CN115924980A - Preparation method of iron-based sodium-ion battery layered positive electrode material precursor of composite phosphate - Google Patents

Preparation method of iron-based sodium-ion battery layered positive electrode material precursor of composite phosphate Download PDF

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CN115924980A
CN115924980A CN202211675841.3A CN202211675841A CN115924980A CN 115924980 A CN115924980 A CN 115924980A CN 202211675841 A CN202211675841 A CN 202211675841A CN 115924980 A CN115924980 A CN 115924980A
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iron
sodium
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phosphate
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孙丽媛
沈锐
同小博
苗春清
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Jiangsu Beiteri Nano Technology Co ltd
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Abstract

The invention provides a preparation method of a layered positive electrode material precursor of an iron-based sodium-ion battery of composite phosphate, which comprises the following steps: preparing a solution containing iron salt; preparing an alkali solution; preparing a complexing agent solution; preparing a base solution; stirring the base solution, heating, and introducing nitrogen; and introducing the iron-containing salt solution, the alkali solution and the complexing agent solution into the base solution for reaction, filtering the reaction solution after the reaction is finished, washing the obtained solid with deionized water, and drying to obtain the precursor of the layered positive electrode material of the iron-based sodium ion battery of the composite phosphate. According to the method, the selected additive has both reducibility and complexation on ferrous ions, so that the ferrous ions can be prevented from being oxidized, and meanwhile, the additive has complexation on the ferrous ions in the reaction, so that the precipitation speed of the ferrous ions can be controlled, and uneven precipitation can be prevented; phosphate is added into the reaction solution, so that the polyanionic material can be compounded in one step, and the mixing-sintering process of the traditional composite material is reduced.

Description

Preparation method of iron-based sodium-ion battery layered positive electrode material precursor of composite phosphate
Technical Field
The invention belongs to the technical field of battery materials, and particularly relates to a preparation method of a precursor of a layered positive electrode material of an iron-based sodium-ion battery of composite phosphate.
Background
Sodium ion batteries are more advantageous in cost and safety as potential replacements for lithium ion batteries in the fields of energy storage and low-speed power batteries. The positive electrode material is one of core materials of the sodium ion battery, and determines the electrochemical properties of the sodium ion battery, such as energy density, safety, cycle retention rate and the like. Different from lithium ion batteries, sodium ion batteries have lower energy density and lower cost, and the future application fields mainly focus on energy storage and low-speed power batteries, so that the iron-based layered anode has the cost advantage over the traditional nickel-cobalt-manganese ternary anode, and has a wider application prospect in the field of sodium electricity. Because the iron element is introduced into the system, the nickel-cobalt-manganese coprecipitation method cannot be used for reference in the synthesis of the precursor hydroxide, because the complexing effect of ferrous ions and ammonia in a solution is far inferior to that of nickel-cobalt-manganese, the precipitation speed of the ferrous ions is too high, and the phenomenon of uneven precipitation is finally caused. In addition, the cycling performance of the layered oxide positive electrode is poor generally, and the cycling performance of the polyanion positive electrode is good, so that the cycling performance of the positive electrode material can be improved by mixing, grinding and sintering the prepared layered oxide and a small amount of polyanion material in a laboratory, but the compounding effect is difficult to control by the method, and part of the polyanion material is possibly not combined with the layered oxide positive electrode.
Therefore, it is necessary to develop a phosphate-compounded iron-based sodium-ion battery layered positive electrode material precursor to solve the above problems.
Disclosure of Invention
The invention provides a preparation method of a precursor of a layered positive electrode material of an iron-based sodium-ion battery of composite phosphate, which aims to solve the technical problems.
The invention provides a preparation method of a layered positive electrode material precursor of an iron-based sodium-ion battery of composite phosphate, which comprises the following steps:
(1) Preparing an iron-containing salt solution, wherein the iron-containing salt solution is prepared from soluble metal salt, an additive and water, the soluble metal salt at least comprises three elements of iron, nickel and manganese, the total molar concentration of all metal ions in the iron-containing salt solution is 0.5-2.5mol/L, and the molar ratio of the iron, the nickel and the manganese in the iron-containing salt solution is X 1 :X 2 :X 3 And then 0.2 is less than or equal to X 1 ≤0.6、0.2≤X 2 ≤0.6、X 1 +X 2 +X 3 =1, wherein the additive comprises at least one of citric acid, sodium citrate, glucose and sodium gluconate, and when the molar ratio of the additive to ferrous ions is Z, Z is more than or equal to 0.01 and less than or equal to 0.1;
(2) Preparing an alkaline solution, wherein the alkaline solution consists of an alkaline substance and a phosphorus source, the alkaline substance comprises at least one of sodium hydroxide, sodium carbonate and sodium bicarbonate, and the phosphorus source comprises at least one of phosphoric acid, pyrophosphoric acid, sodium dihydrogen phosphate, disodium hydrogen phosphate, trisodium phosphate and sodium pyrophosphate;
(3) Preparing a complexing agent solution, wherein the complexing agent solution contains NH 3 NH of said 3 The molar concentration of the complexing agent in the complexing agent solution is 1-3mol/L;
(4) Preparing a base solution, wherein the base solution contains NH 3 And additives, the NH 3 The molar concentration of the additive in the base solution is 0.1-1mol/L, the additive is at least one of citric acid, sodium citrate, glucose and sodium gluconate, and the molar concentration of the additive in the base solution is 0.001-0.05mol/L;
(5) Stirring the base solution, heating to 40-60 ℃, and introducing nitrogen at the speed of 0.2-0.6L/min;
(6) And after the nitrogen is introduced for 4-10 hours, introducing the iron-containing salt solution, the alkali solution and the complexing agent solution into the base solution for reaction, filtering the reaction solution after the reaction is finished, washing the obtained solid with deionized water, and drying to obtain the iron-based multi-hydroxide, namely the precursor of the layered positive electrode material of the iron-based sodium ion battery of the composite phosphate.
As a preferable scheme of the preparation method of the layered positive electrode material precursor of the iron-based sodium-ion battery of the composite phosphate, the soluble metal salt in the step (1) further comprises one or more of magnesium sulfate, zinc sulfate, calcium nitrate, copper sulfate and titanium sulfate, and when the molar ratio of magnesium, zinc, calcium, copper, aluminum and titanium in the iron-containing salt solution to the total metal content is Y, Y is greater than or equal to 0 and less than or equal to 0.1.
As a preferable scheme of the preparation method of the layered positive electrode material precursor of the iron-based sodium-ion battery of the composite phosphate, the soluble metal salt containing three elements of iron, nickel and manganese in the step (1) is selected from at least three of ferrous sulfate, ferrous chloride, ferrous nitrate, nickel sulfate, nickel chloride, nickel nitrate, manganous sulfate, manganous chloride and manganous nitrate.
As a preferable scheme of the preparation method of the precursor of the layered positive electrode material of the iron-based sodium-ion battery of the composite phosphate, in the step (2), the molar concentration of P in the alkali solution is 0.005-0.05mol/L, and OH is - The molar concentration in the alkali solution is 1-5mol/L.
As a preferable embodiment of the preparation method of the precursor of the layered positive electrode material of the iron-based sodium-ion battery of the composite phosphate, in the step (3), the complexing agent solution further contains a surfactant, and the surfactant is selected from at least one of sodium dodecyl benzene sulfonate, sodium dodecyl sulfate, stearic acid, polyethylene glycol, and dodecyl glucoside.
As a preferable scheme of the preparation method of the precursor of the layered positive electrode material of the iron-based sodium-ion battery of the composite phosphate, the molar concentration of the surfactant in the complexing agent solution is 0-1mol/L.
As a preferable embodiment of the preparation method of the precursor of the layered positive electrode material of the iron-based sodium-ion battery of the composite phosphate, in the step (4), the base solution further contains a surfactant, and the surfactant is selected from at least one of sodium dodecyl benzene sulfonate, sodium dodecyl sulfate, stearic acid, polyethylene glycol, and dodecyl glucoside.
In a preferable embodiment of the method for preparing the precursor of the layered positive electrode material of the phosphate-compounded iron-based sodium-ion battery, the molar concentration of the surfactant in the base solution is 0-0.05mol/L.
As a preferable scheme of the preparation method of the precursor of the layered positive electrode material of the iron-based sodium-ion battery of the composite phosphate, the stirring rotating speed in the step (5) is 150-300r/min.
As a preferable scheme of the preparation method of the layered positive electrode material precursor of the iron-based sodium-ion battery of the composite phosphate, in the step (6), when the iron-containing salt solution, the alkali solution and the complexing agent solution are introduced into the base solution for reaction, total metal ions in the iron-containing salt solution and OH in the alkali solution introduced in unit time are reacted - The molar ratio of (1).
Compared with the prior art, the preparation method of the precursor of the layered positive electrode material of the iron-based sodium-ion battery of the composite phosphate has the advantages that:
1. the selected additive has both reducibility and complexation on ferrous ions, can prevent the ferrous ions from being oxidized, has complexation on the ferrous ions in the reaction, can control the precipitation speed of the ferrous ions, and can prevent uneven precipitation;
2. phosphate is added into the reaction solution, so that the polyanionic material can be compounded in one step, and the mixing-sintering process of the traditional composite material is reduced.
Drawings
Fig. 1 is an SEM image of a precursor material prepared in example 1 by the method for preparing a phosphate-compounded iron-based sodium-ion battery layered positive electrode material precursor of the present invention, the SEM image being 2 ten thousand times larger;
fig. 2 is an SEM image of a precursor material prepared in example 2 by the method for preparing a phosphate-compounded iron-based sodium-ion battery layered positive electrode material precursor of the present invention, the SEM image being 2 ten thousand times larger;
fig. 3 is an SEM image of a precursor material prepared in example 3 by the method for preparing a phosphate-compounded iron-based sodium-ion battery layered positive electrode material precursor of the present invention, the SEM image being 2 ten thousand times larger;
fig. 4 is an SEM image of a precursor material prepared in the comparative example, magnified 2 ten thousand times.
Detailed Description
The present invention will be described in further detail with reference to specific embodiments in order to make the above objects, features and advantages more apparent and understandable.
First, reference herein to "one embodiment" or "an embodiment" means that a particular feature, structure, or characteristic described in connection with the embodiment is included in at least one implementation of the invention. The appearances of the phrase "in one embodiment" in various places in the specification are not necessarily all referring to the same embodiment, nor are separate or alternative embodiments mutually exclusive of other embodiments.
The preparation method of the novel phosphate-compounded iron-based sodium-ion battery layered positive electrode material precursor comprises the following specific operation steps:
(1) Preparing a solution containing iron salt: the solution is prepared from soluble metal salt, an additive and water. The soluble metal salt at least comprises soluble metal salts of 3 elements of iron, nickel and manganese, wherein the optional metal salts comprise ferrous sulfate, ferrous chloride, ferrous nitrate, nickel sulfate, nickel chloride, nickel nitrate, manganous sulfate, manganous chloride and manganous nitrate; the soluble metal salt may also contain one or more of magnesium sulfate, zinc sulfate, calcium nitrate, copper sulfate, and titanium sulfate; the total molar concentration of all metal ions in the iron-containing salt solution is 0.5-2.5mol/L, and the molar ratio X of iron, nickel and manganese in the iron-containing salt solution 1 :X 2 :X 3 Should satisfy X is more than or equal to 0.2 1 ≤0.6;0.2≤X 2 ≤0.6;X 1 +X 2 +X 3 =1, the molar ratio Y of magnesium, zinc, calcium, copper, aluminum and titanium in the iron-containing salt solution to the total metal content should satisfy that Y is more than or equal to 0 and less than or equal to 0.1, the metal elements are added in the ratio range, the crystal structure stability of the final anode product can be improved, the structural collapse caused by sodium ion intercalation and deintercalation is reduced, and the material is improvedMaterial stability; the additive comprises at least one of citric acid, sodium citrate, glucose and sodium gluconate, the molar ratio Z of the additive to ferrous ions is more than or equal to 0.01 and less than or equal to 0.1, the Z range can play the role of the additive in resisting oxidation and complexing ferric ions on one hand, and on the other hand, the phenomenon that the ferrous precipitation rate is too low due to too high complexing effect, so that the precipitation is asynchronous is avoided.
(2) Preparing an alkali solution: the solution consists of an alkaline substance and a source of phosphorus. The alkaline substance comprises at least one of sodium hydroxide, sodium carbonate and sodium bicarbonate, the phosphorus source comprises at least one of phosphoric acid, pyrophosphoric acid, sodium dihydrogen phosphate, disodium hydrogen phosphate, trisodium phosphate and sodium pyrophosphate, the molar concentration of P in the alkaline solution is between 0.005 and 0.05mol/L, and OH in the alkaline solution is - The molar concentration is in the range of 1-5mol/L. The molar concentration range of P in the alkali solution, on one hand, a phosphate structure is added into the crystal, the structural strength is enhanced, the cycle performance is improved, and on the other hand, the reduction of the effective structure caused by overhigh P concentration is avoided, and the specific capacity is reduced.
(3) Preparing a complexing agent solution: the solution contains NH 3 ,NH 3 Is in the range of 1-3 mol/L. Optionally, the complexing agent solution further comprises a surfactant, the surfactant comprises at least one of sodium dodecyl benzene sulfonate, sodium dodecyl sulfate, stearic acid, polyethylene glycol and dodecyl glucoside, and the molar concentration of the surfactant in the complexing agent solution is in the range of 0-1mol/L.
(4) Preparing a base solution: the base liquid contains NH 3 And additive, NH 3 The molar concentration of the additive is between 0.1 and 1mol/L, the additive comprises at least one of citric acid, sodium citrate, glucose and sodium gluconate, and the concentration of the additive is within the range of 0.001 to 0.05mol/L. Optionally, the base solution comprises a surfactant, the surfactant comprises at least one of sodium dodecyl benzene sulfonate, sodium dodecyl sulfate, stearic acid, polyethylene glycol and dodecyl glucoside, and the molar concentration of the surfactant in the base solution is in the range of 0-0.05mol/L. NH in the base liquid 3 The concentration range of the additive is combined to ensure that the metals Ni, fe and Mn are close in speedAnd the sediment is avoided being uneven.
(5) Stirring the base solution at 150-300r/min, heating to 40-60 deg.C, and introducing nitrogen at 0.2-0.6L/min.
(6) Introducing the prepared iron-containing salt solution, alkali solution and complexing agent solution into the base solution at a certain flow rate after introducing nitrogen for 4-10h, wherein total metal ions in the iron-containing salt solution and OH in the alkali solution are introduced in unit time - The molar ratio of (1) to (2), the reaction pH value is between 8.5 and 10.5, the reaction time is within the range of 50 to 100 hours, the solution is filtered after the reaction is finished, the obtained solid is washed by deionized water and then dried, and the target product iron-based multi-hydroxide, namely a precursor, is obtained.
For a detailed description and related comparison, see the following examples:
example 1
The invention relates to a preparation method of a novel phosphate-compounded layered positive electrode material precursor of an iron-based sodium-ion battery, which comprises the following steps:
ferrous sulfate, nickel sulfate, manganous sulfate and citric acid are taken, water is added to prepare 2L of salt solution with the total metal ion concentration of 1mol/L, wherein the molar ratio of iron, nickel and manganese is 3. Sodium hydroxide and trisodium phosphate are taken, water is added to prepare 2L of aqueous alkali, so that the concentration of hydroxide radical is 2mol/L, and the concentration of phosphate radical is 0.01mol/L. Adding ammonia water and sodium dodecyl benzene sulfonate into water to prepare 0.5L complexing agent solution, wherein NH is 3 The concentration of (A) is 1.8mol/L, and the molar concentration of the sodium dodecyl benzene sulfonate is 0.2mol/L. Adding ammonia water, sodium dodecyl benzene sulfonate and citric acid into water to prepare 5L base solution, wherein NH 3 The concentration of the sodium dodecyl benzene sulfonate is 0.2mol/L, the molar concentration of the sodium dodecyl benzene sulfonate is 0.02mol/L, and the molar concentration of the citric acid is 0.002mol/L. The bottom liquid is heated to 50 ℃ while stirring at 160r/min, and nitrogen is introduced into the bottom liquid for 6 hours at the flow rate of 0.5L/min. And simultaneously introducing the salt solution, the alkali solution and the complexing agent solution into the base solution, controlling the pH of the base solution to be 9.55, and controlling the flow rates of the salt solution, the alkali solution and the complexing agent solution to be 0.55mL/min, 0.55mL/min and 0.14mL/min respectively when the salt solution, the alkali solution and the complexing agent solution are stable. After 55 hours of reaction, the base solution is taken out and filtered to obtain the precursorWashing the solid of the displacement body by using deionized water until sulfate radical in the filtrate can not be detected, drying and sieving by using a 300-mesh sieve for later use.
Example 2
The invention relates to a preparation method of a novel phosphate-compounded iron-based sodium-ion battery layered positive electrode material precursor, which comprises the following steps:
ferrous sulfate, nickel sulfate, manganous sulfate and glucose are taken, water is added to prepare 2L of salt solution with the total metal ion concentration of 1mol/L, wherein the molar ratio of iron, nickel and manganese is 1. Sodium hydroxide and sodium dihydrogen phosphate are taken and added with water to prepare 2L of aqueous alkali, so that the concentration of hydroxide radical is 2mol/L and the concentration of phosphate radical is 0.01mol/L. Adding ammonia water into water to obtain 0.5L complexing agent solution (NH) 3 The concentration of (2) is 1.8mol/L. Adding ammonia water and glucose into water to obtain 5L base solution, wherein NH 3 The concentration of (2) was 0.2mol/L, and the concentration of glucose was 0.004mol/L. The bottom liquid is heated to 50 ℃ while stirring at 200r/min, and nitrogen is introduced into the bottom liquid for 6 hours at the flow rate of 0.5L/min. And simultaneously introducing the salt solution, the alkali solution and the complexing agent solution into the base solution, controlling the pH of the base solution to be 9.25, and controlling the flow rates of the salt solution, the alkali solution and the complexing agent solution to be 0.55mL/min, 0.55mL/min and 0.14mL/min respectively when the salt solution, the alkali solution and the complexing agent solution are stable. And after 55 hours of reaction, taking out the base solution, filtering, washing the obtained precursor solid with deionized water until sulfate radical in the filtrate can not be detected, drying, and sieving with a 300-mesh sieve for later use.
Example 3
The invention relates to a preparation method of a novel phosphate-compounded iron-based sodium-ion battery layered positive electrode material precursor, which comprises the following steps:
ferrous sulfate, nickel sulfate, manganous sulfate and glucose are taken, water is added to prepare 2L of salt solution with the total metal ion concentration of 1mol/L, wherein the molar ratio of iron, nickel and manganese is 1. Sodium carbonate and trisodium phosphate are taken, water is added to prepare 2L of aqueous alkali, so that the concentration of hydroxide radical is 2mol/L, and the concentration of phosphate radical is 0.01mol/L. Adding ammonia water into water to obtain 0.5L complexing agent solution containing NH 3 The concentration of (2) is 1.8mol/L. Adding ammonia water and glucose into water to obtain 5L base solution,wherein NH 3 The concentration of (2) was 0.2mol/L, and the concentration of glucose was 0.002mol/L. The bottom liquid is heated to 55 ℃ while stirring at 200r/min, and nitrogen is introduced into the bottom liquid for 6 hours at the flow rate of 0.5L/min. And simultaneously introducing the salt solution, the alkali solution and the complexing agent solution into the base solution, controlling the pH of the base solution to be 9.25, and controlling the flow rates of the salt solution, the alkali solution and the complexing agent solution to be 0.55mL/min, 0.55mL/min and 0.14mL/min respectively when the salt solution, the alkali solution and the complexing agent solution are stable. And after 55 hours of reaction, taking out the base solution, filtering, washing the obtained precursor solid with deionized water until sulfate radical in the filtrate can not be detected, drying, and sieving with a 300-mesh sieve for later use.
Comparative example
Ferrous sulfate, nickel sulfate and manganous sulfate are taken, water is added to prepare 2L of salt solution with the total metal ion concentration of 1mol/L, wherein the molar ratio of iron, nickel and manganese is 1. Sodium hydroxide is taken and added with water to prepare 2L of alkali solution, so that the concentration of hydroxide radical is 2mol/L. Adding ammonia water into water to obtain 0.5L complexing agent solution (NH) 3 The concentration of (2) is 1.8mol/L. Adding ammonia water into water to obtain 5L base solution containing NH 3 The concentration of (2) was 0.2mol/L. The bottom liquid is heated to 55 ℃ while stirring at 200r/min, and nitrogen is introduced into the bottom liquid for 6 hours at the flow rate of 0.5L/min. And simultaneously introducing the salt solution, the alkali solution and the complexing agent solution into the base solution, controlling the pH of the base solution to be 9.25, and controlling the flow rates of the salt solution, the alkali solution and the complexing agent solution to be 0.55mL/min, 0.55mL/min and 0.14mL/min respectively when the salt solution, the alkali solution and the complexing agent solution are stable. And after 55 hours of reaction, taking out the base solution, filtering, washing the obtained precursor solid with deionized water until sulfate radical in the filtrate can not be detected, drying, and sieving with a 300-mesh sieve for later use.
The test results of the comparative example and the example are shown in fig. 1 to 4 and table 1 below. 1. SEM test
Referring to fig. 1 to 4, fig. 1 is an SEM image of a precursor material prepared in example 1 by the method for preparing a precursor of a phosphate-compounded iron-based sodium-ion battery layered positive electrode material according to the present invention, the SEM image being 2 ten thousand times larger; fig. 2 is an SEM image of a precursor material prepared in example 2 by the method for preparing a phosphate-compounded iron-based sodium-ion battery layered positive electrode material precursor of the present invention, the SEM image being 2 ten thousand times larger; fig. 3 is an SEM image of a precursor material prepared in example 3 by the method for preparing a phosphate-compounded iron-based sodium-ion battery layered positive electrode material precursor of the present invention, the SEM image being 2 ten thousand times larger; fig. 4 is an SEM image of a precursor material prepared in the comparative example, magnified 2 ten thousand times. As shown in fig. 1 to 4, the precursors of examples 1, 2, and 3 had significant primary particles and good crystallinity; the precursor of the comparative example had a loose structure, poor crystallinity, and no apparent primary particles. The method of the invention can effectively control the coprecipitation reaction, reduce the floccule generated by the rapid precipitation of ferrous ions, slow the overall reaction rate and be beneficial to the growth of primary particle crystals.
2. Sintering of positive electrode material
And uniformly mixing the precursor and anhydrous sodium carbonate, wherein the molar ratio of total metal elements in the precursor to sodium elements in the sodium carbonate is 1.02. The mixed solid is put into a muffle furnace and sintered for 24 hours at 870 ℃. The obtained anode material is sieved by a 300-mesh sieve for later use.
3. Power-off test
The positive electrode material, the conductive agent and the binder are uniformly mixed according to the proportion of 8. And cutting the dried pole piece into a wafer. The button cell is assembled by using the anode wafer, the diaphragm, the sodium metal cathode sheet and the sodium ion battery electrolyte. The cell was charged and discharged at a voltage window of 2.0-4.0V, cycled at 0.1C for 2 cycles, and then cycled at 1C for 50 cycles. (1C = 120mA/g) the test results are shown in Table 1.
Figure BDA0004018233140000081
TABLE 1
As shown in table 1, the specific discharge capacities of examples 1, 2 and 3 at 0.1C and 1C were all higher than those of the comparative examples, and the cycle retention rate was also significantly better than that of the comparative examples. On one hand, the crystallinity of the precursor is improved after the synthesis method of the precursor is optimized, and on the other hand, a small amount of phosphate in the precursor reacts with a sodium source to generate a stable polyanion cathode material.
It should be noted that the above-mentioned embodiments are only for illustrating the technical solutions of the present invention and not for limiting, and although the present invention has been described in detail with reference to the preferred embodiments, it should be understood by those skilled in the art that modifications or equivalent substitutions may be made on the technical solutions of the present invention without departing from the spirit and scope of the technical solutions of the present invention, which should be covered by the claims of the present invention.

Claims (10)

1. A preparation method of a precursor of a layered positive electrode material of an iron-based sodium-ion battery compounded with phosphate is characterized by comprising the following steps:
(1) Preparing a ferrous salt solution, wherein the ferrous salt solution is prepared from soluble metal salt, an additive and water, the soluble metal salt at least comprises three elements of iron, nickel and manganese, the total molar concentration of all metal ions in the ferrous salt solution is 0.5-2.5mol/L, and the molar ratio of the iron, the nickel and the manganese in the ferrous salt solution is X 1 :X 2 :X 3 And then 0.2 is less than or equal to X 1 ≤0.6、0.2≤X 2 ≤0.6、X 1 +X 2 +X 3 =1, wherein the additive comprises at least one of citric acid, sodium citrate, glucose and sodium gluconate, and when the molar ratio of the additive to ferrous ions is Z, Z is more than or equal to 0.01 and less than or equal to 0.1;
(2) Preparing an alkaline solution, wherein the alkaline solution consists of alkaline substances and a phosphorus source, the alkaline substances comprise at least one of sodium hydroxide, sodium carbonate and sodium bicarbonate, and the phosphorus source comprises at least one of phosphoric acid, pyrophosphoric acid, sodium dihydrogen phosphate, disodium hydrogen phosphate, trisodium phosphate and sodium pyrophosphate;
(3) Preparing a complexing agent solution, wherein the complexing agent solution contains NH 3 NH of said 3 The molar concentration of the complexing agent in the complexing agent solution is 1-3mol/L;
(4) Preparing a base solution, wherein the base solution contains NH 3 And additives, the NH 3 The molar concentration of the additive in the base solution is 0.1-1mol/L, the additive is at least one of citric acid, sodium citrate, glucose and sodium gluconate, and the additive in the base solutionThe molar concentration is 0.001-0.05mol/L;
(5) Stirring the base solution, heating to 40-60 ℃, and introducing nitrogen at the speed of 0.2-0.6L/min;
(6) And after the nitrogen is introduced for 4-10 hours, introducing the iron-containing salt solution, the alkali solution and the complexing agent solution into the base solution for reaction, filtering the reaction solution after the reaction is finished, washing the obtained solid with deionized water, and drying to obtain the iron-based multi-hydroxide, namely the precursor of the layered positive electrode material of the iron-based sodium ion battery of the composite phosphate.
2. The method for preparing the precursor of the layered positive electrode material of the phosphate-compounded iron-based sodium-ion battery according to claim 1, wherein the precursor comprises the following steps: the soluble metal salt in the step (1) also comprises one or more of magnesium sulfate, zinc sulfate, calcium nitrate, copper sulfate and titanium sulfate, and the molar ratio of magnesium, zinc, calcium, copper, aluminum and titanium in the iron-containing salt solution to the total metal content is Y, so that Y is more than or equal to 0 and less than or equal to 0.1.
3. The method for preparing the precursor of the layered positive electrode material of the phosphate-compounded iron-based sodium-ion battery according to claim 1, wherein the precursor comprises the following steps: the soluble metal salt containing three elements of iron, nickel and manganese in the step (1) is selected from at least three of ferrous sulfate, ferrous chloride, ferrous nitrate, nickel sulfate, nickel chloride, nickel nitrate, manganous sulfate, manganous chloride and manganous nitrate.
4. The method for preparing the precursor of the layered positive electrode material of the phosphate-compounded iron-based sodium-ion battery according to claim 1, wherein the precursor comprises the following steps: the molar concentration of P in the alkali solution in the step (2) is 0.005-0.05mol/L, OH - The molar concentration in the alkali solution is 1-5mol/L.
5. The method for preparing the precursor of the layered positive electrode material of the phosphate-compounded iron-based sodium-ion battery according to claim 1, wherein the precursor comprises the following steps: and (3) the complexing agent solution also comprises a surfactant, wherein the surfactant is selected from at least one of sodium dodecyl benzene sulfonate, sodium dodecyl sulfate, stearic acid, polyethylene glycol and dodecyl glucoside.
6. The method for preparing the precursor of the layered positive electrode material of the phosphate-compounded iron-based sodium-ion battery according to claim 5, wherein the precursor comprises the following steps: the molar concentration of the surfactant in the complexing agent solution is 0-1mol/L.
7. The method for preparing the precursor of the layered positive electrode material of the phosphate-compounded iron-based sodium-ion battery according to claim 1, wherein the precursor comprises the following steps: and (4) the base solution also comprises a surfactant, wherein the surfactant is selected from at least one of sodium dodecyl benzene sulfonate, sodium dodecyl sulfate, stearic acid, polyethylene glycol and dodecyl glucoside.
8. The method for preparing the precursor of the layered positive electrode material of the phosphate-compounded iron-based sodium-ion battery according to claim 7, wherein the precursor comprises the following steps: the molar concentration of the surfactant in the base solution is 0-0.05mol/L.
9. The method for preparing the precursor of the layered positive electrode material of the iron-based sodium-ion battery of composite phosphate according to claim 1, which is characterized in that: the rotating speed of the stirring in the step (5) is 150-300r/min.
10. The method for preparing the precursor of the layered positive electrode material of the phosphate-compounded iron-based sodium-ion battery according to claim 1, wherein the precursor comprises the following steps: when the iron-containing salt solution, the alkali solution and the complexing agent solution are introduced into the base solution for reaction in the step (6), total metal ions in the iron-containing salt solution and OH in the alkali solution introduced in unit time are reacted - The molar ratio of (1).
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