the cobalt hydroxide-coated precursor Co(OH)2-Ni 0.8 Co 0.1 Mn 0.1 (OH)2 (particle size 1.4 ~ 6μm); In the above preparation method, the precursor dust collecting material Ni 0.8 Co 0.1 Mn 0.1 The mass ratio of (OH)2, cobalt sulfate, and deionized water is 1:0.01:3;
[0174] (2) Preparation of intermediate samples of ternary cathode materials:
[0175] The ternary precursor Ni 0.8 Co 0.1 Mn 0.1 (OH)2 (particle size 1.5 ~ 8μm), coated ternary precursor Co(OH)2-Ni 0.8 Co 0.1 Mn 0.1 (OH)2, strontium oxide, and lithium carbonate are mixed in a mass ratio of 0.3:3:0.012:1.43, and the internal pressure of the kiln is set to 200Pa and the temperature is set to 700℃. The mixed material is sintered for 10 hours, and then crushed and sieved to obtain an intermediate sample of the ternary positive electrode material; among them, the total number of particles W1 with a particle size of 1.2 to 2.9μm in the intermediate sample of the ternary positive electrode material accounts for 20.8% of the total number of particles W0, and the particle size distribution dispersion is 2.4. In the residual alkali of the obtained material, the mass proportion of lithium hydroxide is 0.1%, and the mass proportion of lithium carbonate is 0.1%.
[0176] 2. Preparation of polyurea modified ternary cathode materials
[0177] The internal temperature of the coulter dryer cavity was maintained at 110°C by circulating heating oil, the spindle speed was set to 100 r / min, the intermediate sample of the ternary positive electrode material was added to the reaction liquid and stirred for 30 minutes, and then the internal temperature of the coulter dryer cavity was maintained at 30°C by lowering the circulating heating oil temperature, the spindle speed was set to 50 r / min, and the stirring reaction time was continued for 1 hour. After cooling to room temperature, the material was sieved and demagnetized to obtain a polyurea modified ternary positive electrode material; in the above preparation method, the mass ratio of the ternary positive electrode material to the reaction liquid was 1:0.17; the reaction liquid was obtained by stirring and mixing 1,5-naphthalene diisocyanate, α,ω-diisocyanate polyethylene glycol, and acetone in a mass ratio of 1:0.21:0.5.
[0178] Test Analysis
[0179] Under the same proportion of active substances, corresponding ternary lithium-ion batteries were prepared using the modified ternary cathode materials prepared in the comparative example and the embodiment, respectively, and marked as test examples 1 to 5 and comparative test examples 1 to 3.
[0180] The materials, amounts, and preparation methods of ternary lithium-ion batteries, except for the positive electrode material, are the same. The preparation method of ternary lithium-ion batteries is as follows: the modified ternary positive electrode material prepared in the embodiment and comparative example is used as the positive electrode active material, respectively, with the conductive agent carbon black and the binder polyvinylidene fluoride in a mass ratio of 90:5:5, and N-methyl pyrrolidone as a dispersant, and then evenly coated on aluminum foil. After drying, it is cut into 8mm diameter positive electrode discs and transferred to a 120℃ vacuum oven to dry for 24 hours. The prepared positive electrode disc is used as the working electrode, the metal lithium sheet is used as the counter electrode, and 1 mol / LLiPF6 is dissolved in a mixed solution of ethylene carbonate and dimethyl carbonate (wt% = 1:1) as the electrolyte. 2032-type button cells are assembled in a glove box. The electrochemical performance is tested within the cut-off voltage range of 2.8~4.2V.
[0181] (1) Battery rate retention test: Charge the battery from 2.8V to 4.2V at a constant current of 1C, maintain constant voltage charging at 4.2V, and use a cut-off current of 0.05C; then discharge the battery to 2.8V at 1C and 3C, respectively. Record the discharge capacity retention at different rates at -30°C. The test data are recorded in Table 1.
[0182] (2) Powder resistivity test: A four-electrode powder resistance meter was used to test the powder resistance at the same pressure and different temperatures. The test data are recorded in Table 1.
[0183] (3) SEM test: The cathode materials prepared in Example 1 and Comparative Example 1 do not need to be subjected to gold spraying treatment. The microscopic morphology is directly photographed using a field emission scanning electron microscope. The photographic results are shown in FIG. Figure 1 and Figure 2.
[0184] Table 1
[0185]
[0186] from Figure 1 and Figure 2 It can be seen that the high-performance positive electrode material prepared in the embodiment is compared with the positive electrode material prepared in comparative example 1, and its polyurea-modified aluminum hydroxide / poly (TA) composite layer is evenly and effectively coated on the surface of the positive electrode material, which can effectively improve the lithium diffusion coefficient of the material at low temperature, reduce the polarization internal resistance of the prepared lithium-ion battery at low temperature, and show excellent high-rate charge and discharge performance under low temperature conditions.
[0187] From the rate performance test data in Table 1, it can be seen that the capacity retention rates of Test Examples 1 to 5 at 1C and 3C under low temperature conditions (-30°C) are all higher than 90%, showing excellent low-temperature charge and discharge performance compared to Comparative Test Examples 1 to 3. In addition, the powder resistivity test results under the same pressure also show that the resistivity of Test Examples 1 to 5 at different temperatures is significantly lower than that of Comparative Test Examples 1 to 3, which indicates that the polyurea-modified aluminum hydroxide / poly (TA) composite layer effectively improves the lithium diffusion coefficient at low temperatures and reduces the polarization internal resistance of the lithium-ion battery at low temperatures.
[0188] From the above test results, it can be seen that the above embodiments of the present invention achieve the following technical effects:
[0189] The polyurea-modified aluminum hydroxide / poly (TA) composite layer coated ternary positive electrode material prepared by the present invention effectively improves the lithium diffusion coefficient at low temperature, reduces the polarization internal resistance of the lithium-ion battery at low temperature, and the battery exhibits excellent high-rate charge and discharge performance under low temperature conditions.
[0190] The present invention has been described in detail above. It will be apparent to those skilled in the art that the present invention may be practiced over a wide range of parameters, concentrations, and conditions without departing from the spirit and scope of the present invention and without unnecessary experimentation. Although specific embodiments have been given herein, it should be understood that further modifications may be made to the present invention. In summary, this application is intended to encompass any variations, uses, or improvements to the present invention, including those made by conventional techniques known in the art that depart from the scope of the present invention. Applications of the essential features may be made within the scope of the following claims.
Claims
1. A method for preparing a modified ternary cathode material, characterized in that: The preparation method comprises the following steps: 1) mixing a ternary precursor, a cobalt hydroxide-coated ternary precursor, a dopant, and a lithium source, and sintering the mixed material to obtain an intermediate sample of a ternary cathode material; 2) coating the surface of the intermediate sample of the ternary cathode material in step 1 with aluminum hydroxide, then reacting it with lipoic acid (TA) in the first step, and then adding solvent I to carry out the second step reaction to obtain an aluminum hydroxide / poly (TA) composite layer coated ternary cathode material; the solvent I is selected from at least one of dichloromethane, methanol, and chloroform; 3) subjecting the aluminum hydroxide / poly (TA) composite layer coated ternary cathode material described in step 2 to a low-temperature oxygen plasma surface treatment to obtain a modified aluminum hydroxide / poly (TA) composite layer coated ternary cathode material; 4) The modified aluminum hydroxide layer and the poly (TA) film layer composite layer coated ternary positive electrode material described in step 3 are polymerized with diisocyanate and α, ω-diisocyanate polyethylene glycol to obtain a polyurea-modified aluminum hydroxide / poly (TA) composite layer coated modified ternary positive electrode material, which is the modified ternary positive electrode material.
2. The preparation method according to claim 1, wherein: In the step 1), the chemical formula of the ternary precursor is Ni x Co y M 1-x-y (OH)2, wherein 0<x<1, 0<y<1, 1-xy>0, and M is at least one of Mn and Al; And / or, in step 1), the lithium source is at least one of lithium hydroxide, lithium perchlorate, lithium hexafluorophosphate, and lithium carbonate; And / or, in step 1), the dopant is at least one of tungstic acid, tungsten oxide, strontium carbonate, strontium oxide, aluminum oxide, zirconium oxide, niobium oxide, boric acid, vanadium dioxide, and molybdenum trioxide.
3. The preparation method according to claim 1, wherein: In the step 1, the particle size of the ternary precursor is in the range of 1.2 to 9 μm; And / or, in step 1, the particle size of the cobalt hydroxide-coated ternary precursor is in the range of 1.3 to 6.8 μm.
4. The preparation method according to claim 1, wherein: In step 1, the preparation method of the cobalt hydroxide-coated ternary precursor comprises the following steps: taking the ternary precursor dust collection material and the coating agent I and adding them into a stirred reactor filled with deionized water, stirring and mixing at 100 to 300 r / min for 20 to 120 minutes to obtain slurry I, then adding the precipitant I to the slurry I to adjust the pH value to 9 to 11, aging at 30 to 65° C. for 4 to 16 hours, and then filtering, washing, and drying to obtain the cobalt hydroxide-coated ternary precursor.
5. The preparation method according to claim 4, characterized in that: The particle size range of the ternary precursor dust collecting material is 1.2 to 6.4 μm; And / or, the coating agent I is cobalt sulfate; And / or, the mass ratio of the ternary precursor dust collecting material, coating agent I, and deionized water is 1:0.01-0.05:3-5; And / or, the precipitant I is ammonia water and / or sodium hydroxide.
6. The preparation method according to claim 1, wherein: In the step 1, the mass ratio of the ternary precursor, the cobalt hydroxide-coated ternary precursor, the dopant, and the lithium source is (0.3-1):3:(0.0001-0.012):(1.43-1.92); And / or, in step 1, the sintering is carried out in a kiln, the internal pressure of the kiln is set to 200-500 Pa during the sintering; the sintering temperature is 700-950° C., and the sintering time is 10-30 hours.
7. The preparation method according to claim 1, wherein: In the step 1, the percentage of the total number of particles W1 with a particle size of 1.2 to 2.9 μm in the intermediate sample of the ternary positive electrode material to the total number of particles W0 is 20.8 to 31.2%; And / or, in step 1, the particle size distribution dispersion of the intermediate sample of the ternary positive electrode material is 2.4 to 4.
8. The preparation method according to claim 1, wherein: In step 2, the aluminum hydroxide coating method includes the following steps: adding the intermediate sample of the ternary positive electrode material and the coating agent II into a stirred reactor filled with deionized water, stirring and mixing at 400-800 r / min for 60-120 minutes to obtain slurry II, then adding a precipitant II to the slurry II to adjust the pH value to 9-11, aging at 40-75°C for 2-12 hours, and then filtering, washing, and drying to obtain the slurry.
9. The preparation method according to claim 8, characterized in that: The mass ratio of the intermediate sample of the ternary positive electrode material, the coating agent II, and the deionized water is 1:0.03-0.06:5-8; And / or, the coating agent II is aluminum sulfate; And / or, the precipitant II is ammonia water and / or sodium hydroxide.
10. The preparation method according to claim 1, characterized in that: In the step 2, the mass ratio of the aluminum hydroxide-coated ternary cathode material intermediate sample, thioctic acid (TA), and solvent I is (2066.46-25756.94): (3.6-25.76): 1; And / or, in step 2, the reaction temperature of the first step reaction is 100-120° C., the stirring speed is 50-100 r / min, and the stirring reaction time is 2-6 h; the stirring reaction time of the second step reaction is 30-60 min.
11. The preparation method according to claim 1, characterized in that: In step 3, the low-temperature oxygen plasma surface treatment is carried out in a low-temperature plasma surface treatment machine. Before the treatment, the low-temperature plasma surface treatment machine needs to be evacuated, and then oxygen is introduced into the treatment machine to reach the required treatment pressure; The vacuum degree of the vacuum pumping is 5-10Pa; the processing pressure is 20-100Pa.
12. The preparation method according to claim 1, characterized in that: In step 3, the low-temperature oxygen plasma surface treatment step is as follows: setting the frequency of the low-temperature oxygen plasma surface treatment machine to 10-40 Hz, setting the input power to 200-800 W, fixing the spray gun nozzle to 10-15 mm from the sample, and using a bow-shaped reciprocating treatment for 5-25 seconds.
13. The preparation method according to claim 1, characterized in that: In the step 4, the polymerization is carried out in a reaction solution, wherein the reaction solution is obtained by stirring and mixing the diisocyanate, the α,ω-diisocyanate polyethylene glycol and the solvent II in a mass ratio of 1:0.21 to 0.34:0.5; In the step 3, the mass ratio of the modified aluminum hydroxide / poly (TA) composite layer coated ternary positive electrode material to the reaction solution is 1:0.17-0.
24.
14. The preparation method according to claim 13, characterized in that: The α,ω-diisocyanate polyethylene glycol has the following structural formula: 500≤n≤1000; And / or, the diisocyanate is at least one of toluene diisocyanate, diphenylmethane diisocyanate, and 1,5-naphthalene diisocyanate; And / or, the solvent II is acetone and / or N,N-dimethylformamide.
15. The preparation method according to claim 1, characterized in that: In step 4, the polymerization reaction is a two-step temperature polymerization, that is, a stirring reaction is first performed, the reaction temperature is lowered, and then a second stirring reaction is performed; the first stirring reaction and the second stirring reaction are both performed in a coulter dryer; The primary stirring reaction is to maintain the internal temperature of the coulter dryer cavity at 110-130°C by a heat transfer medium, set the spindle speed to 100-200r / min, and the reaction time to 30-60min; The secondary stirring reaction is to maintain the internal temperature of the coulter dryer cavity at 30-50° C. by using a heat transfer medium, set the main shaft speed to 50-100 r / min, and the reaction time to 1-2 hours.
16. The modified ternary cathode material prepared according to the method according to any one of claims 1 to 15.
17. A lithium-ion battery comprising a positive electrode, a negative electrode, a separator, and an electrolyte, characterized in that: The material of the positive electrode includes the modified ternary positive electrode material according to claim 16.
Citation Information
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