GB2619230A - Nickel-rich high-voltage sodium-ion positive electrode material for battery, preparation method therefor, and application thereof - Google Patents

Nickel-rich high-voltage sodium-ion positive electrode material for battery, preparation method therefor, and application thereof Download PDF

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GB2619230A
GB2619230A GB2313956.1A GB202313956A GB2619230A GB 2619230 A GB2619230 A GB 2619230A GB 202313956 A GB202313956 A GB 202313956A GB 2619230 A GB2619230 A GB 2619230A
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sodium
positive electrode
electrode material
nickel
sulfate
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Yu Haijun
Zhang Xuemei
Xie Yinghao
Li Aixia
ZHONG Yingsheng
Li Changdong
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Hunan Brunp Recycling Technology Co Ltd
Guangdong Brunp Recycling Technology Co Ltd
Hunan Bangpu Automobile Circulation Co Ltd
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Hunan Brunp Recycling Technology Co Ltd
Guangdong Brunp Recycling Technology Co Ltd
Hunan Bangpu Automobile Circulation Co Ltd
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    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B25/00Phosphorus; Compounds thereof
    • C01B25/16Oxyacids of phosphorus; Salts thereof
    • C01B25/26Phosphates
    • C01B25/455Phosphates containing halogen
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/58Selection of substances as active materials, active masses, active liquids of inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFy; of polyanionic structures, e.g. phosphates, silicates or borates
    • H01M4/5825Oxygenated metallic salts or polyanionic structures, e.g. borates, phosphates, silicates, olivines
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/054Accumulators with insertion or intercalation of metals other than lithium, e.g. with magnesium or aluminium
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/54Reclaiming serviceable parts of waste accumulators
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/362Composites
    • H01M4/366Composites as layered products
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/58Selection of substances as active materials, active masses, active liquids of inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFy; of polyanionic structures, e.g. phosphates, silicates or borates
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/62Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M2004/026Electrodes composed of, or comprising, active material characterised by the polarity
    • H01M2004/028Positive electrodes
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

Abstract

The present invention relates to the technical field of sodium-ion batteries, and disclosed are a nickel-rich high-voltage sodium-ion positive electrode material, a preparation method therefor, and an application thereof. The general formula of the sodium-ion positive electrode material is NasNit(PO4)(SO4)/F@M-C, 2≤s≤4, and 0.5≤t≤1.5; and M is an oxide of at least one of zinc, nickel, aluminum, manganese, chromium, molybdenum, manganese, copper, and calcium. In the sodium-ion positive electrode material of the present invention, a stabilizer is added so that the structural stability of the positive electrode material is strengthened, and cyclic discharge performance of the material is improved; a coating layer (formed by tightly combining a metal oxide and the positive electrode material) in the sodium-ion positive electrode material can stabilize ion and electron transport kinetic properties of the material, improve cycle performance of the positive electrode material, hinder the material from continuing agglomeration, and control a particle size.

Description

NICKEL-RICH HIGH-VOLTAGE SODIUM-ION POSITIVE ELECTRODE MATERIAL FOR BATTERY, PREPARATION METHOD THEREFOR, AND APPLICATION
THEREOF
FIELD
[00011 The present disclosure belongs to the technical field of sodium-ion batteries, and specifically relates to a positive electrode material for a nickel-rich high-voltage sodium-ion battery and a preparation method and application thereof.
to BACKGROUND
[0002] Lithium-ion batteries have satisfactory properties, such as high energy density and excellent cycle life, and are successfully applied in mobile electronic devices, transportation power, and energy storage power. At present, thanks to the vigorous development of new energy sources, there is more demand for lithium battery energy storage equipment in fields such as hybrid electric vehicles (HEV), electric vehicles (EV), and smart grids. The current conundrum is that the sharp rise in the cost of lithium and the materials associated with the manufacture of lithium-ion batteries has led to an increase in the price of lithium-ion batteries. The lack of resource prospects and uneven distribution of lithium, therefore, has prompted research into more sustainable and lower-cost, more efficient options.
[0003] Sodium-ion batteries would be a suitable alternative. Sodium is more abundant in the earth's crust; the standard redox potential of sodium is only 0.326V higher than that of lithium metal, and its electronegativity is only 0.05V lower than that of lithium. However, the theoretical mass specific capacity (3860 mAh-g-I) and the theoretical volume specific capacity (2060 mAh-cm') of lithium is much higher than the theoretical mass specific capacity (1160 mAh-g-1) and the theoretical volume specific capacity (1130 mAh-cm-3) of sodium. It can be seen that the performance of sodium-ion battery is inferior to that of lithium-ion battery. Therefore, since 2001, researchers have carried out a lot of research on improving the electrochemical performance of sodium, such as developing high-performance electrode materials, providing superior operating voltage, ascertaining the decomposition reaction of the electrode in the electrolyte and the
-I -
formation of products, and enhancing the electrochemical cycle stability, which will be beneficial to solve the problems of energy density and lifespan of sodium-ion batteries.
[0004] In recent years, with the continuous increase in the price of lithium-ion batteries, especially the consumption of lithium resources and not abundant lithium reserves in the world, we will have to face the dilemma of lithium shortage in the future. The study indicates that sodium, which has similar chemical properties to lithium, is very promising to become the next-generation secondary battery after lithium-ion batteries. Nevertheless, because the larger radius of the sodium ions, the heavier the atomic weight, and the higher standard potential of sodium usually leads to poor reversibility and lower energy density, in general the performance of sodium-ion batteries is not as good as that of lithium-ion batteries. For example, the electrochemical performance of sodium iron phosphate positive electrode materials in terms of capacity, voltage, and cycle ability is lower than that of lithium iron phosphate positive electrode materials.
[0005] Currently, Na4MP207 (M=Fe, Co, Mn, Cu, PO4, 504, CO3) polyanionic positive electrode material, capable of operating at high voltages >3.5 V (vs Na/Na) and exhibiting excellent cycling stability, is a promising positive electrode material. For example, Na4Co3(PO4)2P207 provides a capacity of 95 mAh-g-1 at 0.2C rate in the 3.0-4.4 V (vs Na/Na) voltage window and a capacity retention of >95% over 100 cycles; Na4Fe3(PO4)2(P207), as a positive electrode material for sodium-ion batteries, releases a reversible capacity of 129 mAh-g-1, and the average operating voltage exceeds 3.2 V (vs Nat/Na) electrodes. Nevertheless, for Na4MP04-type sodium-ion batteries, low energy density and poor cycle performance are still the biggest shortcomings, and the energy density of batteries depends on the specific capacity and operating voltage of the material. Therefore, it is urgent to develop a positive electrode material with high specific capacity and high initial operating voltage.
SUMMARY
[0006] The present disclosure aims to solve at least one of the above-mentioned technical problems existing in the prior art. To this end, the present disclosure proposes a nickel-rich high-voltage sodium-ion positive electrode material and a preparation method and application thereof, and the sodium-ion positive electrode material has excellent cycle performance, high specific capacity and an initial operating voltage of up to 3.8V.
[0007] To achieve the above object, the present disclosure adopts the following technical solutions: [0008] A sodium-ion positive electrode material with a general formula of NasNit(PO4)(504)/F@M-C, 2<scl, 0.5<t< I.5; wherein M is oxide of at least one of zinc, nickel, aluminum, manganese, chromium, molybdenum, manganese, copper and calcium.
[0009] Preferably, a value range of s is 2.5<s<3.5, and a value range of t is 0.5<t<1.2.
[0010] Preferably, a formula of the sodium-ion positive electrode material is at least one of Na2.6Nii.2(PO4)(804)/F@A1203-C, Na3.4Nio.s(PO4)(804)/F@CuO-C, and Na3Ni(PO4)(SO4)/F@ZnO-C.
[0011] A preparation method of a sodium-ion positive electrode material, comprising steps of: [0012] mixing a nickel source solution, sulfuric acid source, phosphoric acid source and fluorine source for a microwave hydrothermal reaction, and performing concentration to obtain a triacid salt precursor; [0013] mixing the triacid salt precursor with sodium source and a stabilizer, and heating for reaction to obtain Na,Nit(PO4)(SO4)/F; and [0014] adding a sodium washing agent to the NasNit(PO4)(804)/F for soaking, and sintering to obtain the sodium-ion positive electrode material.
[0015] Preferably, the nickel source solution is obtained by mixing nickel source and an organic acid.
[0016] Further preferably, the organic acid is at least one of tartaric acid, oxalic acid, citric acid, formic acid and acetic acid.
[0017] Further preferably, a concentration of the organic acid is 0.01-12 wt%.
[0018] Further preferably, the nickel source is at least one of nickel sulfate, nickel hydroxide, nickel nitrate, nickel chloride and nickel carbonate.
[0019] Preferably, the sulfuric acid source is at least one of sulfuric acid, sodium sulfate, -3 -ammonium sulfate, ammonium hydrogen sulfate, sodium hydrogen sulfate and nickel sulfate.
[9029] Preferably, the phosphoric acid source is at least one of phosphoric acid, sodium phosphate, ammonium phosphate, di ammonium hydrogen phosphate, ammonium dihydrogen phosphate, sodium hydrogen phosphate and nickel phosphate.
[9021] Preferably, the fluorine source is at least one of ammonium fluoride, potassium fluoride, sodium fluoride and hydrogen fluoride.
[0022] Preferably, a temperature of the microwave hydrothermal reaction is 100-300°C, and a duration of the microwave hydrothermal reaction is 1-60 min: the temperature is preferably 120-240°C, and the duration is preferably 5-300 min [9023] Preferably, after the concentration, it further comprises soaking and drying the triacid salt precursor.
[9024] Preferably, before the mixing, it further comprises hall-milling the triacid salt precursor for 0.5-12 h, and the particle size after ball-milling is <50 p.m.
[9025] Preferably, the sodium source is at least one of sodium hydroxide, sodium citrate, sodium oxalate, sodium acetate, sodium phosphate, sodium sulfate, sodium carbonate and sodium chloride.
[0026] Preferably, the stabilizer is at least one of 1.4-benzenedicarboxylic acid 2,5-dipropoxy-1.4-dihyclrazide, N,N,N-,N.-tetrakis(4-methoxypheny1)-9H-carbazole-3,6-diamine, and 4,4',4-trimethy1-2,2":6',2-terpyridine.
[0027] Preferably, the stabilizer is 0.01-5 wt% of a total mass of the triacid salt precursor and the sodium source.
[9028] Preferably, after the soaking, it further comprises drying, and a temperature of the drying is 60-150°C.
[9029] Preferably, a temperature of the heating reaction is 300-800°C, and a duration of the heating reaction is 0.5-24 h. [9039] Preferably, a solid-liquid ratio of the NasNi1(PO4)(804)/F to the sodium washing agent is (0.1-3): (1-5) g/ml. -4 -
[90311 Preferably, the sodium washing agent is at least one of zinc sulfate, nickel sulfate, aluminum sulfate, manganese sulfate, chromium sulfate, molybdenum sulfate, copper sulfate and calcium sulfate.
[9032] On the one hand, the sodium washing agent can wash away the residual sodium hydroxide on the surface of the positive electrode material, reduce the residual sodium in the positive electrode material, and reduce the side reactions on the surface of the positive electrode material. On the other hand, the sodium ions in the sodium hydroxide on the surface of the positive electrode material are exchanged with acid salts. Some metal ions are added to be hydrolyzed and deposited on the surface of the positive electrode material, dehydrated after drying, and become metal oxides and deposit on the surface of the positive electrode material.
[0033] Preferably, a temperature of the sintering is 400-800'C., and an atmosphere of the sintering is an inert gas.
[9034] A battery, comprising the sodium-ion positive electrode material.
[0035] Preferably, a battery prepared by the sodium-ion positive electrode material has an operating platform voltage of greater than 3.8V during the first discharge.
[9036] With respect to the prior art, the present disclosure has the following beneficial effects: [9037] 1. In the sodium-ion positive electrode material of the present disclosure, by adding a stabilizer, the structural stability of the positive electrode material is strengthened and the cyclic discharge performance of the material is improved; the coating layer (after the sodium washing agent treatment, the metal ions are hydrolyzed and deposited on the surface of the positive electrode material, and are dehydrated to become metal ions, and the metal ions tightly combine with the positive electrode material to form the coating layer) in the sodium-ion positive electrode material can improve the ion and electron transport kinetic properties of the material, improve the cycling performance of the positive electrode material, prevent the nickel-rich high-voltage sodium-ion positive electrode material from continuing to agglomerate and grow, and control the particle size.
[0038] 2. In the preparation method of the present disclosure, the internal particle distribution of the triacid salt precursor synthesized by the microwave method is more uniform, and the electron transfer rate and heat transfer efficiency inside the obtained nickel-rich high-voltage -5 -positive electrode material are of high consistency, which is conducive to the stability of the internal structure of the material. In addition, as a stabilizer is conductive to the stabilized structure and good heat dissipation characteristics, a stabilizer is added to the positive electrode material, so that the stability of the structure of the positive electrode material is strengthened and the cycle discharge performance of the material is improved.
[00391 3. In the present disclosure, during the preparation of a precursor of the nickel-rich high-voltage sodium-ion positive electrode material, the triacid salt precursor is synthesized using microwave, in which the temperature rises rapidly, and the reaction is generally completed within 3-20 minutes. Therefore, the reaction process is very fast and the reaction time is shortened by more than 90%. In addition, the synthesis temperature is controlled at 100-300°C, which is much lower than the conventional high-temperature treatment of 400-800°C, so the reaction temperature of microwave synthesis of triacid salt precursors is lower. In a controlled electromagnetic environment, the crystal nucleation and growth of the triacid salt precursor are accelerated, the grain morphology is controllable, and the uniformity of the triacid salt precursor is good, which is conducive to the synthesis of a material with high crystallinity and uniform and complete particles.
BRIEF DESCRIPTION OF DRAWINGS
[00401 FIG. 1 is a process flow diagram of preparing a sodium-ion positive electrode material
in Example 1 of the present disclosure;
[00411 FIG. 2 is a schematic diagram of the sodium-ion positive electrode material prepared in Example 1 of the present disclosure; [0042] FIG. 3 is an SEM image of the sodium-ion positive electrode material prepared in Example 1 of the present disclosure; [0043] FIG. 4 is a TEM image of the sodium-ion positive electrode material prepared in
Example 1 of the present disclosure.
DETAILED DESCRIPTION -6 -
l00441 The concept of the present disclosure and the technical effects produced thereby will be clearly and completely described below in conjunction with the examples, so as to fully understand the purpose, characteristics and effects of the present disclosure. Obviously, the described examples are only a part of the embodiments of the present disclosure, rather than all the embodiments. Based on the embodiments of the present disclosure, other embodiments obtained by those skilled in the art without creative efforts are all within the scope of protection of the present disclosure.
Example 1
[9045] The sodium-ion positive electrode material of this example has a formula of Na2oNlii.2(PO4)(SO4)/F@A1203-C.
[0046] The process flow diagram of the sodium-ion positive electrode material prepared in this example is shown in FIG. 1. In FIG. 1, nickel hydroxide and citric acid were mixed to obtain solution A; ammonium sulfate, phosphoric acid, and ammonium fluoride were mixed to obtain solution B; under stirring, solution B was added to solution A to obtain solution C; and solution C was placed in a ceramic crucible, sent to a microwave reactor, heated and cooled to obtain a triacid salt precursor. After ball-milling the triacid salt precursor, it was mixed with sodium hydroxide, N,N,N',N'-tetrakis(4-methoxypheny1)-9H-carbazole-3,6-diamine slurry evenly, and the mixture was heated to obtain Na2.6Nii.2(PO4)(SO4)/F. Aluminum sulfate and Na2isNii.2(PO4)(SO4)/F were soaked, heated and cooled to obtain N a2.6Ni.2(PO4)(S 04)/F (9)A1203-C.
[0047] The specific steps for the preparation of the sodium-ion positive electrode material in this example are as follows: l00481 (1) Microwave hydrothermal synthesis of triacid salt precursor: 1.12 g of nickel hydroxide was mixed with 150 nth of 5.5w% citric acid to obtain solution A. 19 mL of 0.53 mol/L ammonium sulfate, 14.9 mL of 0.67 mol/L phosphoric acid, and 9 mL of 0.17 mol/L ammonium fluoride were mixed to obtain solution B. Under stirring, solution B was gradually added dropwise to solution A to obtain solution C. 20 mL of solution C was taken and placed in a ceramic crucible, which was sent to a microwave reactor filled with argon gas at 350W. The microwave reactor was set as follows: the first stage was heating at 110°C and stable evaporation -7 -for 6 mm, the second stage was heating at 275°C and stable evaporation for 25 min, the heating time between the two stages was 180 s, and the temperature was lowered. A triacid salt precursor was obtained.
[9049] (2) Synthesis of Na,6Nii2(PO4)(SO4)/F: After ball-milling the triacid salt precursor for 7.5 h, it was mixed with 17.5 mL of 1.5 mol/L sodium hydroxide and 18 mL of 1.66 wt% N,N,N ',N '-tetrakis(4-methoxypheny1)-9H-carbazole-3,6-diamine slurry evenly under stirring. The mixture was heated in a heating furnace at 300°C for 8h under the argon atmosphere to obtain a sodium-ion positive electrode material Nao 6Nii.2(PO4)(SO4)/F.
[9059] (3) Sodium washing treatment: 4.5 mL of 0.019 mol/L aluminum sulfate was divided 10 into three equal parts, mixed with 1.5 g of sodium-ion positive electrode material Na26Nit2(PO4)(504)/F. The mixture was soaked for three times, and dried in an oven at 110°C for 10 h overnight. It was sintered in the heating furnace at 470°C for 8 h under the argon atmosphere, and cooled to obtain a sodium-ion positive electrode material N a2.6Nii2(PO4)(SO4)/F@ A1203-C.
Example 2
[9051] The sodium-ion positive electrode material of this example has a formula of Na3.4Nio.s(PO4)(S 04)/F @ Cu O-C.
[00521 The specific steps for the preparation of the sodium-ion positive electrode material in this example are as follows: [0053] (I) Microwave hydrothermal synthesis of triacid salt precursor: 1.24 g of nickel sulfate was dissolved in 150 mL of 7.1 w% oxalic acid to obtain solution A. 19 mL of (153 mol/L ammonium sulfate, 1.33 g of diammonium hydrogen phosphate, and 12 mL of (118 mol/L ammonium fluoride were mixed to obtain solution B. Under stirring, solution B was gradually added dropwise to solution A to obtain solution C. 20 mL of solution C was taken and placed in a ceramic crucible, which was sent to a microwave reactor filled with argon gas at 500W. The microwave reactor was set as follows: the first stage was heating at 115°C and stabilization for 3 mm, the second stage was heating at 240°C and stabilization for 20 min, the heating time between the two stages was 180 s, and the temperature was lowered. A triacid salt precursor was obtained. -s -
[00541 (2) Synthesis of Na3.4Nio.8(PO4)(504)/F: After ball-milling the triacid salt precursor to a particle size of <50 pm, it was mixed with 22.7 mL of 1.5 mol/L sodium hydroxide and 18 mL of 1.5 wt% 1,4-benzenedicarboxylic acid 2,5-dipropoxy-1,4-dihydrazide slurry evenly under stirring. The mixture was heated in a heating furnace at 540°C for 6.5h under the argon atmosphere to obtain a sodium-ion positive electrode material Na3.4Nio.s(PO4)(SO4)/F.
[00551 (3) Sodium washing treatment: 4.5 mL of 0.032 mol/L copper sulfate was divided into three equal parts, mixed with 1.5 g of sodium-ion positive electrode material Na3.4Nio.s(PO4)(504)/F. The mixture was soaked for three times, and dried in an oven at 150°C for 4 h. It was sintered in the heating furnace at 590°C for 6.5 h under the argon atmosphere, and cooled to obtain a sodium-ion positive electrode material Na3ANio.s(PO4)(SO4)/F@CuO-C.
Example 3
[00561 The sodium-ion positive electrode material of this example has a formula of Na3Ni(PO4)(SO4)/F@ZnO-C.
[0057] The specific steps for the preparation of the sodium-ion positive electrode material in this example are as follows: [0058] (1) Microwave hydrothermal synthesis of triacid salt precursor: 1.3 g of nickel chloride was dissolved in 500 mL of 0.317mo1/Lw% citric acid to obtain solution A. 19 mL of 0.53 mol/L ammonium sulfate, 1.33 g of diammonium hydrogen phosphate, and 17 mL of 0.18 mol/L ammonium fluoride were mixed to obtain solution B. Under stirring, solution B was gradually added dropwise to solution A to obtain solution C. 200 mL of solution C was taken and placed in a ceramic crucible, which was sent to a microwave reactor filled with argon gas at 350W. The microwave reactor was set as follows: the first stage was heating at 115°C and stable evaporation for 3 mm, the second stage was heating at 275°C and stable evaporation for 20 min, the heating time between the two stages was 180 s, and the temperature was lowered. A triacid salt precursor was obtained.
[0059] (2) Synthesis of Na3Ni(PO4)(504)/F: After ball-milling the triacid salt precursor to a particle size of <50 gm, it was mixed with 20 mL of 1.5 mol/L sodium hydroxide and 22 mL of 1.5 wt% 4,4',4-trimethy1-2,2':6',2-terpyridine slurry evenly under stirring. The mixture was heated in a heating furnace at 620°C for 8h under the argon atmosphere to obtain a sodium-ion positive electrode material Na3Ni(PO4)(SO4)/E [9069] (3) Sodium washing treatment: 6 mL of 0.063 mol/L zinc sulfate was divided into three equal parts, mixed with 2.0 g of sodium-ion positive electrode material Na3Ni(PO4)(SO4)/F. The mixture was soaked for three times, and dried in an oven at 125°C for 3 11. It was sintered in the heating furnace at 470°C for 6.5 h under the argon atmosphere, and cooled to obtain a sodium-ion positive electrode material Na3Ni(PO4)(SO4)/F@ZnO-C.
Comparative Example 1 [9061] The sodium-ion positive electrode material of this comparative example has a formula of Na34Ni0.8(1)04)(SO4)/F@A1203.
[0062] The specific steps for the preparation of the sodium-ion positive electrode material in this comparative example are as follows: [9063] (1) Microwave hydrothermal synthesis of triacid salt precursor: 1.24 g of nickel sulfate was dissolved in 50 mL of 5.5w% citric acid to obtain solution A. 19 mL of 0.53 mol/L ammonium sulfate, 16 mL of 0.67 mol/L phosphoric acid, and 12 mL of 0.18 mol/L ammonium fluoride were mixed to obtain solution B. Under stirring, solution B was gradually added dropwise to solution A to obtain solution C. 200 mL of solution C was taken and placed in a ceramic crucible, which was heated at 540°C for 8 h under argon atmosphere and cooled to obtain a triacid salt precursor.
[9064] (2) Synthesis of Na3.4Nius(PO4)(SO4)/F: After ball-milling the triacid salt precursor to a particle size of <50 pm, it was mixed with 22.7 mL of 1.5 mol/L sodium hydroxide and 18 mL, of L5 wt% 4,4',4-trimethyl-2,2':6',2-terpyridine slurry evenly under stirring. The mixture was heated in a heating furnace at 540°C for 6.5h under the argon atmosphere to obtain a sodium-ion positive electrode material Na3.4Nio.s(PO4)(SOL)/F-C.
Comparative Example 2 [00651 The sodium-ion positive electrode material of this comparative example has a formula of Na3.4Ni0.4PO4)(SO4)/F@A1203.
[0066] The specific steps for the preparation of the sodium-ion positive electrode material in this comparative example are as follows: [00671 (1) Microwave hydrothermal synthesis of triacid salt precursor: 1.24 g of nickel sulfate was dissolved in 50 mL of 5.5w% citric acid to obtain solution A. 19 mL of 0.53 mol/L ammonium sulfate, 1.42 g of diammonium hydrogen phosphate, and 12 mL of 0.18 mol/L ammonium fluoride were mixed to obtain solution B. Under stirring, solution B was gradually added dropwi se to solution A to obtain solution C. 200 mL of solution C was taken and placed in a ceramic crucible, which was heated at 540°C for 8 h under argon atmosphere and cooled to obtain a triacid salt precursor.
[00681 (2) Synthesis of Na34Nios(PO4)(SO4)/F: After ball-milling the triacid salt precursor to a particle size of <50 p.m, it was mixed with 22.7 mL of 1.5 mol/L sodium hydroxide evenly under stirring. The mixture was heated in a heating furnace at 540°C for 6.5h under the argon atmosphere to obtain a sodium-ion positive electrode material Na34Nios(PO4)(504)/F.
[00691 (3) Sodium washing treatment: 6 mL of 0.022 mol/L aluminum sulfate was divided into three equal parts, mixed with 2.0 g of sodium-ion positive electrode material Na3.4Ni0.8(PO4)(SO4)/F. The mixture was soaked for three times, and dried in an oven at 95°C to constant weight. It was sintered in the heating furnace at 540°C for 6.5 h under the argon atmosphere, and cooled to obtain a sodium-ion positive electrode material Na3.4Nio.8(1)04)(504)/F@ A1203.
Comparative Example 3 [00701 The sodium-ion positive electrode material of this comparative example has a formula 20 of Na3Ni(PO4)(SO4)/F.
[00711 The specific steps for the preparation of the sodium-ion positive electrode material in this comparative example are as follows: [0072] (I) Microwave hydrothermal synthesis of triacid salt precursor: 1.55 g of nickel sulfate was dissolved in 50 mL of 5.5w% citric acid to obtain solution A. 19 mL of 0.53 mol/L ammonium sulfate, 1.53 g of diammonium hydrogen phosphate, and 12 mi. of 0.18 mol/L ammonium fluoride were mixed to obtain solution B. Under stirring, solution B was gradually added dropwise to solution A to obtain solution C. 200 mL of solution C was taken and placed in a ceramic crucible, which was sent to a microwave reactor filled with argon gas at 350W. The microwave reactor was set as follows: the first stage was heating at 90°C and stable evaporation for 6 min, the second stage was heating at 275°C and stable evaporation for 25 min, the heating time between the two stages was 180 s, and the temperature was lowered. A triacid salt precursor was obtained.
i90731 (2) Synthesis of NaiNi(PO4)(SO4)/F: The triacid salt precursor was ball-milled to a 5 particle size of <50 pm, mixed with 20 mL of 1.5 mol/L sodium hydroxide, and dried in an oven at 125°C for 3h. The mixture was heated in a heating furnace at 540°C for 8h under the argon atmosphere to obtain a sodium-ion positive electrode material Na3Ni(PO4)(SO4)/F.
Analysis of Examples 1-3 and Comparative Examples 1-3: [00741 The sodium-ion positive electrode material prepared in Examples 1-3 and Comparative Examples 1-3, carbon black conductive agent, and polytetrafluoroethylene were mixed and dissolved in deionized water in a mass ratio of 80:10:10 to prepare a slurry, which was then coated on aluminum foil to form electrode sheet. The electrode sheet was placed in a drying box to dry at 80°C for 12 h, and stamped into a disc in a mold. The disc was cut into a counter electrode sheet with a diameter of 10 mm. 1.0 mol/L NaC104 as electrolyte was added to carbonate. Celgard2400 was used as separator. The battery was assembled in a vacuum glove box under argon atmosphere. The AC impedance and cyclic voltammetry of the button battery were tested by electrochemical workstation, and the charge and discharge of the button battery was tested by the LAND battery test system. The current density of the test was 30 mAig-l.
Table 1 Test data of battery obtained from the positive electrode materials prepared in Examples 1-3 and Comparative Examples 1-3 Sample Discharge Capacity Discharge Efficiency (To) Operating (mAh-g-i) Platform Voltage at First Discharge (V) tsi 1011 tooth 1st win 100th Example 1 132.6 121.3 108.7 981 89.9 80.5 3.8 Example 2 131.4 122.9 108.2 97.3 91.3 80.1 3.8 Example 3 128.3 119.8 107.5 95.1 88.7 79.6 3.8 12 -Comparative 117.7 110.8 91.3 92.7 87.2 71.9 3.7
Example I
Comparative 117.5 109.1 93.2 92.5 86.3 70.8 3.6
Example 2
Comparative 115.6 107.6 89.8 91.0 88.0 73.5 3.7
Example 3
[0075] In Table 1, the first discharge capacity of Examples 1-3 was 128.3-132.6 inAh-g-1 and the platform voltage at the first discharge was 3.8V, whereas the first discharge capacity of Comparative Examples 1-3 was 115.6-117.7 mAh-g-1 and the platform voltage at the first discharge was 3.6-3.7V. In addition, at the 100th discharge; the discharge capacity of Examples 1-3 was still 107.5-108.7 mAh-g-1, and the first discharge capacity of Comparative Examples 1-3 was 89.8-93.2 mAh-g-1. The discharge efficiency of the battery obtained from the positive electrode material prepared in Examples 1-3 was also higher than that of the battery obtained from the positive electrode material prepared in Comparative Examples 1-3 in the first, 10th, and 1001h discharge, respectively. It shows that the electrochemical performance of nickel-rich high-voltage sodium-ion positive electrode material has been improved after microwave hydrothermal treatment, addition of stabilizer, and soaking with sodium washing agent.
[0076] From FIG. 2 and FIG. 4, the surface of the sodium-ion positive electrode material prepared in Example 1 was coated with a layer of aluminium oxide, which was closely combined with the sodium-ion positive electrode material. In FIG. 3, the surface of the nickel-rich high-voltage sodium-ion positive electrode material was relatively rough, and the particle size was about 12 p.m.
[0077] The embodiments of the present disclosure have been described in detail above in conjunction with the drawings. However, the present disclosure is not limited to the above-mentioned embodiments, and various modifications can be made without departing from the purpose of the present disclosure within the scope of knowledge possessed by those of ordinary skill in the art. In addition, in the case of no conflict, the embodiments of the present disclosure and the features in the embodiments may be combined with each other.

Claims (10)

  1. CLAIMS1. A sodium-ion positive electrode material with a general formula of NasNii(PO4)(SO4)/F@M-C; wherein M is oxide of at least one of zinc, nickel, aluminum, manganese, chromium, molybdenum, manganese, copper and calcium, and 2<s<4, 0.5<t< I.5.
  2. 2. The sodium-ion positive electrode material according to claim I, wherein a value range of s is 2.5<s<3.5, and a value range of t is 0.54<1.2.
  3. 3. A preparation method of the sodium-ion positive electrode material according to any one of claims 1-2, comprising steps of: mixing a nickel source solution, sulfuric acid source, phosphoric acid source and fluorine source for a microwave hydrothermal reaction, and performing concentration to obtain a triacid salt precursor; mixing the triacid salt precursor with sodium source and a stabilizer, and heating for reaction to obtain NasNii(PO4)(Sa4)/F; and adding a sodium washing agent to the NasNit(PO4)(SO4)/F for soaking, and sintering to obtain the sodium-ion positive electrode material.
  4. 4. The preparation method according to claim 3, wherein the nickel source solution is obtained by dissolving nickel source in an organic acid; the organic acid is at least one of tartaric acid, oxalic acid, citric acid, formic acid, and acetic acid; and the nickel source is at least one of nickel sulfate, nickel hydroxide, nickel nitrate, nickel chloride and nickel carbonate.
  5. 5. The preparation method according to claim 3, wherein the sulfuric acid source is at least one of sulfuric acid, sodium sulfate, ammonium sulfate, ammonium hydrogen sulfate, sodium hydrogen sulfate and nickel sulfate.
  6. -14 - 6. The preparation method according to claim 3, wherein the phosphoric acid source is at least one of phosphoric acid, sodium phosphate, ammonium phosphate, diammonium hydrogen phosphate, ammonium dihydrogen phosphate, sodium hydrogen phosphate and nickel phosphate.
  7. 7. The preparation method according to claim 3, wherein the fluorine source is at least one of ammonium fluoride, potassium fluoride, sodium fluoride and hydrogen fluoride; the sodium source is at least one of sodium hydroxide, sodium citrate, sodium oxalate, sodium acetate, sodium phosphate, sodium sulfate, sodium carbonate and sodium chloride; the stabilizer is at least one of 1,4-benzenedicarboxylic acid 2,5-dipropoxy-1,4-dihydrazide, N,N,N',N.-tetralcis(4-methoxypheny1)-9H-carbazole-3,6-diamine, and 4,4',4-trimethy1-2,2':6',2-terpyridine.
  8. 8. The preparation method according to claim 3, wherein a temperature of the microwave hydrothermal reaction is 100-300°C, and a duration of the microwave hydrothermal reaction is 1-60 mm; and a solid-liquid ratio of the NaNiu(PO4)(804)/F to the sodium washing agent is (0.1-3): (1-5) g/ml.
  9. 9. The preparation method according to claim 3, wherein the sodium washing agent is at least one of zinc sulfate, nickel sulfate, aluminum sulfate, manganese sulfate, chromium sulfate, molybdenum sulfate, copper sulfate and calcium sulfate.
  10. 10. A battery, comprising the sodium-ion positive electrode material according to any one of claims 1-2.-15 -
GB2313956.1A 2021-11-26 2022-08-30 Nickel-rich high-voltage sodium-ion positive electrode material for battery, preparation method therefor, and application thereof Pending GB2619230A (en)

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CN106328911A (en) * 2016-11-30 2017-01-11 合肥工业大学 Material with mixture of ions with sodium vanadium phosphate cathode material coated by carbon and preparing method thereof
CN109065855A (en) * 2018-07-12 2018-12-21 合肥国轩高科动力能源有限公司 A kind of oxide and carbon coat sodium-ion battery positive material vanadium phosphate sodium of cation doping and preparation method thereof altogether
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