CN117303450A - Preparation method and application of battery-grade sodium iron sulfate - Google Patents

Preparation method and application of battery-grade sodium iron sulfate Download PDF

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Publication number
CN117303450A
CN117303450A CN202311241015.2A CN202311241015A CN117303450A CN 117303450 A CN117303450 A CN 117303450A CN 202311241015 A CN202311241015 A CN 202311241015A CN 117303450 A CN117303450 A CN 117303450A
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sulfate
battery
sodium
atmosphere
iron sulfate
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孙杰
徐东
梅京
范宝安
吴大贝
何中林
何建豪
胡长春
黄龙清
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Hubei Rongtong High Tech Advanced Materials Group 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
    • 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
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01GCOMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
    • C01G49/00Compounds of iron
    • C01G49/009Compounds containing, besides iron, two or more other elements, with the exception of oxygen or hydrogen
    • 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
    • H01M4/581Chalcogenides or intercalation compounds thereof
    • 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
    • H01M4/62Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • H01M4/624Electric conductive fillers
    • H01M4/625Carbon or graphite
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2002/00Crystal-structural characteristics
    • C01P2002/70Crystal-structural characteristics defined by measured X-ray, neutron or electron diffraction data
    • C01P2002/72Crystal-structural characteristics defined by measured X-ray, neutron or electron diffraction data by d-values or two theta-values, e.g. as X-ray diagram
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2006/00Physical properties of inorganic compounds
    • C01P2006/40Electric properties

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Manufacturing & Machinery (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Battery Electrode And Active Subsutance (AREA)

Abstract

The invention provides a preparation method of battery-grade sodium iron sulfate, which comprises the following steps: preparing a mixed solution of ferrous sulfate, sodium sulfate and citric acid according to a certain proportion, keeping the mixed solution in an inert gas atmosphere or a reducing atmosphere, heating and stirring the mixed solution to form sol, and drying and crushing the sol to obtain a precursor; and sintering and crushing the precursor to obtain the battery-grade sodium iron sulfate. The battery grade ferric sodium sulfate prepared by the preparation method provided by the invention has high purity, complete and uniform particles and good electrochemical performance. Meanwhile, the preparation method has simple process flow and is suitable for large-scale industrial production. The invention also comprises a sodium ion battery using the battery-grade ferric sodium sulfate as an anode.

Description

Preparation method and application of battery-grade sodium iron sulfate
Technical Field
The invention relates to the technical field of batteries, in particular to a preparation method and application of battery-grade sodium iron sulfate.
Background
As a representative secondary battery with the highest comprehensive performance, commercialization of a lithium ion battery can be traced back to the 90 th century, and research on the lithium ion battery has been conducted for many years to have a mature battery technology route. However, lithium ion batteries are difficult to support in the current growing energy storage market, limited by the abundance of lithium element crust. The working principle of the sodium ion battery is similar to that of a lithium ion battery, the sodium salt reserves are rich, the exploitation is simple, and the method has more advantages in the large-scale application direction in the subsequent energy storage field.
The sodium ion battery mainly comprises a positive electrode, a negative electrode, electrolyte, a diaphragm and accessory parts. The positive and negative electrode materials are key to influence the performance of the sodium ion battery system, and the positive electrode materials are particularly prominent. The positive electrode materials of sodium ion batteries are classified into three main categories, namely transition metal oxides, prussian white/blue and polyanions. The positive electrode material of the polyanionic sodium ion battery has the advantages of stable structure and small volume change during charge and discharge. Among the positive electrode materials of the polyanionic sodium ion battery, the iron-based sodium battery has the advantages of lowest cost and no toxicity, wherein the sodium iron sulfate is a positive electrode material with higher performance, and has the advantages of low cost, environmental friendliness, high theoretical capacity and excellent cycle performance.
At present, aiming at the preparation of sodium iron sulfate, a preparation process of sintering and solidifying after ball milling and mixing is mainly adopted, the integrity of material particles can be damaged in the process of multiple ball milling, the particle size of the particles is difficult to regulate and control, uncontrollable factors can exist in the material performance, and in the process of ball milling, grinding aid ethanol is required to be added, so that potential safety hazards exist, and the large-scale industrialization is not facilitated.
Disclosure of Invention
In view of the above, the present invention aims to solve at least one of the technical problems existing in the prior art. Therefore, the invention provides a preparation method and application of battery-grade sodium iron sulfate. The preparation method provided by the invention can be used for preparing the battery-grade sodium iron sulfate with complete and uniform particles, and further can be used as a battery anode material to improve the utilization rate of the battery material. Meanwhile, the preparation method has simple process flow and is suitable for large-scale industrial production.
To this end, in a first aspect, an embodiment of the present invention provides a method for preparing battery-grade sodium iron sulfate, where the method includes:
s10, preparing a mixed solution of ferrous sulfate, sodium sulfate and citric acid according to a certain proportion, keeping the mixed solution in an inert gas atmosphere or a reducing atmosphere, heating and stirring the mixed solution to form sol, and drying and crushing the sol to obtain a precursor;
and S20, sintering and crushing the precursor to obtain the battery-grade sodium iron sulfate.
Preferably, the mixed solution of ferrous sulfate, sodium sulfate and citric acid is prepared according to a certain proportion, and specifically comprises the following steps: and preparing a mixed solution of ferrous sulfate, sodium hydroxide and citric acid according to a certain proportion.
Preferably, the inert gas atmosphere is a nitrogen atmosphere or an argon atmosphere; alternatively, the reducing atmosphere is a mixed atmosphere of 5% hydrogen and 95% inert gas, preferably, the inert gas is nitrogen or argon.
Preferably, the mixed solution of ferrous sulfate, sodium sulfate and citric acid is prepared according to a certain proportion, and specifically comprises the following steps: according to a certain proportion, preparing a mixed solution of ferrous sulfate, an additive, sodium sulfate and citric acid, wherein the additive comprises sulfate of at least one of manganese, nickel and cobalt.
Preferably, the molar ratio of the sodium element in the sodium sulfate to the iron element in the ferrous sulfate is 1.0.ltoreq.n (Na): n (Fe). Ltoreq.3.0; and/or the number of the groups of groups,
the carbon element in the citric acid accounts for 1-10% of the theoretical product sodium iron sulfate by weight; and/or the number of the groups of groups,
the heating temperature is 80-95 ℃; and/or the number of the groups of groups,
the sol is dried for 6-10 h at 70-90 ℃.
Preferably, the sintering of the precursor is controlled under certain temperature conditions; preferably, the temperature is raised to 150-250 ℃ at 3-5 ℃ per minute, kept for 2-6 hours, and then raised to 300-400 ℃ at 1-3 ℃ per minute, and kept for 12-30 hours.
Preferably, the sintering control of the precursor is performed under inert gas atmosphere or reducing atmosphere conditions.
Preferably, the inert gas atmosphere is a nitrogen atmosphere or an argon atmosphere; alternatively, the reducing atmosphere is a mixed atmosphere of 5% hydrogen and 95% inert gas, preferably, the inert gas is nitrogen or argon.
In a second aspect, the embodiment of the invention also provides a battery-grade sodium iron sulfate, which is prepared by the preparation method provided by the first aspect.
In a third aspect, an embodiment of the present invention further provides a sodium ion battery, where the sodium ion battery includes the positive electrode prepared from the battery-level sodium iron sulfate provided in the second aspect and the negative electrode of the sodium sheet.
The preparation method of the battery-grade sodium ferric sulfate provided by the embodiment of the invention has the advantages of simple process flow, high efficiency, no need of high-end equipment, no need of adding expensive reagents, low-cost and easily-obtained raw materials, and no involvement of toxic and harmful raw materials; the preparation method adopts a wet system for mixing, so that the uniformity of the materials in the coating and mixing process can be further ensured; citric acid is introduced, the citric acid can be used as a complexing agent of solution gel and also can be used as a carbon source of carbon coating, carbon after the citric acid is decomposed reacts in situ to form carbon coating on the surface of sodium ferric sulfate, the conductivity of the material is enhanced, and the electrochemical performance is improved.
Drawings
FIG. 1 is a flow chart of a method for preparing battery grade sodium iron sulfate according to an embodiment of the present invention;
FIG. 2 is an XRD pattern of battery grade sodium iron sulfate prepared in example 1 of the present invention;
FIG. 3 is an XRD pattern of battery grade sodium iron sulfate prepared in example 2 of the present invention;
fig. 4 is an XRD pattern of battery grade sodium iron sulfate prepared in comparative example 3 of the present invention.
Detailed Description
Embodiments of the present invention are described in detail below, examples of which are illustrated in the accompanying drawings, wherein like or similar reference numerals refer to like or similar elements or elements having like or similar functions throughout. The embodiments described below by referring to the drawings are illustrative and intended to explain the present invention and should not be construed as limiting the invention.
The following disclosure provides many different embodiments, or examples, for implementing different structures of the invention. In order to simplify the present disclosure, components and arrangements of specific examples are described below. They are, of course, merely examples and are not intended to limit the invention. Furthermore, the present invention may repeat reference numerals and/or letters in the various examples. This repetition is for the purpose of simplicity and clarity and does not in itself dictate a relationship between the various embodiments and/or configurations discussed. In addition, the present invention provides examples of various specific processes and materials, but one of ordinary skill in the art will recognize the applicability of other processes and/or the use of other materials.
Referring to fig. 1, the present invention aims to provide a method for preparing battery grade sodium iron sulfate, wherein the chemical formula of the sodium iron sulfate positive electrode material is as follows: na (Na) x Fe(SO4) y Wherein y= (x+2)/2; x is more than or equal to 1.0 and less than or equal to 3.0. The preparation method comprises the following steps:
s10, preparing a mixed solution of ferrous sulfate, sodium sulfate and citric acid according to a certain proportion, keeping the mixed solution in an inert gas atmosphere or a reducing atmosphere, heating and stirring the mixed solution to form sol, and drying and crushing the sol to obtain a precursor;
and S20, sintering and crushing the precursor to obtain the battery-grade sodium iron sulfate.
Specifically, in the step S10, ferrous sulfate, a sodium source and citric acid are weighed and dissolved in deionized water according to a certain proportion, then the mixed solution is kept to form sol under the condition of inert gas atmosphere or reducing atmosphere and heating and stirring, and the precursor is obtained after the sol is dried and crushed.
Further, the mixed solution of ferrous sulfate, sodium sulfate and citric acid is prepared according to a certain proportion, and specifically comprises the following steps: and preparing a mixed solution of ferrous sulfate, sodium hydroxide and citric acid according to a certain proportion. I.e. during the gelling of said step S10, a small amount of sodium hydroxide is further added. Wherein, the addition of sodium hydroxide solves the problem that the carboxyl of citric acid is relative to Fe 2+ The problem of lower complexing coefficient can further improve the Fe 2+ Is used as a complexing agent.
Specifically, the inert gas atmosphere is a nitrogen atmosphere or an argon atmosphere; alternatively, the reducing atmosphere is a mixed atmosphere of 5% hydrogen and 95% inert gas, preferably, the inert gas is nitrogen or argon. That is, during the heating and stirring process of the step S10, inert gas atmosphere such as nitrogen or argon or reducing atmosphere containing a small amount of hydrogen is introduced, which is more beneficial to Fe 2+ Is protected from oxidation.
Preferably, the mixed solution of ferrous sulfate, sodium sulfate and citric acid is prepared according to a certain proportion, and specifically comprises the following steps: according to a certain proportion, preparing a mixed solution of ferrous sulfate, an additive, sodium sulfate and citric acid, wherein the additive comprises sulfate of at least one of manganese, nickel and cobalt. In the embodiment, metal ions such as Mn, ni, co and the like are doped to replace Fe ions at the B site, so that the electronic conductivity of the material is improved, and the charge-discharge specific capacity of the material is further improved.
Further, in the step S10, the molar ratio of the sodium element in the sodium sulfate to the iron element in the ferrous sulfate is 1.0.ltoreq.n (Na): n (Fe). Ltoreq.3.0. The carbon element in the citric acid accounts for 1-10% wt of the theoretical product sodium iron sulfate. The heating temperature is 80-95 ℃. The sol is dried for 6-10 h at 70-90 ℃. Specifically, ferrous sulfate, a sodium source and citric acid are mixed according to sodium atoms and iron atoms X:1 (x is more than or equal to 1.0 and less than or equal to 3.0), adding citric acid according to the weight percent of carbon element of 1-10%, heating in water bath under stirring condition, wherein the water bath temperature is 80-95 ℃ until no obvious moisture is evaporated, transferring into a blast drying oven, drying for 6-10 hours at 70-90 ℃, and crushing and grinding to prepare the precursor.
Further, the step S20 includes:
sintering: sintering the precursor in a box furnace under a certain temperature condition to obtain a block material, and controlling the temperature and the atmosphere uniformity in the sintering process.
Crushing: and crushing the material obtained by sintering by a roller machine to obtain powder, namely the carbon-coated sodium iron sulfate anode material.
Wherein, the sintering of the precursor is controlled under a certain temperature condition; preferably, the temperature is raised to 150-250 ℃ at 3-5 ℃ per minute, kept for 2-6 hours, and then raised to 300-400 ℃ at 1-3 ℃ per minute, and kept for 12-30 hours. Specifically, the first stage temperature platform, namely 150-250 ℃, is used for removing moisture in the material; the first stage temperature platform, 300-400 deg.c, is the material sintering reaction temperature.
Wherein the sintering of the precursor is controlled under the condition of inert gas atmosphere or reducing atmosphere. Further, the inert gas atmosphere is a nitrogen atmosphere or an argon atmosphere; alternatively, the reducing atmosphere is a mixed atmosphere of 5% hydrogen and 95% inert gas, preferably, the inert gas is nitrogen or argon. Under the condition of inert gas atmosphere or reducing atmosphere, avoiding Fe 2+ Oxidation to Fe 3+
In a second aspect, the embodiment of the invention also provides a battery-grade sodium iron sulfate, which is prepared by the preparation method provided by the first aspect.
In a third aspect, an embodiment of the present invention further provides a sodium ion battery, where the sodium ion battery includes the positive electrode prepared from the battery-level sodium iron sulfate provided in the second aspect and the negative electrode of the sodium sheet.
The following describes the specific procedures and effects of the preparation method of battery grade sodium iron sulfate according to the present invention in further detail with reference to some specific examples, but is not limited to the scope of the present invention.
Example 1
The embodiment prepares the battery-grade sodium iron sulfate and the battery-grade anhydrous ferric hydrogen phosphate, and specifically comprises the following steps:
1. 2.78kg of ferrous sulfate heptahydrate, 1.42kg of sodium sulfate and 0.56kg of citric acid are weighed; wherein Na is 2 SO 4 FeSO 4 The molar ratio of the sodium atoms to the iron atoms is 2:1, and the carbon-based material accounts for 5 percent by weight
2. The raw materials are dissolved by deionized water and then heated in water bath under the stirring condition, the heating temperature is 80-95 ℃, and the gel is formed and then transferred into a blast drying oven for drying.
3. And crushing and grinding the dried substance to obtain a precursor.
4. Sintering the precursor at about 350 ℃, maintaining the temperature for 24 hours in nitrogen atmosphere, and obtaining the battery-grade sodium iron sulfate.
The XRD is used for analyzing the prepared battery grade sodium iron sulfate, and the result is shown in figure 2, and compared with a standard card, the synthesized battery grade sodium iron sulfate has the advantages of single phase, high purity, no impurity peak and good crystallinity.
Example 2
The embodiment prepares the battery-grade sodium iron sulfate and the battery-grade anhydrous ferric hydrogen phosphate, and specifically comprises the following steps:
1. 2.78kg of ferrous sulfate heptahydrate, 1.42kg of sodium sulfate and 0.896kg of citric acid are weighed; wherein Na is 2 SO 4 FeSO 4 The molar ratio of the sodium atoms to the iron atoms is 2:1, and the carbon-based material accounts for 8 percent by weight
2. The raw materials are dissolved by deionized water and then heated in water bath under the stirring condition, the heating temperature is 80-95 ℃, and the gel is formed and then transferred into a blast drying oven for drying.
3. And crushing and grinding the dried substance to obtain a precursor.
4. Sintering the precursor at about 350 ℃, maintaining the temperature for 24 hours in nitrogen atmosphere, and obtaining the battery-grade sodium iron sulfate.
The XRD is used for analyzing the prepared battery grade sodium iron sulfate, and the result is shown in figure 3, and compared with a standard card, the synthesized battery grade sodium iron sulfate has the advantages of single phase, high purity, no impurity peak and good crystallinity.
Example 3
The embodiment prepares the battery-grade sodium iron sulfate and the battery-grade anhydrous ferric hydrogen phosphate, and specifically comprises the following steps:
the preparation method of the carbon-coated sodium iron sulfate positive electrode material comprises the following steps:
1. 2.78kg of ferrous sulfate heptahydrate, 1.42kg of sodium sulfate and 0.56kg of citric acid are weighed; wherein Na is 2 SO 4 FeSO 4 The molar ratio of the sodium atoms to the iron atoms is 2:1, and the carbon-based material accounts for 5 percent by weight
2. The raw materials are dissolved by deionized water and then heated in water bath under the stirring condition, the heating temperature is 80-95 ℃, and the gel is formed and then transferred into a blast drying oven for drying.
3. And crushing and grinding the dried substance to obtain a precursor.
4. Sintering the precursor at about 375 ℃, maintaining the temperature for 24 hours in a nitrogen atmosphere, and obtaining the battery-grade anhydrous ferric hydrogen phosphate.
The XRD is used for analyzing the prepared battery grade sodium iron sulfate, and the result is shown in figure 4, and compared with a standard card, the synthesized battery grade sodium iron sulfate has the advantages of single phase, high purity, no impurity peak and good crystallinity.
Further, after adding an appropriate amount of NMP to the battery grade sodium iron sulfate, acetylene black and PVDF prepared in examples 1-3 in a mass ratio of 90:5:5, mixing and homogenizing, a black paste was coated on an aluminum foil using a 150 μm four-side preparer, and then the film was dried in a vacuum oven at 110℃for 6 hours. And punching the dried electrode film into a wafer with the same radius by using a sheet punching machine to obtain the positive electrode sheet. The metal sodium is used as a negative electrode plate, the diaphragm is a glass fiber membrane, the electrolyte is NaPF6/EC+DEC+DMC (EC: DEC: DMC=1:1:1 volume ratio), and the button cell is assembled in a glove box. The results of testing the first charge-discharge capacity, the discharge rate and the like are shown in table 1, and the battery prepared based on the above embodiment has good electrochemical performance and can meet the working requirements of the sodium ion button battery.
TABLE 1 button discharge capacity
The preparation method of the battery-grade sodium iron sulfate provided by the embodiment of the invention has the advantages of simple process flow, high efficiency, no need of high-end equipment, no need of adding expensive and practical materials, low-cost and easily-obtained raw materials, and no involvement of toxic and harmful raw materials; the preparation method adopts a wet system for mixing, so that the uniformity of the materials in the coating and mixing process can be further ensured; citric acid is introduced, the citric acid can be used as a complexing agent of solution gel and also can be used as a carbon source of carbon coating, carbon after the citric acid is decomposed reacts in situ to form carbon coating on the surface of sodium ferric sulfate, the conductivity of the material is enhanced, and the electrochemical performance is improved.
In the description of the present specification, a description referring to terms "one embodiment," "some embodiments," "examples," "specific examples," or "some examples," etc., means that a particular feature, structure, material, or characteristic described in connection with the embodiment or example is included in at least one embodiment or example of the present invention. In this specification, schematic representations of the above terms are not necessarily directed to the same embodiment or example. Furthermore, the particular features, structures, materials, or characteristics described may be combined in any suitable manner in any one or more embodiments or examples. Furthermore, the different embodiments or examples described in this specification and the features of the different embodiments or examples may be combined and combined by those skilled in the art without contradiction.
While embodiments of the present invention have been shown and described, it will be understood by those of ordinary skill in the art that: many changes, modifications, substitutions and variations may be made to the embodiments without departing from the spirit and principles of the invention, the scope of which is defined by the claims and their equivalents.

Claims (10)

1. A method for preparing battery-grade sodium iron sulfate, which is characterized by comprising the following steps:
s10, preparing a mixed solution of ferrous sulfate, sodium sulfate and citric acid according to a certain proportion, keeping the mixed solution in an inert gas atmosphere or a reducing atmosphere, heating and stirring the mixed solution to form sol, and drying and crushing the sol to obtain a precursor;
and S20, sintering and crushing the precursor to obtain the battery-grade sodium iron sulfate.
2. The method for preparing battery-grade sodium iron sulfate according to claim 1, wherein the preparing the mixed solution of ferrous sulfate, sodium sulfate and citric acid according to a certain proportion comprises the following steps: and preparing a mixed solution of ferrous sulfate, sodium hydroxide and citric acid according to a certain proportion.
3. The method for producing battery grade sodium iron sulfate according to claim 1, wherein the inert gas atmosphere is a nitrogen atmosphere or an argon atmosphere; alternatively, the reducing atmosphere is a mixed atmosphere of 5% hydrogen and 95% inert gas, preferably, the inert gas is nitrogen or argon.
4. The method for preparing battery-grade sodium iron sulfate according to claim 1, wherein the preparing the mixed solution of ferrous sulfate, sodium sulfate and citric acid according to a certain proportion comprises the following steps: according to a certain proportion, preparing a mixed solution of ferrous sulfate, an additive, sodium sulfate and citric acid, wherein the additive comprises sulfate of at least one of manganese, nickel and cobalt.
5. The method for producing battery-grade sodium iron sulfate according to claim 1, wherein a molar ratio of sodium element in the sodium sulfate to iron element in the ferrous sulfate is 1.0.ltoreq.n (Na): n (Fe). Ltoreq.3.0; and/or the number of the groups of groups,
the carbon element in the citric acid accounts for 1-10% of the theoretical product sodium iron sulfate by weight; and/or the number of the groups of groups,
the heating temperature is 80-95 ℃; and/or the number of the groups of groups,
the sol is dried for 6-10 h at 70-90 ℃.
6. The method for preparing battery grade sodium iron sulfate according to claim 1, wherein the sintering of the precursor is controlled under a certain temperature condition; preferably, the temperature is raised to 150-250 ℃ at 3-5 ℃ per minute, kept for 2-6 hours, and then raised to 300-400 ℃ at 1-3 ℃ per minute, and kept for 12-30 hours.
7. The method for producing battery grade sodium iron sulfate according to claim 1, wherein the sintering control of the precursor is performed under an inert gas atmosphere or a reducing atmosphere.
8. The method for producing battery grade sodium iron sulfate according to claim 1, wherein the inert gas atmosphere is a nitrogen atmosphere or an argon atmosphere; alternatively, the reducing atmosphere is a mixed atmosphere of 5% hydrogen and 95% inert gas, preferably, the inert gas is nitrogen or argon.
9. A battery grade sodium iron sulfate, characterized in that it is produced according to the production method of any one of claims 1-8.
10. A sodium ion battery comprising a positive electrode prepared from battery grade sodium iron sulfate according to claim 8 and a negative sodium sheet electrode.
CN202311241015.2A 2023-09-22 2023-09-22 Preparation method and application of battery-grade sodium iron sulfate Pending CN117303450A (en)

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