CN116598462A - Layered positive electrode material of sodium ion battery and preparation method thereof - Google Patents

Layered positive electrode material of sodium ion battery and preparation method thereof Download PDF

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CN116598462A
CN116598462A CN202310683354.XA CN202310683354A CN116598462A CN 116598462 A CN116598462 A CN 116598462A CN 202310683354 A CN202310683354 A CN 202310683354A CN 116598462 A CN116598462 A CN 116598462A
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sodium
positive electrode
ion battery
electrode material
layered
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肖卿慧嫱
褚曼曼
万玉梅
丁楚雄
胡进
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BASF Shanshan Battery Materials Co Ltd
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BASF Shanshan Battery Materials Co Ltd
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    • 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
    • H01M4/364Composites as mixtures
    • 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
    • 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 application provides a layered positive electrode material of a sodium ion battery and a preparation method thereof, wherein sodium Na is remained on the surface of the layered positive electrode material of the sodium ion battery 2 CO 3 The mass percentage of the total substances is 0.05-0.20%, and the mass percentage of the surface residual sodium NaOH is 0.04-0.16%. According to the application, M1 and M2 are used for co-doping, besides the two elements are used for respectively fluxing and improving the cycle performance, the co-doping of the two elements also has a synergistic effect, and the residual alkali on the surface of the positive electrode material can be regulated and controlled by influencing the binding energy.

Description

Layered positive electrode material of sodium ion battery and preparation method thereof
Technical Field
The application belongs to the technical field of sodium ion batteries, and particularly relates to a sodium ion battery positive electrode material and a preparation method thereof.
Background
Energy storage batteries have evolved from lead acid batteries to lithium ion batteries as a major key accessory for clean energy. Lithium ion batteries are widely used in the fields of electronic products, power batteries and the like as rechargeable secondary batteries, and have the highest volumetric specific energy and mass specific energy. However, as lithium ore resources continue to be mined, the cost of lithium ion batteries is gradually increased. On the other hand, the lithium ion battery still has the problems of safety, long service life, poor low-temperature performance and the like. Therefore, development of a new secondary battery that can replace a lithium ion battery is required.
The sodium ion battery is similar to the lithium ion battery in principle, when the sodium ion battery is in a charged state, sodium ions of the positive electrode are separated, migrate to the negative electrode under the action of potential and are embedded into lattices between the negative electrode layers, and when the battery is in a discharged state, the process is opposite to the process. Therefore, the capacity of the sodium ion battery is also derived from sodium ions repeatedly intercalated and deintercalated between the positive electrode and the negative electrode, and the more sodium ions intercalated into the negative electrode during charging, the higher the positive electrode charge capacity, the more sodium ions intercalated into the positive electrode during discharging, and the higher the positive electrode discharge capacity. Sodium ion batteries have attracted extensive interest in scientific research and industry as a new generation of energy storage products because of the abundance of sodium sources and low cost, and the higher safety factor of sodium ion batteries compared to lithium ion batteries. As the main improvement direction of the sodium ion battery, there are mainly layered transition metal oxides, tunnel oxides, polyanion compounds, prussian blue analogues, and the like. However, the tunnel oxide has a low sodium content and a low theoretical capacity; the polyanion compound has complex synthesis and poor conductivity; prussian blue analogues contain crystal water, are difficult to control in the material preparation process, and have low tap density, so that the energy density of the battery is affected.
Layered transition metal oxide Na 1-x MO 2 The closer the x value is to 0, the more stable the structure, and therefore the higher the sodium content, the higher the theoretical capacity. On the basis, the layered transition metal oxide is the most promising sodium ion positive electrode material at present due to the large specific capacity, high ion conductivity and feasible preparation conditions. Compared with the Na content in the P2 type layered transition metal oxide is usually less than or equal to 0.8, the Na content in the O3 type layered material is usually between 0.8 and 1.0, so that the O3 type material has higher energy density, and the preparation mode is simple and is more suitable for industrial production.
However, the O3 phase layered material is sensitive to air and water, water molecules are easily embedded into a sodium layer, sodium ions are separated, structural change is caused, residual alkali on the surface is increased, and electrochemical circulation is not facilitated, so that the residual sodium on the surface of the positive electrode material needs to be regulated and controlled, and electrochemical performance degradation caused by excessive residual sodium is avoided. In addition, the surface residual sodium can reflect whether the sodium ions contained in the material are sufficient, and if the residual sodium is too low under the same chemical formula and the preparation process, the actual sodium is not sufficiently prepared. The current methods for reducing the residual alkali on the surface are mainly surface coating and acid washing, carbon materials [ Sustainable Mater, technology, 2021, 28, e00258, electrochem, commun, 2012, 22, 85-88, J, alloys Compd, 2021, 866, 158950 ], metal oxides [ J, alloys Compd, 2021, 855, 157533, trans, non ferrous Met, soc, china 2022, 32, ACS appl, energy, mater, 2020, 3, 933-942 ], phosphates [ chem, eng, J, 2020, 382, 12269, chem, eng, J, 2020, 384, 123234 ] are all currently the main coating materials, and the application No. CN114725357A describes a method for reacting an acidic solution with residual sodium on the surface of a positive electrode material and then calcining the positive electrode material together with the coating agent, thereby reducing the electrochemical performance of the positive electrode material on the surface. These methods all have good results in terms of improving material properties, but one aspect of the uniformity and integrity of the coating is our control, and on the other hand, too thick a coating can reduce the conductivity of the electrode, which is detrimental to ion and electron transport. In addition, the added coating and acid washing steps further increase the manufacturing cost and increase the unstable factors of the steps.
Disclosure of Invention
The application aims to solve the technical problem that the electrochemical performance is not ideal due to the excessive residual sodium on the surface of a sodium ion layered anode material, overcomes the defects and the shortcomings in the background art, and provides a sodium ion battery layered anode material with low residual sodium and a preparation method thereof.
In order to solve the technical problems, the technical scheme provided by the application is as follows:
sodium ion battery layered positive electrode material, wherein sodium Na is remained on surface of sodium ion battery layered positive electrode material 2 CO 3 The mass percentage of the total substances is 005% -0.20%, and the mass percentage of the surface sodium NaOH to the total substances is 0.04% -0.16%. Materials outside the range have over high alkalinity, so that the materials are easy to absorb water and wet, the viscosity is increased during homogenization, the processing performance is poor, and the subsequent capacity loss is too fast; too low alkalinity indicates that the actual sodium is insufficient or the internal defects of the material are too large, resulting in lower initial capacity or increased capacity fade.
Preferably, the chemical formula of the layered positive electrode material of the sodium ion battery is Na a Ni b Fe c Mn d Cu e M1 f M2 g O h The method comprises the steps of carrying out a first treatment on the surface of the Wherein, M1 element is one or more of Sr, nb and B, and M2 element is one or more of Zr, W, ca, mg, al, ti, P, N, mo or Y; wherein a is more than or equal to 0.9 and less than or equal to 1.1,0.2, b is more than or equal to 0.7, c is more than or equal to 0.2 and less than or equal to 0.7, d is more than or equal to 0.2 and less than or equal to 0.7,0 and less than or equal to e is more than or equal to 0.3, f is more than 0 and less than 0.05, g is more than 0 and less than 0.05,1.95, and h is more than 2.05. According to the technical scheme, the M1 element is doped in the layered positive electrode material of the sodium ion battery, and the fluxing characteristic is utilized, so that the sintering temperature of the material is reduced, and the cost is reduced; m2 element is doped, so that the structural stability of the material is improved, and the cycle life of the material is prolonged; and the co-doping of M1 and M2 has a synergistic effect, and partial transition metal elements or oxygen elements are respectively replaced to enable the transition metal layer or the oxygen layer to be in a negative valence state, so that the bonding strength of sodium ions, the transition metal layer and the oxygen atom layer is enhanced, the surface residual alkali of the positive electrode material is adjusted, and the surface residual alkali of a sample is in a better level.
More preferably, 1.03.ltoreq.a.ltoreq.1.08, and the loss of material capacity outside this range is large.
More preferably, 0.4 < f/g < 2.5; more preferably, the co-doped combination of M1 and M2 is Sr/Mg, nb/P, B/Li. The co-doping combination of the groups enables the transition metal layer or the oxygen layer to be in a negative valence state, enhances the Na+ bonding strength with a positive valence state, and reduces the residual alkali on the surface.
Preferably, the method for testing the surface sodium residue comprises the following steps: using an organic solvent as a residual alkali test solvent, adding an acid solution to perform acid-base neutralization by utilizing the solubility difference of strong alkali and weak alkali in the organic solvent, and using a potentiometric titration method to test the residual Na of a sample 2 CO 3 And NaOH content.
The calculation formula is as follows:
NaOH%=
Na 2 CO 3 %=
v1 is the volume of the acid standard solution consumed by the first equivalence point, V2 is the volume of the acid standard solution consumed by the second equivalence point (comprising the first equivalence point), V is the volume of the constant volume of the sample, and the units are mL.
Preferably, the organic solvent comprises one or more of methanol, ethanol, isopropanol, ethylene glycol, benzyl alcohol or glycerol; the acid used in the neutralization of the acid and the alkali is one or more of sulfuric acid, nitric acid, hydrochloric acid, acetic acid or oxalic acid.
Under the same technical conception, the application also provides a preparation method of the layered positive electrode material of the sodium ion battery, which comprises the following steps:
(1) Mixing a salt solution containing Ni, fe and Mn or a salt solution of Ni, fe, mn, cu according to a proportion to carry out coprecipitation reaction, so as to prepare a ternary or quaternary precursor material;
(2) And mixing the precursor material, a sodium source and a compound containing M1 and M2 elements, sintering, cooling to room temperature, crushing and sieving to obtain the sodium-electricity layered anode material.
The doping substitution can be completed by adding the M1 or the M1 and the M2 elements and performing heat treatment, and the M1 element can improve the lattice energy of the material to stabilize the electrode crystal structure, so that the cycle performance and the heat stability of the material are improved, and the co-doping of the M1 element and the M2 element has a synergistic effect to further influence the bonding energy.
Preferably, the sintering schedule in the step (2) is two-step sintering, including sintering at 450-600 ℃ for 3-8 hours and at 820-1000 ℃ for 10-15 hours. And the constant-temperature sintering stage is added to pre-oxidize the precursor, so that internal defects are eliminated, anisotropy in the grain growth process is inhibited, the subsequent full melting reaction of a sodium source and the precursor is facilitated, and the residual sodium which cannot enter the crystal lattice on the surface is reduced.
Preferably, in the cooling process in the step (2), the cooling rate is controlled to be 0.3-0.7 ℃/min, so that excessive sodium residue caused by precipitation of sodium ions between layers due to excessive cooling rate is avoided, and the energy consumption is increased due to excessive cooling rate.
Preferably, the atmosphere in the step (2) is compressed air, the dew point is < -30 ℃, the humidity is less than 1%, and the rise of residual sodium caused by precipitation of interlayer sodium ions is further avoided.
The sodium source includes Na 2 CO 3 、NaHCO 3 Or NaOH; the M1 element-containing compound comprises SrCO 3 、SrO、SrSO 4 、Sr(OH) 2 ·8H 2 O、H 3 BO 3 、B 2 O 3 、Nb 2 O 5 Or (b)One or more of the following; the M2 element-containing compound comprises Li 2 TiO 3 、TiO 2 、Al 2 O 3 、Al(OH) 3 、CaO、Mg(OH) 2 、/>、MgO、H 3 PO 4 、Na 3 PO 4 、/>、Li 3 BO 3 、LiBO 2 Or Li (lithium) 2 CO 3 One or more of the following.
Compared with the prior art, the layered positive electrode material of the sodium ion battery has the beneficial effects that:
(1) According to the application, M1 and M2 are used for co-doping, besides the two elements are used for respectively fluxing and improving the cycle performance, the co-doping of the two elements also has a synergistic effect, and the residual alkali on the surface of the positive electrode material can be regulated and controlled by influencing the binding energy. When sodium Na is remained on the surface of the sodium-electricity positive electrode material 2 CO 3 Accounting for 0.05 to 0.20 percent of the total mass percent,NaOH is 0.04% -0.16%, so that poor electrochemical performance caused by too high or too low residual alkali on the surface of the material can be effectively avoided, and adverse effects on the capacity and circulation of the anode material are avoided.
(2) The application increases the presintering constant temperature stage, controls the cooling rate and uses compressed air, and prevents interlayer sodium ions from separating out by fully melting the sodium source and the precursor, thereby further reducing the surface residual sodium.
Drawings
In order to more clearly illustrate the embodiments of the present application or the technical solutions in the prior art, the drawings that are required in the embodiments or the description of the prior art will be briefly described, and it is obvious that the drawings in the following description are some embodiments of the present application, and other drawings may be obtained according to these drawings without inventive effort for a person skilled in the art.
FIG. 1 is an FE-SEM image of a layered polycrystalline cathode material of a sodium ion battery of example 1;
FIG. 2 is an FE-SEM image of a layered single crystal positive electrode material of a sodium ion battery of example 2;
FIG. 3 is an FE-SEM image of a layered single crystal positive electrode material of a sodium ion battery of example 3;
fig. 4 is a charge-discharge graph of the layered polycrystalline cathode materials of the sodium ion batteries of example 1 and comparative examples 1 and 2;
fig. 5 is a graph of the capacity retention rate of a 100-turn battery of the layered polycrystalline cathode material of the sodium-ion battery of example 1 and comparative examples 1, 2;
fig. 6 is a charge-discharge curve diagram of a layered single crystal positive electrode material of a sodium ion battery of example 2 and comparative examples 3, 4, 5;
fig. 7 is a graph of the capacity retention rate of a 100-turn battery of the layered single-crystal cathode material of the sodium-ion battery of example 2 and comparative examples 3, 4, 5;
fig. 8 is a charge-discharge curve diagram of a layered single-crystal positive electrode material of a sodium ion battery of example 3 and comparative examples 6 and 7;
fig. 9 is a graph of the capacity retention rate of a 100-turn battery of the layered single-crystal cathode material for sodium ion batteries of example 3 and comparative examples 6 and 7.
Detailed Description
The present application will be described more fully hereinafter with reference to the accompanying drawings, in which preferred embodiments are shown, for the purpose of illustrating the application, but the scope of the application is not limited to the specific embodiments shown.
Unless defined otherwise, all technical and scientific terms used hereinafter have the same meaning as commonly understood by one of ordinary skill in the art. The terminology used herein is for the purpose of describing particular embodiments only and is not intended to be limiting of the scope of the present application.
Unless otherwise specifically indicated, the various raw materials, reagents, instruments, equipment and the like used in the present application are commercially available or may be prepared by existing methods.
Example 1
The layered polycrystalline positive electrode material of the sodium ion battery of the embodiment has a chemical formula of Na 1.03 Ni 0.31 Fe 0.31 Mn 0.33 B 0.0 2 Li 0.02 O 2 Testing residual sodium Na 2 CO 3 The mass fraction is 0.1873%, and the NaOH content is 0.1324%. The FE-SEM of the layered positive electrode material of the sodium ion battery of this example is shown in FIG. 1.
The preparation method of the layered polycrystalline anode material of the sodium ion battery comprises the following steps:
(1) Preparing a nickel-manganese-iron precursor: according to the mole ratio of 1:1:1 preparing 1.0mol/L sulfate or nitrate solution containing Ni, mn and Fe, and precipitating agent NaOH solution and complexing agent NH 3 ·H 2 Adding the O solution into a reaction kettle in parallel, heating and stirring to perform coprecipitation reaction, performing solid-liquid separation on slurry after the reaction is completed, washing the separated solid by deionized water, and drying in an oven to obtain a nickel-iron-manganese precursor;
(2) The nickel-iron-manganese precursor and Na 2 CO 3 、LiBO 2 According to the element mole ratio of 1:1.03: and 0.02, carrying out dry mixing, heating to 450 ℃ in a compressed air atmosphere at a heating rate of 4 ℃/min after uniform mixing, and sintering for 6 hours. Then heating to 855 ℃ at a heating rate of 3 ℃/min, and sintering for 12h. Finally cooling at a cooling rate of 0.5 ℃/minCooling to room temperature, sieving to obtain Na-electric layered polycrystalline anode material with chemical formula of Na 1.03 Ni 0.31 Fe 0.31 Mn 0.33 B 0.02 Li 0.02 O 2
Example 2
The layered single crystal positive electrode material of the sodium ion battery of the embodiment has a chemical formula of Na 1.06 Ni 0.33 Fe 0.324 Mn 0.33 Nb 0.006 P 0.006 O 1.994 Testing residual sodium Na 2 CO 3 The mass fraction is 0.0940%, and the NaOH content is 0.1025%. The FE-SEM of the layered positive electrode material of the sodium ion battery of this example is shown in FIG. 2.
The preparation method of the layered single crystal positive electrode material of the sodium ion battery comprises the following steps:
(1) Preparing a nickel-manganese-iron precursor: according to the mole ratio of 1:1:1 preparing 1.0mol/L sulfate or nitrate solution containing Ni, mn and Fe, and precipitating agent NaOH solution and complexing agent NH 3 ·H 2 Adding the O solution into a reaction kettle in parallel, heating and stirring to perform coprecipitation reaction, performing solid-liquid separation on slurry after the reaction is completed, washing the separated solid by deionized water, and drying in an oven to obtain a nickel-iron-manganese precursor;
(2) The nickel-iron-manganese precursor and Na 2 CO 3 、Nb 2 O 5 、H 3 PO 4 According to the element mole ratio of 1:1.06:0.006:0.006, mixing uniformly, heating to 450 ℃ in a compressed air atmosphere at a heating rate of 4 ℃/min, and sintering for 6 hours. Then heating to 985 ℃ at a heating rate of 3 ℃/min, and sintering for 12 hours. Finally cooling to room temperature at a cooling rate of 0.5 ℃/min, and sieving to obtain the sodium-electricity layered single crystal anode material with a chemical formula of Na 1.06 Ni 0.33 Fe 0.324 Mn 0.33 Nb 0.006 P 0.006 O 1.9 94
Example 3
The layered single crystal positive electrode material of the sodium ion battery of the embodiment has a chemical formula of Na 1.05 Ni 0.217 Fe 0.247 Mn 0.40 Cu 0.13 Sr 0.003 Mg 0.003 O 2 Testing residual sodium Na 2 CO 3 The mass fraction is 0.1389%, and the NaOH content is 0.1192%. The FE-SEM of the layered positive electrode material of the sodium ion battery of this example is shown in FIG. 3.
The preparation method of the layered positive electrode material of the sodium ion battery comprises the following steps:
(1) Preparing a nickel-copper-manganese-iron precursor: preparing a sulfate or nitrate solution containing Ni, mn, fe, cu and a precipitator NaOH solution and a complexing agent NH according to the mole number 3 ·H 2 Adding the O solution into a reaction kettle in parallel, heating and stirring to perform coprecipitation reaction, performing solid-liquid separation on slurry after the reaction is completed, washing the separated solid by deionized water, and drying the separated solid by an oven to obtain a sodium-electricity nickel-iron-manganese precursor;
(2) The sodium-electricity nickel-iron-manganese precursor and Na 2 CO 3 、SrCO 3 MgO in the element mole ratio of 1:1.05:0.003:0.003, and after being mixed uniformly, heating to 450 ℃ at a heating rate of 4 ℃/min in a compressed air atmosphere, and sintering for 6 hours. Then heating to 915 ℃ at a heating rate of 3 ℃/min, and sintering for 12h. Finally cooling to room temperature at a cooling rate of 0.5 ℃/min, and sieving to obtain the sodium-electricity layered single crystal anode material with a chemical formula of Na 1.05 Ni 0.217 Fe 0.247 Mn 0.40 Cu 0.13 Sr 0.003 Mg 0.003 O 2
Comparative example 1
The layered polycrystalline positive electrode material of the sodium ion battery of the comparative example has a chemical formula of Na 1.03 Ni 0.27 Fe 0.31 Mn 0.33 B 0.0 6 Li 0.02 O 2 Removing nickel-iron-manganese precursor and Na 2 CO 3 、H 3 BO 3 、Li 2 CO 3 According to the element mole ratio of 1:1.03:0.06:0.02, the preparation method is identical to that of the positive electrode material of example 1, and sodium residue Na is tested 2 CO 3 The mass fraction is 0.6806%, and the NaOH content is 0.1682%.
Comparative example 2
The comparative example is Na 1.03 Ni 0.33 Fe 0.33 Mn 0.33 O 2 The preparation method of the layered polycrystalline cathode material is the same as that of the cathode material of example 1 except that M1 and M2 substances are not added, and the sodium residue Na is tested 2 CO 3 The mass fraction is 0.6617%, and the NaOH content is 0.2174%.
Comparative example 3
The layered single crystal positive electrode material of the sodium ion battery of the embodiment has a chemical formula of Na 1.06 Ni 0.33 Fe 0.324 Mn 0.33 Nb 0.006 O 2 Removing nickel-iron-manganese precursor and Na 2 CO 3 、Nb 2 O 5 According to the element mole ratio of 1:1.06:0.006, the preparation method is the same as that of the positive electrode material of example 2, and sodium residue Na is tested 2 CO 3 The mass fraction is 0.2164%, and the NaOH content is 0.1657%.
Comparative example 4
The layered single crystal positive electrode material of the sodium ion battery of the embodiment has a chemical formula of Na 1.06 Ni 0.33 Fe 0.324 Mn 0.3 3 P 0.006 O 1.994 Removing nickel-iron-manganese precursor and Na 2 CO 3 、H 3 PO 4 According to the element mole ratio of 1:1.06:0.006, the preparation method is the same as that of the positive electrode material of example 2, and sodium residue Na is tested 2 CO 3 The mass fraction is 0.2318%, and the NaOH content is 0.1958%.
Comparative example 5
The comparative example is Na 1.02 Ni 0.33 Fe 0.324 Mn 0.33 Nb 0.006 P 0.006 O 1.994 Layered single crystal positive electrode material, sodium-removing electric nickel-iron-manganese precursor and Na 2 CO 3 、Nb 2 O 5 、H 3 PO 4 According to the element mole ratio of 1:1.02:0.006:0.006, the preparation method is the same as that of the positive electrode material of example 2, and sodium residue Na is tested 2 CO 3 The mass fraction is 0.0452 percent, and the NaOH content is 0.0341 percent.
Comparative example 6
The comparative example is Na 1.05 Ni 0.217 Fe 0.247 Mn 0.40 Cu 0.13 Sr 0.003 Mg 0.003 O 2 The preparation method of the layered single crystal positive electrode material is identical with that of the positive electrode material of example 3 except that the sintering atmosphere is natural air, and a pre-sintering platform which is used for preserving heat for 6 hours at 450 ℃ is not used in the sintering process, and the residual sodium Na is tested 2 CO 3 The mass fraction is 1.2532%, and the NaOH content is 0.6565%.
Comparative example 7
The comparative example is Na 1.05 Ni 0.217 Fe 0.247 Mn 0.40 Cu 0.13 Sr 0.003 Mg 0.003 O 2 Layered single crystal positive electrode material, the preparation method of which is consistent with that of the positive electrode material of example 3 except that the cooling rate is more than 0.7 ℃/min, and the residual sodium Na is tested 2 CO 3 The mass fraction is 0.8371%, and the NaOH content is 0.2258%.
The residual sodium test methods of examples 1 to 3 and comparative examples 1 to 7 are as follows: respectively taking 10g of samples, dissolving in 100mL of glycerol solution, stirring for 10-30 min, and then carrying out suction filtration and taking filtrate. Preparing 0.1mol/L HCl solution, placing in an automatic potentiometric titrator, titrating in an isocratic mode, recording the volume of HCl consumed during jump points, calculating the residual sodium content of the sample according to the formula, and repeating for 3 times. The test average was taken. And the anode is prepared as a metal sodium sheet, and the anode is subjected to 0.1C constant current charge and discharge twice in a voltage range of 2.0-4.2V at normal temperature, and then subjected to 100 cycles at 1C, and the test results and the residual sodium results are shown in Table 1 together.
TABLE 1
Table 1 illustrates that the addition of M1 and M2 elements to replace cations or anions in the examples can reduce the residual alkali on the surface of the material, and the reduction degree of the residual sodium on the surface can be adjusted by changing the content of the two elements. The synergy of M1 and M2 can effectively increase cycle retention without affecting capacity as compared to the comparative example. When the doping content is too high, the residual sodium is low, but the internal defects are serious, so that capacity loss is caused. When the actual sodium is not sufficiently prepared, the residual sodium is low, but the active substances are too little, so the first-round capacity is too low. The presintering section is increased, compressed air is used, the cooling rate is controlled, residual alkali can be effectively reduced, and the cycle life is prolonged. See in particular figures 4-9.

Claims (7)

1. A layered positive electrode material of a sodium ion battery is characterized in that sodium Na is remained on the surface of the layered positive electrode material of the sodium ion battery 2 CO 3 The mass percentage of the total substances is 0.05-0.20%, and the mass percentage of the surface residual sodium NaOH is 0.04-0.16%.
2. The layered positive electrode material of a sodium ion battery of claim 1, wherein the layered positive electrode material of a sodium ion battery has a chemical formula Na a Ni b Fe c Mn d Cu e M1 f M2 g O h The method comprises the steps of carrying out a first treatment on the surface of the Wherein, M1 element is one or more of Sr, nb and B, and M2 element is one or more of Zr, W, ca, mg, al, ti, P, N, mo or Y; wherein a is more than or equal to 0.9 and less than or equal to 1.1,0.2, b is more than or equal to 0.7, c is more than or equal to 0.2 and less than or equal to 0.7, d is more than or equal to 0.2 and less than or equal to 0.7,0 and less than or equal to e is more than or equal to 0.3, f is more than 0 and less than 0.05, g is more than 0 and less than 0.05,1.95, and h is more than 2.05.
3. The layered cathode material of a sodium ion battery according to claim 1, wherein the method for testing the residual sodium on the surface comprises the following steps: using an organic solvent as a residual alkali test solvent, adding an acid solution to perform acid-base neutralization by utilizing the solubility difference of strong alkali and weak alkali in the organic solvent, and using a potentiometric titration method to test the residual Na of a sample 2 CO 3 And NaOH content.
4. The layered cathode material for a sodium ion battery of claim 3, wherein the organic solvent comprises one or more of methanol, ethanol, isopropanol, ethylene glycol, benzyl alcohol, or glycerol; the acid used in the neutralization of the acid and the alkali is one or more of sulfuric acid, nitric acid, hydrochloric acid, acetic acid or oxalic acid.
5. A method for preparing the layered positive electrode material of sodium ion battery as claimed in any one of claims 1 to 4, comprising the steps of:
(1) Mixing a salt solution containing Ni, fe and Mn or a salt solution of Ni, fe, mn, cu according to a proportion to carry out coprecipitation reaction, so as to prepare a ternary or quaternary precursor material;
(2) And mixing the precursor material, a sodium source and a compound containing M1 and M2 elements, sintering, cooling to room temperature, crushing and sieving to obtain the sodium-electricity layered anode material.
6. The preparation method of claim 5, wherein the sintering schedule in the step (2) is two-step sintering, the two-step sintering comprises performing a first-stage sintering at 450-600 ℃ for 3-8 hours and a second-stage sintering at 820-1000 ℃ for 10-15 hours;
the sintering atmosphere in the step (2) is compressed air, the dew point is less than-30 ℃, and the humidity is less than 1%;
and (3) controlling the cooling rate to be 0.3-0.7 ℃/min in the cooling process in the step (2).
7. The method of claim 5, wherein the sodium source comprises Na 2 CO 3 、NaHCO 3 Or NaOH; the M1 element-containing compound comprises SrCO 3 、SrO、SrSO 4 、Sr(OH) 2 ·8H 2 O、H 3 BO 3 、B 2 O 3 、Nb 2 O 5 Or Nb (Nb) 2 O 5 ·nH 2 One or more of O; the M2 element-containing compound comprises Li 2 TiO 3 、TiO 2 、Al 2 O 3 、Al(OH) 3 、CaO、Mg(OH) 2、MgO、H 3 PO 4 、Na 3 PO 4 、/>、Li 3 BO 3 、LiBO 2 Or Li (lithium) 2 CO 3 One or more of the following.
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