COMPOSITE SODIUM ION BATTERY CATHODE MATERIAL WITH RADIAL HETEROJUNCTION AND PREPARATION METHOD THEREOF

Abstract

A composite sodium ion battery cathode material with radial heterojunction and a preparation method thereof are provided. The cathode material is prepared by sintering a precursor and a sodium source, and the prepared cathode material is a core-shell structure with a radial heterojunction, the core of the cathode material is an O3-type nickel-manganese-based layered oxide, there is a coating material on the surface of the core, and the coating material is a P2-type nickel-manganese-based layered oxide. By adopting the above composite sodium ion battery cathode material with radial heterojunction and preparation method thereof, while reducing the cost of the materials, the composite cathode materials with radially heterogeneous distributions are synthesized by constructing different thicknesses of Ni.sub.0.3Mn.sub.0.7(OH).sub.2 on the surface of Ni.sub.0.5Mn.sub.0.5(OH).sub.2 precursor, so as to improve the air stability and cycling stability of the materials, and improve the sodium ion transmission kinetic property.

Claims

1. A preparation method for a composite sodium ion battery cathode material with a radial heterojunction, wherein the composite sodium ion battery cathode material with the radial heterojunction is prepared by sintering a precursor and a sodium source, the composite sodium ion battery cathode material with the radial heterojunction is a core-shell structure with the radial heterojunction, a core of the composite sodium ion battery cathode material with the radial heterojunction is an O3-type nickel-manganese-based layered oxide, a coating material is on a surface of the core of the composite sodium ion battery cathode material with the radial heterojunction, and the coating material is a P2-type nickel-manganese-based layered oxide, and a thickness of the coating material is less than 1 m; the precursor has the core-shell structure, a chemical formula of a core of the precursor is Ni.sub.0.5Mn.sub.0.5(OH).sub.2, and Ni.sub.0.3Mn.sub.0.7(OH).sub.2 is deposited on a surface of the core of the precursor; wherein the preparation method for the composite sodium ion battery cathode material with the radial heterojunction comprises the following steps: step 1, dissolving a nickel salt and a manganese salt in deionized water according to a proportion to obtain a first mixed solution and a second mixed solution respectively, preparing a precipitant solution by adding a precipitant into the deionized water to dissolve, and preparing a complexing agent solution by diluting a complexing agent to a predetermined concentration; step 2, simultaneously introducing the first mixed solution as a salt solution, the precipitant solution, and the complexing agent solution into a reaction kettle protected by a protective gas, maintaining a pH and a temperature in the reaction kettle, taking out a precursor material when a particle size of the precursor material reaches a requirement to obtain an extracted material, then switching the salt solution in the reaction kettle from the first mixed solution to the second mixed solution, and repeating operations of introducing, maintaining, taking out, and switching, wherein an ammonia concentration in the reaction kettle is maintained at 7.5 g/L; step 3, obtaining a precursor particle of Ni.sub.0.3Mn.sub.0.7(OH).sub.2 coated Ni.sub.0.5Mn.sub.0.5(OH).sub.2 of a corresponding size by washing and drying the extracted material, wherein a size of the Ni.sub.0.3Mn.sub.0.7(OH).sub.2 is x m, wherein 0x1; step 4, obtaining a mixed material by uniformly mixing the sodium source and the precursor particle according to a predetermined molar ratio, and uniformly mixing the sodium source and the precursor particle according to the predetermined molar ratio of Na:M=0.9:1; and step 5, firstly sintering the mixed material in an air atmosphere, secondly transferring the mixed material to an atmosphere furnace for a continued sintering, and finally synthesizing a series of cathode material Na.sub.xNi.sub.yMn.sub.2O.sub.2 samples.

2. The preparation method for the composite sodium ion battery cathode material with the radial heterojunction according to claim 1, wherein a particle size of the precursor material is 3.6-4.2 m.

3. The preparation method for the composite sodium ion battery cathode material with the radial heterojunction according to claim 1, wherein in the step 1, the nickel salt is one or more of nickel sulfate, nickel nitrate, and nickel chloride, the manganese salt is one or more of manganese sulfate, manganese nitrate, and manganese chloride, the precipitant is one or more of sodium hydroxide, sodium carbonate, sodium bicarbonate, potassium hydroxide, potassium carbonate, and potassium bicarbonate, and the complexing agent is one or more of ammonia and oxalic acid.

4. The preparation method for the composite sodium ion battery cathode material with the radial heterojunction according to claim 1, wherein a concentration of OH.sup./CO.sub.3.sup.2/HCO.sup.3 in the precipitant solution is 3-7 mol/L and a concentration of the complexing agent solution is 1.5-2 mol/L.

5. The preparation method for the composite sodium ion battery cathode material with the radial heterojunction according to claim 1, wherein a ratio of Ni and Mn in the first mixed solution is 1:1, a ratio of Ni and Mn in the second mixed solution is 3:7, and a concentration of the first mixed solution and a concentration of the second mixed solution are 3-10 mol/L.

6. The preparation method for the composite sodium ion battery cathode material with the radial heterojunction according to claim 1, wherein a capacity of the reaction kettle is 50 L, the protective gas is nitrogen or argon, and the pH in the reaction kettle is 11.0-11.6.

7. The preparation method for the composite sodium ion battery cathode material with the radial heterojunction according to claim 1, wherein in the step 4, the sodium source is one or more of Na.sub.2CO.sub.3, NaOH, and NaNO.sub.3.

8. The preparation method for the composite sodium ion battery cathode material with the radial heterojunction according to claim 1, wherein in the step 5, the mixed material is sintered at 500 C. for 6 h in the air atmosphere, and the mixed material is transferred to an oxygen atmosphere furnace and sintering at 900 C. for 24 h.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0027] FIG. 1 is a scanning electron microscope (SEM) view of a precursor prepared in embodiment 2 of a composite sodium ion battery cathode material with radial heterojunction and a preparation method thereof of the present invention;

[0028] FIG. 2 is an SEM view of a cathode material prepared in embodiment 2 of a composite sodium ion battery cathode material with radial heterojunction and a preparation method thereof of the present invention;

[0029] FIG. 3 is a partially enlarged SEM view of a precursor prepared in embodiment 2 of a composite sodium ion battery cathode material with radial heterojunction and a preparation method thereof of the present invention;

[0030] FIG. 4 is a partially enlarged SEM view of a cathode material prepared in embodiment 2 of a composite sodium ion battery cathode material with radial heterojunction and a preparation method thereof of the present invention;

[0031] FIG. 5 is an X-ray diffraction (XRD) pattern of a cathode material prepared in embodiment 2 of a composite sodium ion battery cathode material with radial heterojunction and a preparation method thereof of the present invention;

[0032] FIG. 6 is a diagram of a cycle performance comparison at 2.0-4.0V between embodiment 2 and comparative embodiment 1 of a composite sodium ion battery cathode material with radial heterojunction and a preparation method thereof of the present invention.

DETAILED DESCRIPTION OF THE EMBODIMENTS

[0033] The technical solution of the present invention will be further elaborated hereafter in conjunction with accompanying drawings and embodiments.

[0034] Unless otherwise defined, technical or scientific terms used in the present invention are to be given their ordinary meaning as understood by those of ordinary skill in the art to which the present invention belongs.

EMBODIMENT

[0035] The present invention provides the composite sodium ion battery cathode material with radial heterojunction, where the cathode material is prepared by sintering the precursor and the sodium source, the prepared cathode material is the core-shell structure with the radial heterojunction, the core of the cathode material is the O3-type nickel-manganese-based layered oxide, there is the coating material on the surface of the core, and the coating material is the P2-type nickel-manganese-based layered oxide, the thickness of the coating material is 0-1 m.

[0036] The particle size of the precursor material is 3.6-4.2 m, the precursor has the core-shell structure, the chemical formula of the core is Ni.sub.0.5Mn.sub.0.5(OH).sub.2, Ni.sub.0.3Mn.sub.0.7(OH).sub.2 is deposited on the surface of the core, and the size of the Ni.sub.0.3Mn.sub.0.7(OH).sub.2 is x m, wherein 0x1.

[0037] The present invention further provides the preparation method for the composite sodium ion battery cathode material with radial heterojunction, the preparation method includes the following steps: [0038] step 1, nickel salt and manganese salt were dissolved in deionized water according to proportion to obtain the first mixed solution and second mixed solution respectively, the precipitant solution was prepared by adding the precipitant into deionized water to dissolve, and the complexing agent solution was prepared by diluting the complexing agent to a certain concentration; nickel salts (such as nickel sulfate, nickel chloride, etc.) can increase the nickel content in the cathode material, thereby increasing the energy density of the battery. The increase in the proportion of nickel can make the battery store more electric energy and increase its endurance. The addition of manganese salts (such as manganese sulfate, manganese nitrate, etc.) can improve the structural stability and safety of cathode materials. Manganese can help to form a stable lattice structure and resist the structural changes caused by the charge-discharge cycle, thereby prolonging the battery life.

[0039] The ratio of Ni and Mn in the first mixed solution is 1:1, and the concentration of each solution is 2 M, the ratio of Ni and Mn in the second mixed solution is 3:7, and the concentration of each solution is 2 M, and both the concentration of the first mixed solution and the second mixed solution is 3-10 mol/L. By adjusting the ratio of nickel and manganese, the charge-discharge efficiency, cycle stability and rate performance of the battery can be optimized to meet the requirements of different application fields.

[0040] The nickel salt is one or more of nickel sulfate, nickel nitrate and nickel chloride, nickel sulfate is nickel sulfate hexahydrate, the manganese salt is one or more of manganese sulfate, manganese nitrate and manganese chloride, manganese sulfate is manganese sulfate monohydrate, the precipitant is one or more of sodium hydroxide, sodium carbonate, sodium bicarbonate, potassium hydroxide, potassium carbonate and potassium bicarbonate, and the complexing agent is one or more of ammonia and oxalic acid.

[0041] The concentration of OH.sup.+/CO.sub.3.sup.2/HCO.sup.3 in the precipitant solution is 3-7 mol/L, and the concentration of the complexing agent solution is 1.5-2 mol/L. The complexing agent can form a stable complex with the metal ions, and can also improve the solubility of the metal salt, and the precipitant can promote the prefabrication reaction of the metal ions in the solution to form precipitation insoluble in water.

[0042] Step 2, the first mixed solution, the precipitant solution and the complexing agent solution were simultaneously introduced into the reaction kettle protected by the protective gas, the pH and temperature were maintained in the reaction kettle, and the material was taken out when the particle size of the material reaches the requirement, and then the salt solution in the reaction kettle was switched from the first mixed solution to the second mixed solution, and the above operation was repeated.

[0043] Step 3, the precursor particles with different sizes were obtained by washing and drying the extracted materials, the precursor particles were Ni.sub.0.5Mn.sub.0.5(OH).sub.2 and different sizes of Ni.sub.0.3Mn.sub.0.7(OH).sub.2 coated precursor particles. In the reaction process of first mixed solution, when the particle size of the material reached 3.6 m, the material was taken out, in the reaction process of second mixed solution, when the particle size of the material reached 3.8 m, 4.0 m and 4.2 m, the materials were taken out respectively.

[0044] Step 4, the mixed material was obtained by uniformly mixing sodium source and precursor particles according to a certain molar ratio; the sodium source is one or more of Na.sub.2CO.sub.3, NaOH and NaNO.sub.3, and the sodium source and the precursor particles were uniformly mixed according to the molar ratio of Na:M=0.9:1.

[0045] Step 5, firstly the mixed material was sintered in the air atmosphere, secondly, it was transferred to the atmosphere furnace for continued sintering, and finally, a series of cathode material Na.sub.xNi.sub.yMn.sub.2O.sub.2 samples were synthesized, where the mixed material was first sintered at 500 C. for 6 h in the air atmosphere, and then transferred to the oxygen atmosphere furnace and sintered at 900 C. for 24 h, and the final synthesized cathode materials were denoted as NM, NM+0.2 m, NM+0.4 m and NM+0.6 m, respectively.

Embodiment 1

[0046] This embodiment prepares the composite sodium ion battery cathode material with radial heterojunction, including the following steps:

[0047] (1) nickel sulfate hexahydrate and manganese sulfate monohydrate were dissolved in deionized water according to the required ratio to obtain two mixed solutions. Where the Ni:Mn in the first mixed solution was 1:1, the Ni:Mn in the second mixed solution was 3:7, and the solution concentration was 2 M.

[0048] (2) Firstly, the first mixed solution, 4 M NaOH solution and 2 M NH.sub.3.Math.H.sub.2O solution were simultaneously introduced into the reactor with nitrogen as the protective gas, the pH in the reactor was maintained at 11.2, and the ammonia concentration was maintained at 7.5 g/L, when the particle size of the material in the reactor reached 3.6 m, 200 g of the material was taken out.

[0049] Then the first mixed solution was switched to the second mixed solution, the pH in the reactor was maintained at 11.2, and the ammonia concentration was maintained at 7.5 g/L, when the particle size of the material in the reactor reached 3.8 m, 200 g of material was taken out each time; the precursor particles were screened out after washing and drying, where the core of the precursor particles was Ni.sub.0.5Mn.sub.0.5(OH).sub.2, and Ni.sub.0.3Mn.sub.0.7(OH).sub.2 with a size of 0.2 m was deposited on the surface of the core.

[0050] (3) Na.sub.2CO.sub.3 and precursor particles were mixed uniformly according to the molar ratio of 0.9:1 (Na:M) to obtain the mixed material, the mixed material was first sintered at 500 C. for 6 h in the air atmosphere, and then transferred to the oxygen atmosphere furnace and sintered at 900 C. for 24 h. The cathode material sample can be obtained and denoted as NM+0.2 m.

[0051] (4) The specific capacity of the first cycle discharge and the capacity retention rate after 300 cycles of the composite sodium ion battery cathode material were measured.

Embodiment 2

[0052] This embodiment prepares the composite sodium ion battery cathode material with radial heterojunction, including the following steps:

[0053] (1) nickel sulfate hexahydrate and manganese sulfate monohydrate were dissolved in deionized water according to the required ratio to obtain two mixed solutions. Where the Ni:Mn in the first mixed solution was 1:1, the Ni:Mn in the second mixed solution was 3:7, and the solution concentration was 2 M.

[0054] (2) Firstly, the first mixed solution, 4 M NaOH solution and 2M NH.sub.3.Math.H.sub.2O solution were simultaneously introduced into the reactor with nitrogen as the protective gas, the pH in the reactor was maintained at 11.2, and the ammonia concentration was maintained at 7.5 g/L, when the particle size of the material in the reactor reached 3.6 m, 200 g of the material was taken out.

[0055] Then the first mixed solution was switched to the second mixed solution, the pH in the reactor was maintained at 11.2, and the ammonia concentration was maintained at 7.5 g/L, when the particle size of the material in the reactor reached 4.0 m, 200 g of material was taken out each time; the precursor particles were screened out after washing and drying, where the core of the precursor particles was Ni.sub.0.5Mn.sub.0.5(OH).sub.2, and Ni.sub.0.3Mn.sub.0.7(OH).sub.2 with a size of 0.4 m was deposited on the surface of the core.

[0056] (3) Na.sub.2CO.sub.3 and precursor particles were mixed uniformly according to the molar ratio of 0.9:1 (Na:M) to obtain the mixed material, the mixed material was first sintered at 500 C. for 6 h in the air atmosphere, and then transferred to the oxygen atmosphere furnace and sintered at 900 C. for 24 h. The cathode material sample can be obtained and denoted as NM+0.4 m.

[0057] (4) The specific capacity of the first cycle discharge and the capacity retention rate after 300 cycles of the composite sodium ion battery cathode material were measured.

[0058] FIG. 1 is the SEM view of the prepared precursor, FIG. 3 is the partially enlarged SEM view of the prepared precursor, it can be seen from the figure that the precursor particles were successfully prepared, and the prepared precursor had good particle morphology and distribution. FIG. 2 is the SEM view of the prepared cathode material, FIG. 4 is the partially enlarged SEM view of the prepared cathode material, FIG. 5 is the XRD pattern of the prepared cathode material, it can be seen from FIG. 2, FIG. 4 and FIG. 5 that the cathode material was successfully prepared, and the prepared precursor particles and the cathode material had a two-phase structure.

Embodiment 3

[0059] This embodiment prepares the composite sodium ion battery cathode material with radial heterojunction, including the following steps:

[0060] (1) nickel sulfate hexahydrate and manganese sulfate monohydrate were dissolved in deionized water according to the required ratio to obtain two mixed solutions. Where the Ni:Mn in the first mixed solution was 1:1, the Ni:Mn in the second mixed solution was 3:7, and the solution concentration was 2 M.

[0061] (2) Firstly, the first mixed solution, 4 M NaOH solution and 2 M NH.sub.3.Math.H.sub.2O solution were simultaneously introduced into the reactor with nitrogen as the protective gas, the pH in the reactor was maintained at 11.2, and the ammonia concentration was maintained at 7.5 g/L, when the particle size of the material in the reactor reached 3.6 m, 200 g of the material was taken out.

[0062] Then the first mixed solution was switched to the second mixed solution, the pH in the reactor was maintained at 11.2, and the ammonia concentration was maintained at 7.5 g/L, when the particle size of the material in the reactor reached 4.2 m, 200 g of material was taken out each time; the precursor particles were screened out after washing and drying, where the core of the precursor particles was Ni.sub.0.5Mn.sub.0.5(OH).sub.2, and Ni.sub.0.3Mn.sub.0.7(OH).sub.2 with a size of 0.6 m was deposited on the surface of the core.

[0063] (3) Na.sub.2CO.sub.3 and precursor particles were mixed uniformly according to the molar ratio of 0.9:1 (Na:M) to obtain the mixed material, the mixed material was first sintered at 500 C. for 6 h in the air atmosphere, and then transferred to the oxygen atmosphere furnace and sintered at 900 C. for 24 h. The cathode material sample can be obtained and denoted as NM+0.6 m.

[0064] (4) The specific capacity of the first cycle discharge and the capacity retention rate after 300 cycles of the composite sodium ion battery cathode material were measured.

Comparative Embodiment 1

[0065] The preparation for the sodium ion battery cathode materials includes the following steps:

[0066] (1) nickel sulfate hexahydrate and manganese sulfate monohydrate were dissolved in deionized water according to the required ratio to obtain two mixed solutions. Where the Ni:Mn in the first mixed solution was 1:1, the Ni:Mn in the second mixed solution was 3:7, and the solution concentration was 2 M.

[0067] (2) Firstly, the first mixed solution, 4 M NaOH solution and 2 M NH.sub.3.Math.H.sub.2O solution were simultaneously introduced into the reactor with nitrogen as the protective gas, the pH in the reactor was maintained at 11.2, and the ammonia concentration was maintained at 7.5 g/L, when the particle size of the material in the reactor reached 3.6 m, 200 g of the material was taken out; then the first mixed solution was switched to the second mixed solution, the pH in the reactor was maintained at 11.2, and the ammonia concentration was maintained at 7.5 g/L; the cathode material Ni.sub.0.5Mn.sub.0.5(OH).sub.2 were screened out after washing and drying, and denoted as NM.

[0068] (3) The specific capacity of the first cycle discharge and the capacity retention rate after 300 cycles of the composite sodium ion battery cathode material were measured.

[0069] The composite sodium ion battery cathode material with radial heterojunction obtained in embodiments 1-3 and the NM material obtained in the comparative embodiment 1 are used as the positive electrode, and the lithium metal sheet is used as the negative electrode, they are assembled into button batteries for charge and discharge comparison tests, the test results are as follows:

TABLE-US-00001 TABLE 1 Discharge specific capacity test data of battery cathode material Specific capacity of Capacity retention first cycle discharge rate after 300 at 1 C rate (mAh/g) cycles (%) Embodiment 1 119.61 40.61 Embodiment 2 109.85 64.61 Embodiment 3 103.32 51.46 Comparative embodiment 1 134.82 11.69

[0070] From Table 1, it can be concluded that the button battery is assembled for charge and discharge comparison test based on the composite sodium ion battery cathode material with radial heterojunction obtained in embodiments 1-3 is the positive electrode, and the lithium metal sheet is the negative electrode, the specific capacity of the first cycle discharge is up to 119.61 mAh/g at 1C rate, and the capacity retention rate is up to 64.61 after 300 cycles, although the specific capacity of the first cycle discharge of the NM material obtained by the comparative embodiment 1 as the positive electrode reaches 134.82 mAh/g, the capacity retention rate after 300 cycles is only 11.69%.

[0071] It can be seen that the cycle stability of the battery made of the composite sodium ion battery cathode material with radial heterojunction is much higher than that of the battery made of the cathode material of the ordinary sodium ion battery, and from a comprehensive point of view, the battery made of the composite sodium ion battery cathode material with radial heterojunction is superior to the battery made of the cathode material of the ordinary sodium ion battery, and the optimum thickness of the coating material of the composite sodium ion battery cathode material with radial heterojunction is 0.4 m.

[0072] FIG. 6 is the diagram of the cycle performance comparison at 2.0-4.0 V between embodiment 2 and comparative embodiment 1, it can be seen from the figure that embodiment 2 performs well under long-cycle conditions and can maintain higher specific energy.

[0073] Therefore, the present invention adopts the above composite sodium ion battery cathode material with radial heterojunction and the preparation method thereof, while reducing the cost of the materials, the composite cathode materials with radially heterogeneous distributions are synthesized by constructing different thicknesses of Ni.sub.0.3Mn.sub.0.7(OH).sub.2 on the surface of Ni.sub.0.5Mn.sub.0.5(OH).sub.2 precursor, so as to improve the air stability and cycling stability of the materials, and improve the sodium ion transmission kinetic property, the present invention is low-cost, simple and reasonable, with good electrical properties, and is suitable for commercialized production.

[0074] Finally, it should be noted that the above examples are merely used for describing the technical solutions of the present invention, rather than limiting the same. Although the present invention has been described in detail with reference to the preferred examples, those of ordinary skill in the art should understand that the technical solutions of the present invention may still be modified or equivalently replaced. However, these modifications or substitutions should not make the modified technical solutions deviate from the spirit and scope of the technical solutions of the present invention.