Positive electrode active material for sodium secondary batteries, method for manufacturing the same, positive electrode for sodium secondary batteries, and sodium secondary batteries containing the same

Abstract

To provide a positive electrode active material with excellent initial capacity and excellent lifespan characteristics.SOLUTION: One embodiment of the present invention provides a positive electrode active material for a sodium secondary battery, including P2-type layered oxide particles and O3-type layered oxide particles. In SEM-EDS mapping analysis, the ratio (S3 / S2) of the surface Na content (at.%) (S3) of the O3-type layered oxide particles to a surface Na content (at.%) (S2) of the P2-type layered oxide particles is 0.4 to 1.6.SELECTED DRAWING: Figure 1b

Description

[Technical Field]

[0001] The present invention relates to a positive electrode active material for a sodium secondary battery, a method for producing the same, a positive electrode for a sodium secondary battery, and a sodium secondary battery containing the same. [Background technology]

[0002] Lithium-ion rechargeable batteries have been widely used as energy storage devices in various fields of electronics technology. Recently, with the surge in demand for lithium-ion rechargeable batteries, sodium-ion rechargeable batteries are attracting attention as an alternative to expensive metallic lithium. Sodium-ion rechargeable batteries have an insertion-deletion reaction operating principle similar to that of lithium-ion rechargeable batteries, making them one of the next-generation materials with high potential for application in rechargeable batteries.

[0003] Typically, transition metal oxides with a layered structure are used as positive electrode active materials for sodium-ion secondary batteries because they have a simple structure, excellent electrochemical performance, and are easy to synthesize. Generally, O3-type layered oxides have an even higher energy density than P2-type layered oxide particles, but they have the disadvantage of undergoing even larger structural changes during the charge-discharge process, resulting in reduced cycle stability. P2-type layered oxides have relatively good cycle stability, but their low sodium content and relatively low energy density make them difficult to apply commercially.

[0004] There are attempts to develop a product with excellent initial capacity and lifetime characteristics by simultaneously creating a mixture of P2-type oxide particles and O3-type oxide particles, where the O3-type layered oxide provides relatively high discharge capacity, and the P2-type layered oxide suppresses the structural changes that occur when a relatively large number of sodium ions escape.

[0005] However, simply applying a mixed phase makes it difficult to achieve the target battery performance. Furthermore, when O3-type oxide particles are washed with water to remove residual Na from the surface, it is difficult to overcome the problem that all the Na inside escapes, causing the particle structure to be compromised. Consequently, it is difficult to solve the problem of reduced battery life and stability caused by sodium byproducts present on the particle surface in the form of Na2CO3 and NaOH, which lead to gas generation due to electrolyte side reactions during battery operation, and a decrease in the capacity and output of the positive electrode active material. [Prior art documents] [Patent Documents]

[0006] [Patent Document 1] China Patent Publication CN 115692681 A [Patent Document 2] China Patent Publication CN 113839018 A [Patent Document 3] China Patent Publication CN 116002717 A [Overview of the project] [Problems that the invention aims to solve]

[0007] The object of the present invention is to provide a cathode active material that exhibits excellent initial capacity and excellent lifetime characteristics when used in combination with P2-type and O3-type particles, by inducing Na migration from the surface of the O3-type oxide particles to the surface of the P2-type oxide particles by manufacturing P2-type particles and O3-type particles separately, and then mixing and firing them.

[0008] Furthermore, the present invention aims to improve the problem of the particle structure of O3-type layered oxide particles collapsing and undergoing phase transition to P3-type by controlling the ratio (S3 / S2) of the surface Na content (at%) (S2) of P2-type layered oxide particles to the surface Na content (at%) (S3) of O3-type layered oxide particles. Furthermore, the present invention aims to provide a technique for selectively adjusting only the surface Na content while maintaining the total Na equivalent for both P2-type particles and O3-type particles. [Means for solving the problem]

[0009] One embodiment of the present invention provides a positive electrode active material for a sodium secondary battery, comprising P2-type layered oxide particles and O3-type layered oxide particles, characterized in that, in SEM-EDS mapping analysis, the ratio of the surface Na content (at%) (S3) of the O3-type layered oxide particles to the surface Na content (at%) (S2) of the P2-type layered oxide particles (S3 / S2) is 0.4 to 1.6.

[0010] The ratio (S3 / S2) of the surface Na content (at%) (S3) of the O3-type layered oxide particles to the surface Na content (at%) (S2) of the P2-type layered oxide particles may be 0.65 to 1.45. In SEM-EDS mapping analysis, the surface Na content (at%) (S2) of the P2-type layered oxide particles may be 14.5 to 21.5 at%, and the surface Na content (at%) (S3) of the O3-type layered oxide particles may be 7.5 to 21.5 at%.

[0011] The surface Na content (at%) (S2) of the P2-type layered oxide particles may be 14.5 to 21.5 at%, and the surface Na content (at%) (S3) of the O3-type layered oxide particles may be 14.5 to 21.5 at%.

[0012] The P2-type layered oxide may be represented by the following chemical formula 1, and the O3-type layered oxide may be represented by the following chemical formula 2. [ka] In the aforementioned chemical formula 1, M1 is at least one selected from P, Sr, Ba, Ti, Zr, W, Co, Mg, Al, Cu, Zn, Ce, Hf, Ta, F, Cr, V, Si, Fe, Y, Ga, Sn, Mo, Ge, Nd, B, Nb, and Gd. 0.44 <a<0.80、0.05≦x≦0.45、0.05≦y≦0.15、0.45<1-x-y≦0.9である。 [Chemical formula] In the above Chemical formula 2, M1 is at least one selected from the group consisting of Fe and Mn, M2 is at least one selected from P, Sr, Ba, Ti, Zr, W, Co, Mg, Al, Cu, Zn, Ce, Hf, Ta, F, Cr, V, Si, Fe, Y, Ga, Sn, Mo, Ge, Nd, B, Nb and Gd, 0.80 < a < 1.1, 0.05 ≤ x ≤ 0.45, 0.05 ≤ y ≤ 0.45, 0.05 ≤ z ≤ 0.15, 0.05 < 1 - x - y - z ≤ 0.45.

[0013] The P2-type layered oxide may have a Na equivalent (Na / M ratio) of 0.60 to 0.70, and the O3-type layered oxide may have a Na equivalent (Na / M ratio) of 0.90 to 1.05.

[0014] The P2-type layered oxide particles and the O3-type layered oxide particles may be contained in a weight ratio of 8:2 to 2:8.

[0015] The positive electrode active material may not show a NiOx peak by XRD analysis. The positive electrode active material may have a residual Na content (TTS, Total Sodium) of 500 to 10,000 ppm.

[0016] The positive electrode active material may be manufactured by mixing P2-type layered oxide particles and O3-type layered oxide particles and firing the mixed oxide particles.

[0017] Another embodiment of the present invention provides a method for manufacturing a positive electrode active material for a sodium secondary battery, which comprises mixing P2-type layered oxide particles and O-type layered oxide particles and firing the mixed oxide particles.

[0018] Before proceeding with the firing process, the P2-type layered oxide particles and O3-type layered oxide particles may not be washed with water to remove residual Na from their surfaces.

[0019] The P2-type layered oxide particles and O3-type layered oxide particles may be mixed in a weight ratio of 8:2 to 2:8. The firing process may be carried out at a temperature of 400 to 1,000°C for 3 to 16 hours.

[0020] Another embodiment of the present invention provides a positive electrode for a sodium secondary battery containing a positive electrode active material, and a sodium secondary battery containing the positive electrode and a negative electrode. [Effects of the Invention]

[0021] According to the present invention, P2 type particles can replenish surface Na lost by washing with water or due to an overall low Na content, and O3 type particles can effectively remove residual Na without structural breakdown.

[0022] Furthermore, O3-type oxide particles have inherently low structural stability regardless of the adjustment of the total Na equivalent. Therefore, when washing with water to remove residual Na, there is a problem in that all the internal Na escapes, preventing the structure from being maintained. However, in the present invention, residual Na can be effectively removed from O3-type oxide particles.

[0023] Furthermore, the present invention can control excessive Na migration from O3-type oxide particles to P2-type oxide particles, thereby improving the problem of the particle structure of O3-type particles collapsing and undergoing phase change to the P3 type. [Brief explanation of the drawing]

[0024] [Figure 1a] This shows the results of SEM-EDS mapping analysis of the particle surface of a mixture of P2-type oxide particles and O3-type oxide particles produced in Example 1, before secondary calcination. [Figure 1b]This shows the results of SEM-EDS mapping analysis of the particle surface after secondary calcination of a mixture of P2-type oxide particles and O3-type oxide particles produced in Example 1. [Figure 2a] This shows the results of SEM-EDS mapping analysis of the particle surface of the mixture of P2-type oxide particles and O3-type oxide particles produced in Example 3, before secondary calcination. [Figure 2b] This shows the results of SEM-EDS mapping analysis of the particle surface after secondary calcination of a mixture of P2-type oxide particles and O3-type oxide particles produced in Example 3. [Figure 3a] These are the XRD peak analysis results before and after calcination (secondary calcination) of a mixture of P2-type oxide particles and O3-type oxide particles produced in Example 1. [Figure 3b] These are the XRD peak analysis results before and after calcination (secondary calcination) of the mixture of P2-type oxide particles and O3-type oxide particles produced in Example 2. [Figure 3c] These are the XRD peak analysis results before and after calcination (secondary calcination) of the mixture of P2-type oxide particles and O3-type oxide particles produced in Example 3. [Figure 4a] This is a graph showing the measured residual sodium content (TTS) before and after secondary firing. [Figure 4b] This graph shows the measured primary charge capacity (CH), primary discharge capacity (DCH), and initial efficiency (ICE) before and after secondary firing. [Figure 5] This shows the results of XRD peak shift analysis of the positive electrode active material depending on whether or not secondary firing was applied at different temperatures. [Figure 6] This graph analyzes the life characteristics of sodium secondary batteries based on the application of secondary firing at different temperatures. [Figure 7] This is a graph showing the gas generation measurement of a sodium secondary battery with and without the application of secondary firing in Example 1. [Modes for carrying out the invention]

[0025] The advantages and features of the present invention, and the methods for achieving them, will become clearer with reference to the embodiments described below in detail, along with the accompanying drawings. However, the present invention is not limited to the embodiments disclosed below, but can be embodied in a variety of different forms, and these embodiments are provided only to complete the disclosure of the present invention and to fully inform those who are ordinary skill in the art to which the present invention pertains, and the present invention is defined only by the scope of the claims.

[0026] Unless otherwise defined, all terms used herein (including technical and scientific terms) may be used in a way that is commonly understood by a person of ordinary skill in the art to which the invention pertains. Wherever any part of the specification “includes” a certain component, this means, unless otherwise stated, that it does not exclude other components, but rather that it may include other components. Furthermore, unless otherwise specified in the statement, singular forms also include plural forms.

[0027] One embodiment of the present invention provides a positive electrode active material for a sodium secondary battery. The positive electrode active material comprises P2-type layered oxide particles and O3-type layered oxide particles.

[0028] P2-type layered oxides have excellent lifetime properties due to their structural stability, but suffer from a low initial capacity due to their low Na content. O3-type layered oxides have a high initial capacity due to their high Na content, but suffer from poor structural stability and a low Na migration rate due to the relatively small size of the octahedral positions in the structure where Na can be located, resulting in degraded lifetime properties. In this invention, a positive electrode active material can be provided that maintains the advantages of each particle while improving their disadvantages by mixing P2-type and O3-type layered oxide particles and firing them.

[0029] The positive electrode active material of the present invention is characterized in that, in SEM-EDS mapping analysis, the ratio (S3 / S2) of the surface Na content (at%) (S3) of O3-type layered oxide particles to the surface Na content (at%) (S2) of P2-type layered oxide particles is 0.4 to 1.6.

[0030] These structural characteristics are the result of inducing Na migration from the surface of the O3 oxide particles to the surface of the P2 oxide particles by mixing and calcining P2-type and O3-type particles after manufacturing them separately. As a result, the P2-type particles can replenish the surface Na lost through washing or due to the overall low Na content, and the O3-type particles can effectively remove residual Na without structural collapse.

[0031] Unlike the present invention, even if particles are manufactured by increasing the total Na equivalent of P2-type particles and decreasing the total Na equivalent of O3-type particles, the range of Na equivalents required to maintain the P2 and O3 phases is limited. Furthermore, considering the difficulty in selectively adjusting only the surface Na content while maintaining the total Na equivalent, it is difficult to control the surface Na content ratio of O3 / P2 particles within the range of the present invention. Additionally, O3-type oxide particles have inherently low structural stability regardless of the adjustment of the total Na equivalent. Therefore, when washing with water to remove residual Na, there is a problem in that all the internal Na escapes, preventing the structure from being maintained. However, the present invention can effectively remove residual Na from O3-type oxide particles.

[0032] Specifically, it is preferable that the ratio of the surface Na content (at%) (S3) of the O3-type layered oxide particles to the surface Na content (at%) (S2) of the P2-type layered oxide particles (S3 / S2) is 0.65 to 1.45. If the S3 / S2 ratio becomes excessively low, excessive Na migration from the O3-type oxide particles to the P2-type oxide particles occurs, causing the O3-type particles to collapse in structure and undergo phase change to the P3-type.

[0033] In SEM-EDS elemental mapping analysis, the surface Na content (at%) (S2) of the P2-type layered oxide particles may be 14.5 to 21.5 at%, specifically 15 to 21 at%, 16 to 20 at%, or 17 to 19 at%. Furthermore, the surface Na content (at%) (S3) of the O3-type layered oxide particles may be 7.5 to 21.5 at%, specifically 8 to 21 at%, 14.5 to 21.5 at%, 15 to 21 at%, 16 to 20 at%, or 17 to 19 at%. This further improves the aforementioned effects.

[0034] In both P2 and O3 type layered oxides, if the surface Na content exceeds the design range, the residual Na content can increase proportionally, potentially leading to increased electrolyte side reactions and gas generation due to residual Na within the upper voltage limit (~4.3V). Conversely, if the surface Na content is below the design range, internal Na on the particle surface may escape, potentially causing problems in maintaining the crystalline structure.

[0035] Furthermore, SEM-EDS elemental mapping analysis may be performed at a voltage intensity of 10 to 20 kV, preferably 15 kV. The detection depth (region) and target elements can be identified from the surface to the interior of the particles by the set voltage intensity. In this invention, EDS elemental mapping analysis is performed at a voltage intensity within the design range to measure the change in the percentage of Na atoms on the surface of P2 and O3 type particles under the same analytical conditions. In this case, the particle surface can be slightly changed by the voltage intensity, and the invention is not limited to a specific depth (length, region).

[0036] The P2-type layered oxide may be represented by the following chemical formula 1, and the O3-type layered oxide may be represented by the following chemical formula 2. [ka] In the aforementioned chemical formula 1, M1 is at least one selected from P, Sr, Ba, Ti, Zr, W, Co, Mg, Al, Cu, Zn, Ce, Hf, Ta, F, Cr, V, Si, Fe, Y, Ga, Sn, Mo, Ge, Nd, B, Nb, and Gd, and 0.44 <a<0.80、0.05≦x≦0.45、0.05≦y≦0.15、0.45<1-x-y≦0.9である。 When the Na equivalent of the P2-type layered oxide is 0.44 or less (a ≤ 0.44), the oxide has a three-dimensional tunnel structure, and its electrochemical properties may deteriorate due to the arrangement of lattice units. Conversely, when the Na equivalent is 0.80 or more (0.80 ≤ a), the oxide has a layered O3 structure, which has the disadvantage of reduced atmospheric and moisture stability and sensitivity to synthesis conditions such as temperature and atmosphere. [ka] In the above chemical formula 2, M1 is at least one selected from the group consisting of Fe and Mn, and M2 is at least one selected from P, Sr, Ba, Ti, Zr, W, Co, Mg, Al, Cu, Zn, Ce, Hf, Ta, F, Cr, V, Si, Fe, Y, Ga, Sn, Mo, Ge, Nd, B, Nb and Gd, and 0.80 <a<1.1、0.05≦x≦0.45、0.05≦y≦0.45、0.05≦z≦0.15、0.05<1-x-y-z≦0.45である。

[0037] When the Na equivalent of the aforementioned O3-type layered oxide is less than 0.80 (a < 0.80), the oxide has a P3-type structure, and its electrochemical properties may deteriorate due to the arrangement of lattice units. Conversely, when the Na equivalent is 1.10 or more (0.10 ≤ a), it has the disadvantage of reduced atmospheric and moisture stability and sensitivity to synthesis conditions such as temperature and atmosphere.

[0038] The P2-type layered oxide may have a Na equivalent (Na / M ratio) of 0.60 to 0.70, and the O3-type layered oxide may have a Na equivalent (Na / M ratio) of 0.90 to 1.05. This can further improve the effects described above.

[0039] The P2-type layered oxide particles and O3-type layered oxide particles may be present in a weight ratio of 8:2 to 2:8. Specifically, weight ratios of 8:2 to 4:6, 8:2 to 5:5, or 8:2 to 6:4 are preferred. If the content of O3-type particles is somewhat low, the overall volume characteristics deteriorate, and conversely, if it is somewhat high, even if Na migration proceeds, the residual Na content is high, leading to problems such as the possibility of thick CEI (Cathode-Electrolyte Interface) formation, decreased ICE, and gas generation. Furthermore, when the above-mentioned preferred content range is met, an ICE of 90% or more and sufficient volume characteristics can be ensured.

[0040] The positive electrode active material is characterized by the absence of a NiOx peak when analyzed by XRD. In P2 type particles, the NiOx crystalline phase is easily synthesized on the surface of particles that have been lost by washing with water or due to the overall low Na content. However, in the present invention, the surface of P2 type particles can be replenished by Na migration by O3 type particles, thereby preventing the synthesis of crystalline phases such as NiOx.

[0041] The positive electrode active material of the present invention can reduce the residual Na content (TTS, Total Sodium) to 500-10,000 ppm, specifically to 500-9,500 ppm, 500-9,000 ppm, 1,000-9,000 ppm, or 5,000-9,000 ppm. This suppresses gas generation caused by residual Na, significantly improving battery life characteristics.

[0042] The residual sodium content (TTS, Total Sodium) may also be the value obtained by separately calculating the total amount of sodium only from the residual sodium-containing compounds (for example, NaOH or Na2CO3).

[0043] Another embodiment of the present invention provides a method for producing a positive electrode active material for a sodium secondary battery, characterized by mixing P2-type layered oxide particles and O3-type layered oxide particles and firing the mixed oxide particles.

[0044] The mixing of the aforementioned particles can be carried out using the weight ratios described above, and the mixing method can be applied without limitation as long as it is a method known in the art. The P2-type layered oxide particles and O3-type layered oxide particles are the same as those described above, and any particles obtained by a manufacturing method known in the art can be used without limitation.

[0045] Furthermore, the P2-type layered oxide particles may undergo water washing to remove residual Na from their surface, while the O3-type layered oxide particles may not undergo water washing to remove residual Na from their surface. The P2-type layered oxide has high structural stability and can be washed with water, but the O3-type layered oxide is difficult to wash with water because its structure is likely to collapse during washing.

[0046] Furthermore, both the P2-type layered oxide particles and the O3-type layered oxide particles are preferable when water washing to remove residual Na from the surface is not performed. For this reason, in the case of P2-type layered oxide particles, the P2 structure is synthesized with a low Na equivalent (0.65, 0.60, 0.55, etc.), and in the subsequent second calcination step, the phenomenon of surface Na migration of the O3-type layered oxide (moving Na from high concentration to low concentration) is utilized to replenish the deficient Na.

[0047] The calcination of the mixed oxide particles may be carried out at a temperature of 400 to 1,000°C for 4 to 16 hours, and more specifically, at a temperature of 500 to 1,000°C, 600 to 1,000°C, or 700 to 1,000°C in an air atmosphere for 6 to 16 hours, 8 to 16 hours, or 10 to 14 hours.

[0048] If the firing temperature or firing time is below the lower limit, the desired phase may not be sufficiently synthesized, and if it exceeds the upper limit, the Na that has entered the lattice may further leach to the surface.

[0049] Through the process described above, Na migration can proceed from the surface of O3 type oxide particles to the surface of P2 type oxide particles. As a result, the P2 type particles can replenish the surface Na lost through washing or due to the overall low Na content, and the O3 type particles can effectively remove residual Na without structural collapse, thereby improving battery performance such as capacity characteristics, efficiency characteristics, and lifespan characteristics.

[0050] Another embodiment of the present invention provides a positive electrode for a sodium secondary battery and a sodium secondary battery, both containing the positive electrode active material.

[0051] The positive electrode includes a positive electrode current collector and a positive electrode active material layer located on the positive electrode current collector, and the positive electrode active material according to one aspect of the present invention is present in the positive electrode active material layer.

[0052] The positive electrode current collector is not particularly limited as long as it is conductive without inducing chemical changes in the battery. For example, stainless steel, aluminum, nickel, titanium, calcined carbon, or aluminum or stainless steel surfaces treated with carbon, nickel, titanium, silver, etc., can be used. The positive electrode current collector can also typically have a thickness of 3 to 500 μm, and fine irregularities can be formed on the surface of the current collector to enhance the adhesion of the positive electrode active material. Such positive electrode current collectors can be provided in various forms such as films, sheets, foils, nets, porous materials, foams, and nonwoven fabrics.

[0053] Furthermore, the positive electrode active material layer may also be a layer containing a conductive material and a binder along with the aforementioned positive electrode active material.

[0054] Here, the conductive material is used to impart conductivity to the electrode and can be used without special restrictions as long as it is conductive without causing a chemical change in the positive electrode active material. Non-restrictive examples of conductive materials include graphite such as natural graphite and artificial graphite; carbon-based materials such as carbon black, acetylene black, Ketjen black, channel black, furnace black, lamp black, thermal black, and carbon fiber; metal powders or metal fibers such as copper, nickel, aluminum, and silver; conductive whiskers such as zinc oxide and potassium titanate; conductive metal oxides such as titanium oxide; and conductive polymers such as polyphenylene derivatives. The conductive material may usually be included in an amount of 1% to 30% by weight based on the total weight of the positive electrode active material layer.

[0055] Furthermore, the binder is a substance that improves the adhesion between positive electrode active material particles and the adhesion between the positive electrode active material and the current collector. Non-limiting examples of binders include polyvinylidene fluoride (PVDF), vinylidene fluoride-hexafluoropropylene copolymer (PVDF-co-HFP), polyvinyl alcohol, polyacrylonitrile, carboxymethylcellulose (CMC), starch, hydroxypropylcellulose, regenerated cellulose, polyvinylpyrrolidone, tetrafluoroethylene, polyethylene, polypropylene, ethylene-propylene-diene polymer (EPDM), sulfonated-EPDM, styrene-butadiene rubber (SBR), fluororubber, or various copolymers thereof. The binder may typically be present in an amount of 1% to 30% by weight based on the total weight of the positive electrode active material layer.

[0056] A positive electrode according to one embodiment of the present invention can be manufactured by a conventional method for manufacturing a positive electrode for a sodium secondary battery, except that the positive electrode active material described above is used. For example, a positive electrode can be manufactured by applying a slurry for forming a positive electrode active material layer, which includes the positive electrode active material and selectively a binder and a conductive material, onto a positive electrode current collector, followed by drying and rolling. In another example, a positive electrode can be manufactured by casting the slurry for forming a positive electrode active material layer onto a separate support, peeling the positive electrode active material layer from the support, and then laminating the resulting film onto a positive electrode current collector.

[0057] According to yet another aspect of the present invention, an electrochemical element including the aforementioned positive electrode is provided. Here, the electrochemical element may be a battery, a capacitor, or more specifically, a sodium secondary battery.

[0058] A sodium-based secondary battery includes a positive electrode, a negative electrode positioned opposite the positive electrode, a separator interposed between the positive and negative electrodes, and an electrolyte. The sodium-based secondary battery may also include a battery container (case) housing the electrode assembly, including the positive electrode, negative electrode, and separator, and a sealing member for sealing the battery container.

[0059] At this time, depending on the shape of the battery container (case), the sodium secondary battery can be classified into a can type sodium secondary battery in which the electrode assembly is built in a metal can and a pouch type sodium secondary battery in which the electrode assembly is built in a pouch made of a sheet such as aluminum laminate.

[0060] Particularly, in the case of a pouch type sodium secondary battery using a positive electrode containing a positive electrode active material according to various embodiments of the present invention, since there is little possibility of a side reaction between the positive electrode active material and the electrolyte, the stability is improved during storage and / or operation, and at the same time, there is an advantage that gas generation can be reduced.

[0061] Hereinafter, the present invention will be described in detail based on examples, but these are for explaining the present invention in more detail, and the scope of rights of the present invention is not limited by the following examples. Examples (Example 1) Ni 0.35 Mn 0.65 Sodium compound Na2CO3 was added to the (OH)2 precursor at Na / M = 0.65 equivalent, and calcined at 950 °C for 6 hours in an air atmosphere to produce P2-type layered oxide particles (Na 0.65 Ni 0.35 Mn 0.65 O2 powder).

[0062] Ni 0.33 Fe 0.33 Mn 0.33 Sodium compound Na2CO3 was added to the (OH)2 precursor at Na / M = 1.05 equivalent, and calcined at 950 °C for 12 hours in an air atmosphere to produce O3-type layered oxide particles (Na 1.05 Ni 0.33 Fe 0.33 Mn 0.33 O2 powder).

[0063] The manufactured P2-type oxide particles and O3-type oxide particles were mixed in a 7:3 weight ratio and subjected to secondary calcination at 800°C in an air atmosphere for 6 hours to produce the positive electrode active material. A cathode slurry was prepared by dispersing 30 g of 96 wt% of the manufactured cathode active material, 2 wt% of carbon black, and 2 wt% of PVdF binder in N-methyl-2-pyrrolidone (NMP). The cathode slurry was uniformly coated onto a 15 μm thick aluminum thin film and vacuum-dried at 135°C to produce a cathode for a sodium secondary battery.

[0064] A sodium secondary battery (coin cell) was manufactured using a sodium metal plate as the counter electrode to the positive electrode, a porous polyethylene membrane (Celgard 2300, thickness: 25 μm) as the separation membrane, and an electrolyte containing ethylene carbonate and ethyl methyl carbonate mixed in a volume ratio of 3:7 with NaPF6 present at a concentration of 1.15 M.

[0065] (Examples 2-3) When producing P2-type layered oxide particles, Na / M was set to 0.55 equivalents (Example 2) and 0.45 equivalents (Example 3), respectively. 0.55 Ni 0.35 Mn 0.65 O2 (Example 2), Na 0.45 Ni 0.35 Mn 0.65 Except for producing O2 (Example 3) particles, the process was the same as in Example 1 to produce the positive electrode active material and the sodium secondary battery.

[0066] Experimental example Experimental Example 1: SEM-EDS Mapping Analysis of Cathode Active Material Particles After mixing the P2-type oxide particles and O3-type oxide particles produced in Examples 1 and 3, surface SEM-EDS mapping analysis of the particles was performed at a voltage intensity of 15 kV before and after secondary calcination. (Example 1) Before / After Secondary Firing: Figure 1a / Figure 1b (Example 3) Before / After Secondary Firing: Figure 2a / Figure 2b [Table 1] Referring to Figures 1a and 1b (Example 1) and Figures 2a and 2b (Example 3), a Na migration phenomenon was observed in both Example 1 and Example 3 after firing, from the surface of the O3-type oxide particles to the surface of the P2-type oxide particles. It was confirmed that residual Na from the O3-type particles migrated to the surface of the P2-type particles through secondary firing, allowing the P2-type particles to replenish the surface Na lost by washing, and that residual Na could be effectively removed from the O3-type particles without structural collapse.

[0067] Referring to Table 1, in Example 1, the ratio of Na content on the surface of O3-type particles / P2-type particles decreased from 1.67-2.6 to 0.7-1.4 after firing, which was lower than the ratio of total Na equivalent (O3-type particles / P2-type particles total) of 1.62. Therefore, it was confirmed that P2-type particles replenish Na on their surface, improving the problem of low initial capacity due to low Na levels, and O3-type particles stably reduce Na on their surface without generating particle surface defects or structural collapse, improving the problem of poor structural stability and low Na migration rate due to the small size of the octahedral positions where Na can be located. Furthermore, the reduced residual Na also has the effect of improving electrolyte side reactions and gas generation problems.

[0068] In Example 3, it was confirmed that Na migration proceeded somewhat excessively after secondary calcination, and the ratio of Na content on the surface of O3-type particles to P2-type particles decreased to a somewhat low range of 0.4 to 0.93. As a result, the O3-type particles underwent a collapse of their particle structure and could undergo phase change to the P3-type.

[0069] Experimental Example 2: XRD Peak Shift Analysis XRD peak analysis was performed before and after calcination (secondary calcination) of the P2-type oxide particles and O3-type oxide particles produced in Examples 1-3, and the results are shown in Table 2 and Figure 3 below.

[0070] Referring to Figure 3, the migration phenomenon can be demonstrated from the XRD shift results. Residual Na on the O3 surface enters the P2 structure, causing the P2(002) peak to shift to the right (high angle). During heat treatment, not only the residual Na in O3 moves, but also some Na within the O3 lattice, causing the (003) peak of the O3 structure to shift to the left (low angle). Therefore, the stability of both the P2 and O3 structures can be improved.

[0071] Based on the peak shift (increase) of the P2-type particles (on the 002 plane), it is calculated that the final Na / M equivalent of P2 converges to 0.68-0.66 in Examples 1-3, and based on the peak shift (decrease) of the O3-type particles (on the 003 plane), it is calculated that the final Na / M equivalent of O3 converges to 0.9-1.0.

[0072] However, the lower the Na equivalent of the P2-type particles, the greater the tendency for Na migration from O3-type particles to P2-type particles during firing after mixing the P2 / O3 particles. When the P2-type particles contain 0.45 Na equivalents, excessive Na migration occurs, and structural collapse of the O3-type particles is expected.

[0073] Experimental Example 3: Evaluation of battery performance based on the mixing ratio of P2-type and O3-type particles Except for the fact that the P2-type particles and O3-type particles were manufactured in the mixing ratios shown in Table 2 below in Example 1, the positive electrode active material and sodium secondary battery were manufactured in the same manner. The residual Na content (TTS) was measured before and after secondary calcination, and the primary charge capacity (CH), primary discharge capacity (DCH), and initial efficiency (ICE) of the sodium secondary battery were measured and are shown in Table 2 and Figure 4 below.

[0074] *Measurement of residual sodium content (TTS) The residual sodium content was determined by measuring the residual Na-containing compounds (e.g., NaOH or Na2CO3) separately using potentiometric titration, and then calculating the total amount of Na alone separately (TTS, Total Sodium).

[0075] The calculation method is as shown in Formula 1 below. [Calculation Formula 1] TTS (Total Na) = NaOH analysis value (%) × Na / NaOH + Na2CO3 analysis value (%) × 2Na / Na2CO3

[0076] *Battery performance evaluation After performing one charge / discharge cycle at 25°C and a drive voltage range of 2.0V to 4.6V under conditions of 0.1C / 0.5C, the primary charge capacity, primary discharge capacity, and primary discharge / charge capacity (ICE) were calculated. [Table 2] Referring to Table 2 and Figure 4, when the O3-type particle content is less than 20 wt%, the volume characteristics are poor. Conversely, when the O3-type particle content is 80 wt% or more, the residual Na content becomes excessively high, leading to problems such as the possibility of thick CEI (Cathode-Electrolyte Interface) formation, reduced ICE, and gas generation. Furthermore, in order to ensure an ICE of 90% or more and sufficient capacity characteristics, it is preferable to design the P2 / O3 mixing ratio to be 8 / 2 to 6 / 4 by weight.

[0077] Experimental Example 4: Evaluation of XRD peak shift and lifetime characteristics due to changes in secondary firing temperature Except for the fact that the secondary firing was carried out at the temperatures listed in Table 3 below in Example 1, the positive electrode active material and sodium secondary battery were manufactured in the same manner. The results of XRD peak shift analysis of the manufactured positive electrode active material before and after secondary calcination at different temperatures are shown in Table 3 and Figure 5 below. Figure 6 shows an analysis of the battery life characteristics before and after secondary firing at different temperatures.

[0078] *Battery life characteristics Battery life characteristics were measured using an electrochemical analyzer (Toyo, Toscat-3100) after 50 charge / discharge cycles at 25°C and a drive voltage range of 2.0V to 4.6V under 1C / 1C conditions. The ratio of the discharged capacity from cycles 1 to 50 to the initial capacity (cycle capacity retention) was then measured. [Table 3] Referring to Table 3, Figures 5 and 6, when secondary firing is carried out in the preferred secondary firing temperature range of 750-900°C, an XRD shift due to Na migration is observed.

[0079] On the other hand, below the design temperature, the migration effect does not occur, and when the design temperature is exceeded, high-temperature firing can cause structural degradation of the positive electrode active material. In both P2 and O3 type oxides, Na present inside the lattice can come to the surface, causing the crystal structure to collapse.

[0080] Experimental Example 5: Analysis of Gas Generation During Secondary Firing The experimental results (1) to (4) below are shown in Figure 7 for sodium secondary batteries manufactured using positive electrode active material produced without secondary calcination after mixing P2-type and O3-type particles in Example 1, and sodium secondary batteries manufactured using positive electrode active material produced with secondary calcination. (1) After primary charge / discharge: The gas generated after the first charge / discharge following battery assembly was measured. (2) After degassing: The process of removing the gas generated after the initial charge and discharge was carried out. (3) After secondary to tertiary charge-discharge: The gas generated after the charge-discharge phase of the formation stage was measured. (4) After 50 cycles of life: After assuming the volume was zero after secondary and tertiary charge-discharge cycles, the gas generated after 50 cycles was measured.

[0081] Referring to Figure 7, it was confirmed that when the secondary firing process of the present invention is carried out, residual Na can be removed and the amount of gas generated can be reduced compared to when it is not carried out.

[0082] As described above, the present invention has been illustrated and explained in relation to specific embodiments, but it will be obvious to those ordinary in the art that the present invention can be improved and modified in various ways without departing from the technical spirit of the invention provided by the following claims.

Claims

1. It contains P2-type layered oxide particles and O3-type layered oxide particles. A positive electrode active material for sodium secondary batteries, characterized in that, in SEM-EDS mapping analysis, the ratio (S3 / S2) of the surface Na content (at%) (S3) of O3-type layered oxide particles to the surface Na content (at%) (S2) of P2-type layered oxide particles is 0.4 to 1.

6.

2. The positive electrode active material for a sodium secondary battery according to claim 1, characterized in that the ratio (S3 / S2) of the surface Na content (at%) (S3) of the O3 type layered oxide particles to the surface Na content (at%) (S2) of the P2 type layered oxide particles is 0.65 to 1.

45.

3. The positive electrode active material for a sodium secondary battery according to claim 1, characterized in that, in SEM-EDS mapping analysis, the surface Na content (at%) (S2) of the P2-type layered oxide particles is 14.5 to 21.5 at%, and the surface Na content (at%) (S3) of the O3-type layered oxide particles is 7.5 to 21.5 at%.

4. The positive electrode active material for a sodium secondary battery according to claim 3, characterized in that the surface Na content (at%) (S2) of the P2 type layered oxide particles is 14.5 to 21.5 at%, and the surface Na content (at%) (S3) of the O3 type layered oxide particles is 14.5 to 21.5 at%.

5. The positive electrode active material for a sodium secondary battery according to claim 1, characterized in that the P2-type layered oxide particles are represented by the following chemical formula 1, and the O3-type layered oxide particles are represented by the following chemical formula 2: 【Chemistry 1】 In the above chemical formula 1, M1 is P, Sr, Ba, Ti, Zr, W, Co, Mg, Al, Cu, Zn, Ce, Hf, Ta, F, Cr, V, Si, Fe, Y, Ga, Sn, Mo, It is at least one selected from Ge, Nd, B, Nb, and Gd, and 0.44 < a < 0.80, 0.05 ≤ x ≤ 0.45, 0.05 ≤ y ≤ 0.15, and 0.45 < 1 - x - y ≤ 0.

9. 【Chemistry 2】 In the above chemical formula 2, M1 is at least one selected from the group consisting of Fe and Mn, and M2 is at least one selected from P, Sr, Ba, Ti, Zr, W, Co, Mg, Al, Cu, Zn, Ce, Hf, Ta, F, Cr, V, Si, Fe, Y, Ga, Sn, Mo, Ge, Nd, B, Nb, and Gd, and 0.80 < a < 1.1, 0.05 ≤ x ≤ 0.45, 0.05 ≤ y ≤ 0.45, 0.05 ≤ z ≤ 0.15, and 0.05 < 1 - x - y - z ≤ 0.

45.

6. The P2-type layered oxide particles have a Na equivalent (number of moles of Na per mole of the P2-type layered oxide particles) of 0.60 to 0.

70. The positive electrode active material for a sodium secondary battery according to claim 1, characterized in that the O3-type layered oxide particles have a Na equivalent (number of moles of Na per mole of the O3-type layered oxide particles) of 0.90 to 1.

05.

7. The positive electrode active material for a sodium secondary battery according to claim 1, characterized in that the P2-type layered oxide particles and O3-type layered oxide particles are contained in a weight ratio of 8:2 to 2:

8.

8. The positive electrode active material for a sodium secondary battery according to claim 1, characterized in that no NiOx peak appears when analyzed by XRD.

9. The positive electrode active material for a sodium secondary battery according to claim 1, characterized in that the positive electrode active material has a residual Na content (TTS, Total Sodium) of 500 to 10,000 ppm.

10. P2-type layered oxide particles and O3-type layered oxide particles are mixed together. The method is characterized by firing the mixed oxide particles, A method for producing a positive electrode active material for a sodium secondary battery, characterized in that, before proceeding with the aforementioned firing, the P2-type layered oxide particles and O3-type layered oxide particles are not subjected to water washing to remove residual Na from their surfaces.

11. The method for producing a positive electrode active material for a sodium secondary battery according to claim 10, characterized in that the P2-type layered oxide particles and the O3-type layered oxide particles are mixed in a weight ratio of 8:2 to 2:

8.

12. The method for producing a positive electrode active material for a sodium secondary battery according to claim 10, characterized in that the firing is carried out at a temperature of 400 to 1,000°C for 3 to 16 hours.

13. A positive electrode for a sodium secondary battery comprising the positive electrode active material described in claim 1.

14. A sodium secondary battery comprising the positive electrode and the negative electrode described in claim 13.

Images