ALUMINUM-COATED PRECURSOR, PREPARATION METHOD THEREFOR, AND USE THEREOF

Abstract

Disclosed are an aluminum-coated precursor and a preparation method therefor. The aluminum coated precursor has a chemical formula of xMCO.sub.3(1-x).Al(OH).sub.3, wherein M is at least one of nickel, cobalt and manganese, and x is 0.995-0.999. The aluminum-coated precursor has the advantages of a controllable particle size and uniform particle size distribution, a high degree of sphericity, a smooth particle surface, a high tap density, not easily breaking, and an excellent electrochemical performance and energy density.

Claims

1. An aluminum-coated precursor, having a chemical formula of xMCO.sub.3(1-x).Al(OH).sub.3, wherein M is at least one of nickel, cobalt and manganese, and x is 0.995 to 0.999.

2. The precursor according to claim 1, wherein the precursor has a particle size of 6 μm to 15 μm and a tap density of not lower than 1.8 g/cm.sup.3.

3. A method for preparing the precursor according to claim 1, comprising: (1) continuously introducing carbon dioxide in the presence of a conductive agent, mixing a metal salt with a precipitant for a precipitation reaction, and then sealing same and leaving to stand, so as to obtain pre-prepared particles; (2) mixing the pre-prepared particles with water to obtain a slurry, and with stirring, continuously introducing the metal salt, the precipitant and the carbon dioxide for a coprecipitation reaction, so as to obtain a reacted liquid; (3) mixing the reacted liquid with an aluminum salt for a reaction, and aging and stirring same, so as to obtain an aged material; and (4) successively performing iron removal, solid-liquid separation, washing, and drying on the aged material, so as to obtain an aluminum-coated precursor.

4. The method according to claim 3, wherein, in step (1), the metal salt comprises at least one of a soluble nickel salt, a soluble manganese salt and a soluble cobalt salt, and the metal salt is in a concentration of 899 g/L to 400 g/L.

5. (canceled)

6. The method according to claim 4, wherein, in step (1), the soluble nickel salt is at least one selected from the group consisting of nickel chloride, nickel nitrate, and nickel sulfate, the soluble cobalt salt is at least one selected from the group consisting of cobalt chloride, cobalt nitrate, and cobalt sulfate, and the soluble manganese salt is at least one selected from the group consisting of manganese chloride, manganese nitrate, and manganese sulfate.

7. (canceled)

8. (canceled)

9. The method according to claim 3, wherein, in step (1), the carbon dioxide is at a flow rate of 0.1 L/min to 0.5 L/min.

10. The method according to claim 3, wherein, in step (1), the metal salt and the precipitant are in a molar ratio of 1:(2 to 3.5).

11. The method according to claim 3, wherein, in step (1), the conductive agent is used in an amount of 10 g to 50 g, based on a total of 1 L of the metal salt and the precipitant.

12. The method according to claim 3, wherein, in step (1), the precipitant is at least one selected from the group consisting of sodium carbonate, ammonium bicarbonate, sodium hydroxide, and sodium bicarbonate; optionally, the sodium carbonate is in a concentration of 50 g/L to 200 g/L; optionally, the ammonium bicarbonate is in a concentration of 50 g/L to 200 g/L; optionally, the sodium hydroxide is in a concentration of 50 g/L to 200 g/L; and optionally, the sodium bicarbonate is in a concentration of 50 g/L to 200 g/L.

13. (canceled)

14. (canceled)

15. (canceled)

16. (canceled)

17. (canceled)

18. (canceled)

19. The method according to claim 3, wherein, in step (1), the conductive agent is at least one of glucose and fructose; wherein, in step (1), the pre-prepared particles have a particle size of 1 μm to 2 μm.

20. (canceled)

21. The method according to claim 3, wherein, in step (2), the slurry has a solid content of 50 g/L to 100 g/L.

22. (canceled)

23. (canceled)

24. The method according to claim 3, wherein, in step (2), the metal salt is continuously introduced at a flow rate of 100 mL/h to 500 mL/h, the precipitant is continuously introduced at a flow rate of 100 mL to 500 mL/h, and the carbon dioxide is continuously introduced at a flow rate of 0.25 L/min to 0.6 L/min, and the reacted liquid has a solid content of 30 g/L to 500 g/L.

25. (canceled)

26. The method according to claim 3, wherein, in step (2), with stirring, a complexing agent is continuously introduced, the complexing agent is ammonia water or ammonium bicarbonate, and the complexing agent is ammonia water or ammonium bicarbonate.

27. (canceled)

28. (canceled)

29. The method according to claim 3, wherein, in step (3), the reacted liquid and the aluminum salt are in a volume ratio of (10 to 20):1, the aluminum salt is at least one of aluminum chloride and aluminum sulfate, and the aluminum salt is in a concentration of 10 g/L to 50 g/L.

30. (canceled)

31. (canceled)

32. (canceled)

33. A method for preparing a cathode material, comprising: (a) mixing a precursor with a lithium salt and performing primary sintering, so as to obtain a primary sintered material; and (b) crushing the primary sintered material and performing secondary sintering, so as to obtain a cathode material; wherein, in step (a), the precursor is the aluminum-coated precursor according to claim 1.

34. The method according to claim 33, wherein, in step (a), the precursor material and the lithium salt are in a molar ratio of 1:(1.02 to 1.08).

35. The method according to claim 33, wherein, in step (a), the primary sintering is performed at a temperature of 450° C. to 600° C. for 4 hours to 6 hours, and in step (b), the secondary sintering is performed at a temperature of 700° C. to 850° C. for 15 hours to 25 hours.

36. (canceled)

37. A cathode material, prepared by using the method according to claim 33, wherein the cathode material has a chemical formula of Li(Li.sub.aNi.sub.mCo.sub.nMn.sub.(1-a-b-m-n)Al.sub.b)O.sub.2, wherein a is 0.05 to 0.35, b is 0.005 to 0.01, m is 0.01 to 0.25, and n is 0.01 to 0.25.

38. (canceled)

39. A lithium battery, comprising the cathode material according to claim 37.

40. A vehicle, comprising the lithium battery according to claim 39.

Description

BRIEF DESCRIPTION OF DRAWINGS

[0071] The drawings are used to provide a further understanding of the technical solutions of the present disclosure, constitute a part of the description, explain the solutions of the present disclosure in conjunction with the embodiments of the present application, and do not limit the technical solutions of the present disclosure.

[0072] FIG. 1 is a flowchart of a method for preparing an aluminum-coated precursor according to an embodiment of the present disclosure;

[0073] FIG. 2 is a flowchart of a method for preparing a cathode material according to an embodiment of the present disclosure;

[0074] FIG. 3 is a scanning electron microscope image of a prepared aluminum-coated precursor according to an embodiment of the present disclosure;

[0075] FIG. 4 is a scanning electron microscope image of a prepared aluminum-coated precursor according to an embodiment of the present disclosure; and

[0076] FIG. 5 is a first charge-discharge curve at 0.1 C of a button cell made of a prepared cathode material according to an embodiment of the present disclosure.

DETAILED DESCRIPTION

[0077] Technical solutions of the present disclosure are further described below through specific embodiments in conjunction with the drawings.

[0078] In an embodiment, the present disclosure provides an aluminum-coated precursor. The precursor has a chemical formula of xMCO.sub.3(1-x).Al(OH).sub.3, where M is at least one of nickel, cobalt and manganese, and x is 0.995 to 0.999. The aluminum-coated precursor has the advantages of controllable particle size, uniform particle size distribution, high degree of sphericity, smooth particle surface, high tap density, not easily breaking, excellent electrochemical performance, and excellent energy density, and meanwhile, the cathode material prepared by using the precursor has a high specific capacity, excellent cycle performance, and excellent electrochemical discharge performance. The precursor having such a composition has a high specific discharge capacity and stability. The precursor has a particle size of 6 μm to 15 μm and a tap density of not lower than 1.8 g/cm.sup.3.

[0079] In an embodiment, the present disclosure provides a method for preparing the aluminum-coated precursor. As shown in FIG. 1, the method includes steps S100, S200, S300, and S400.

[0080] In S100, carbon dioxide is continuously introduced in the presence of a conductive agent, a metal salt is mixed with a precipitant for a precipitation reaction and then sealed and left to stand, so as to obtain pre-prepared particles. The concentration of the metal salt is 80 g/L to 400 g/L. The precipitant is at least one selected from the group consisting of sodium carbonate, ammonium bicarbonate, sodium hydroxide, and sodium bicarbonate, where the concentration of sodium carbonate is 50 g/L to 200 g/L, the concentration of ammonium bicarbonate is 50 g/L to 200 g/L, the concentration of sodium hydroxide is 50 g/L to 200 g/L, and the concentration of sodium bicarbonate is 50 g/L to 200 g/L. The molar ratio of the metal salt to the precipitant is 1:(2 to 3.5). The amount of the conductive agent is 10 g to 50 g, based on a total of 1 L of the metal salt and the precipitant. In this process, carbon dioxide is continuously introduced at a flow rate of 0.1 L/min to 0.5 L/min. The precipitation reaction is performed at a temperature of 30° C. to 80° C. The operation of sealing and leaving to stand is performed for 12 hours to 24 hours. The particle size of the obtained pre-prepared particles is 1 μm to 2 μm.

[0081] In S200, the pre-prepared particles are mixed with water to obtain a slurry, and with stirring, the metal salt, the precipitant and carbon dioxide are continuously introduced to perform a coprecipitation reaction, so as to obtain a reacted liquid. The solid content of the slurry obtained by mixing pre-prepared particles and water is 50 g/L to 100 g/L. The stirring is performed at a speed of 350 rpm to 800 rpm. The coprecipitation reaction is performed at a temperature of 30° C. to 60° C. for 5 hours to 150 hours in a pH range of 6 to 8. The metal salt is continuously introduced at a flow rate of 100 mL/h to 500 mL/h, the precipitant is continuously introduced at a flow rate of 100 mL to 500 mL/h, and the carbon dioxide is continuously introduced at a flow rate of 0.25 L/min to 0.6 L/min. The solid content of the reacted liquid is controlled to be 30 g/L to 500 g/L.

[0082] In S300, the obtained reacted liquid is mixed with an aluminum salt for a reaction and then is aged and stirred, where aluminum elements in the aluminum salt react with the precipitant to precipitate on the surface of the precursor, so as to obtain an aged material. The aluminum salt is at least one of aluminum chloride and aluminum sulfate. The concentration of the aluminum salt is 10 g/L to 50 g/L. The weight ratio of the reacted liquid to the aluminum salt is (10 to 20):1. The stirring for aging is performed at a speed of 200 rpm to 300 rpm for 0.5 hour to 5 hours.

[0083] In S400, iron removal, solid-liquid separation, washing, and drying are successively performed on the aged material.

[0084] In an embodiment, the present disclosure provides a method for preparing a cathode material. As shown in FIG. 2, the method includes steps Sa and Sb.

[0085] In Sa, the above-mentioned precursor or a precursor prepared by using the above-mentioned method is mixed with a lithium salt and then subjected to primary sintering, so that lithium ions in the lithium salt enter the precursor and combine to form a lithium salt cathode material which is, namely, the primary sintered material. The lithium salt is selected from at least one of lithium hydroxide and lithium carbonate, the molar ratio of the precursor material to the lithium salt is 1:(1.02 to 1.08), and the primary sintering is performed at a temperature of 450° C. to 600° C. for 4 hours to 6 hours.

[0086] In Sb, the primary sintered material obtained in step Sa is crushed and then subjected to secondary sintering so that the lithium salt which does not enter the precursor in the primary sintering further migrates into the inside of precursor, which enables the reaction to sufficiently proceed in the sintering process, so as to obtain a cathode material. The secondary sintering is performed at 700° C. to 850° C. for 15 hours to 25 hours.

[0087] In an embodiment, the present disclosure provides a cathode material. The cathode material is prepared by using the method as described in the preceding embodiment.

[0088] In an embodiment, the present disclosure provides a lithium battery. The lithium battery includes the cathode material as described in the preceding embodiment.

[0089] In an embodiment, the present disclosure provides a vehicle. The vehicle includes the lithium battery as described in the preceding embodiment.

Example 1

[0090] The aluminum-coated precursor was prepared by using the following method.

[0091] (1) Nickel sulfate, cobalt sulfate and manganese sulfate were mixed in a nickel-cobalt-manganese molar ratio of 0.2:0.18:0.6 to obtain a mixed metal salt, where the concentrations of nickel sulfate, cobalt sulfate and manganese sulfate in the mixed metal salt were all 400 g/L. Then in the presence of glucose as the conductive agent, carbon dioxide was continuously introduced at a flow rate of 0.1 L/min, the mixed metal salt and a sodium hydroxide solution with a concentration of 200 g/L were quickly mixed (the mixing was completed within 10 seconds, where the molar ratio of the mixed metal salt to sodium hydroxide was 1:2.0, and the amount of the conductive agent glucose was 20 g based on a total of 1 L of the mixed metal salt and sodium hydroxide), and the mixture was sealed and left to stand at 30° C. for 12 hours, so as to obtain pre-prepared particles with a particle size of 1.2 μm.

[0092] (2) The pre-prepared particles were mixed with water to obtain a slurry (with the solid content of 200 g/L), and then the coprecipitation reaction was performed with stirring (at a speed of 400 rpm). Meanwhile, the mixed metal salt (at a flow rate of 200 mL/h), sodium bicarbonate (in a concentration of 50 g/L to 200 g/L and at a flow rate of 150 mL/h to 250 mL/h) and carbon dioxide (at a flow rate of 0.25 mL/min) were continuously introduced, and the pH of the system was controlled to be 7.5. The reaction was performed for 60 hours, so as to obtain a reacted material with a solid content of 500 g/L.

[0093] (3) The reacted liquid was mixed with aluminum chloride and then aged and stirred, so as to obtain an aged material, where the stirring was performed at a speed of 300 rpm and the aging was performed for 2 hours.

[0094] (4) The obtained aged material was successively subjected to iron removal, solid-liquid separation, washing and drying, so as to obtain an aluminum-coated precursor with a particle size of 8 μm, where the precursor had a chemical formula of (Mn.sub.0.6Ni.sub.0.2Co.sub.0.18)CO.sub.3.0.02Al(OH).sub.3 and a tap density of 1.8 g/cm.sup.3.

[0095] The cathode material was prepared by using the following method.

[0096] In Sa, the aluminum-coated precursor obtained in step (4) and lithium hydroxide were mixed in a molar ratio of 1:1.06 and then subjected to primary sintering at 500° C. in an air atmosphere for 6 hours, so as to obtain a primary sintered material.

[0097] In Sb, the obtained primary sintered material was crushed and then subjected to secondary sintering at 700° C. for 18 hours, so as to obtain a cathode material that had a chemical formula of Li(Li.sub.0.2Ni.sub.0.16Co.sub.0.15Mn.sub.0.48Al.sub.0.014)O.sub.2 and a compaction density of 3.2 g/cm.sup.3.

[0098] Conclusion: FIG. 3 and FIG. 4 are scanning electron microscope images of the precursor material. As can be seen, the precursor material prepared by using the above-mentioned method had a spherical structure, uniform particle size distribution and smooth surface, and it is further found from the detection of the particle size distribution by a laser particle size analyzer that the precursor had a uniform particle size distribution. Meanwhile, the cathode material was mixed with conductive agent carbon black (SP) and polyvinylidene fluoride (PVDF) and then stirred with N-methylpyrrolidone (NMP) as a solvent for several hours for pulping to prepare a lithium-ion half cell. The charge-discharge test was performed by using a LAND cell tester at 4.8 V, and it is found that the discharge capacity of per gram of the product at 0.1 C was 305 mAh (FIG. 5 is a charge-discharge curve of the lithium-ion half cell at 0.1 C), the discharge capacity at 1.0 C was 230 mAh to 240 mAh, and the capacity retention rate was 92% after 50 cycles.

Example 2

[0099] The aluminum-coated precursor was prepared by using the following method.

[0100] (1) Nickel chloride, cobalt chloride and manganese chloride were mixed in a nickel-cobalt-manganese molar ratio of 0.2:0.09:0.7 to obtain a mixed metal salt, where the concentrations of nickel chloride, cobalt chloride and manganese chloride in the mixed metal salt were all 300 g/L. Then in the presence of fructose as the conductive agent, carbon dioxide was continuously introduced at a flow rate of 0.5 L/min, the mixed metal salt and a sodium hydroxide solution with a concentration of 50 g/L were quickly mixed (the mixing was completed within 10 seconds, where the molar ratio of the mixed metal salt to sodium hydroxide was 1:3.5, and the amount of the conductive agent fructose was 30 g based on the total of 1 L of the mixed metal salt and sodium hydroxide), and the mixture was sealed and left to stand at 80° C. for 18 hours, so as to obtain pre-prepared particles with a particle size of 1.5 μm.

[0101] (2) The pre-prepared particles were mixed with water to obtain a slurry (with the solid content of 100 g/L), and then the coprecipitation reaction was performed with stirring (at a speed of 500 rpm). Meanwhile, the mixed metal salt (at a flow rate of 300 mL/h), sodium carbonate (in a concentration of 50 g/L to 200 g/L and at a flow rate of 250 mL/h to 350 mL/h) and carbon dioxide (at a flow rate of 0.4 mL/min) were continuously introduced, and the pH of the system was controlled to be 8. The reaction was performed for 50 hours, so as to obtain a reacted material with a solid content of 800 g/L.

[0102] (3) The reacted liquid was mixed with aluminum sulfate and then aged and stirred, so as to obtain an aged material, where the stirring was performed at a speed of 300 rpm and the aging was performed for 2 hours.

[0103] (4) The obtained aged material was successively subjected to iron removal, solid-liquid separation, washing and drying, so as to obtain an aluminum-coated precursor with a particle size of 10 μm, where the precursor had a chemical formula of (Mn.sub.0.7Ni.sub.0.2Co.sub.0.09)CO.sub.3.0.01Al(OH).sub.3 and a tap density of 1.8 g/cm.sup.3.

[0104] The cathode material was prepared in the following method.

[0105] In Sa, the aluminum-coated precursor obtained in step (4) and lithium carbonate were mixed in a molar ratio of 1:1.06 and then subjected to primary sintering at 500° C. in an air atmosphere for 5 hours, so as to obtain a primary sintered material.

[0106] In Sb, the obtained primary sintered material was crushed and then subjected to secondary sintering at 750° C. for 20 hours, so as to obtain a cathode material that had a chemical formula of Li(Li.sub.0.2Ni.sub.0.16Co.sub.0.07Mn.sub.0.56Al.sub.0.008)O.sub.2 and a compaction density of 3.1 g/cm.sup.3.

[0107] Conclusion: as can be seen from the scanning electron microscope image of the precursor material, the precursor material prepared by using the above-mentioned method had a spherical structure, uniform particle size distribution, and smooth surface, and it is further found from the detection of the particle size distribution by a laser particle size analyzer that the precursor had a uniform particle size distribution. Meanwhile, the cathode material was mixed with conductive agent carbon black (SP) and polyvinylidene fluoride (PVDF) and then stirred with N-methylpyrrolidone (NMP) as a solvent for several hours for pulping to prepare a lithium-ion half cell. The charge-discharge test was performed by using a LAND cell tester at 4.8 V, and it is found that the discharge capacity of per gram of the product at 0.1 C was 295 mAh to 305 mAh, the discharge capacity at 1.0 C was 230 mAh to 235 mAh, and the capacity retention rate was 88% after 50 cycles.

Example 3

[0108] The aluminum-coated precursor was prepared by using the following method.

[0109] (1) Nickel nitrate, cobalt nitrate and manganese nitrate were mixed in a nickel-cobalt-manganese molar ratio of 0.2:0.19:0.6 to obtain a mixed metal salt, where the concentrations of nickel nitrate, cobalt nitrate and manganese nitrate in the mixed metal salt were all 200 g/L. Then in the presence of glucose as the conductive agent, carbon dioxide was continuously introduced at a flow rate of 0.3 L/min, the mixed metal salt and a sodium carbonate solution with a concentration of 100 g/L were quickly mixed (the mixing was completed within 10 seconds, where the molar ratio of the mixed metal salt to sodium carbonate was 1:2.8, and the amount of the conductive agent glucose was 25 g based on the total of 1 L of the mixed metal salt and sodium hydroxide), and the mixture was sealed and left to stand at 50° C. for 20 hours, so as to obtain pre-prepared particles with a particle size of 1.8 m.

[0110] (2) The pre-prepared particles were mixed with water to obtain a slurry (with the solid content of 60 g/L), and then the coprecipitation reaction was performed with stirring (at a speed of 400 rpm). Meanwhile, the mixed metal salt (at a flow rate of 250 mL/h), sodium bicarbonate (in a concentration of 50 g/L to 200 g/L and at a flow rate of 200 mL/h to 300 mL/h), carbon dioxide (at a flow rate of 0.6 mL/min) and ammonia water as the complexing agent (in a concentration of 30 g/L) were continuously introduced, and the pH of the system was controlled to be 6.5. The reaction was performed for 50 hours, so as to obtain a reacted material with a solid content of 500 g/L.

[0111] (3) The reacted liquid was mixed with aluminum chloride and then aged and stirred, so as to obtain an aged material, where the stirring was performed at a speed of 300 rpm and the aging was performed for 2 hours.

[0112] (4) The obtained aged material was successively subjected to iron removal, solid-liquid separation, washing and drying, so as to obtain an aluminum-coated precursor with a particle size of 15 μm, where the precursor had a chemical formula of (Mn.sub.0.6Ni.sub.0.2Co.sub.0.19)CO.sub.3.0.01Al(OH).sub.3 and a tap density of 1.9 g/cm.sup.3.

[0113] The cathode material was prepared in the following method.

[0114] In Sa, the aluminum-coated precursor obtained in step (4) and lithium hydroxide were mixed in a molar ratio of 1:1.02 and then subjected to primary sintering at 550° C. in an air atmosphere for 5 hours, so as to obtain a primary sintered material.

[0115] In Sb, the obtained primary sintered material was crushed and then subjected to secondary sintering at 800° C. for 20 hours, so as to obtain a cathode material which had a chemical formula of Li(Li.sub.0.2Ni.sub.0.16Co.sub.0.15Mn.sub.0.48Al.sub.0.008)O.sub.2 and a compaction density of 3.2 g/cm.sup.3.

[0116] Conclusion: as can be seen from the scanning electron microscope image of the precursor material, the precursor material prepared by using the above-mentioned method had a spherical structure, uniform particle size distribution, and smooth surface, and it is further found from the detection of the particle size distribution by a laser particle size analyzer that the precursor had a uniform particle size distribution. Meanwhile, the cathode material was mixed with conductive agent carbon black (SP) and polyvinylidene fluoride (PVDF) and then stirred with N-methylpyrrolidone (NMP) as a solvent for several hours for pulping to prepare a lithium-ion half cell. The charge-discharge test was performed by using a LAND cell tester at 4.8 V, and it is found that the discharge capacity of per gram of the product at 0.1 C was 255 mAh to 260 mAh, the discharge capacity at 1.0 C was 205 mAh to 208 mAh, and the capacity retention rate was 84% after 50 cycles.