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CN113506866A - Carbon-coated Fe2O3Hard carbon composite material and preparation method thereof - Google Patents

Carbon-coated Fe2O3Hard carbon composite material and preparation method thereof Download PDF

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Publication number
CN113506866A
CN113506866A CN202110720807.2A CN202110720807A CN113506866A CN 113506866 A CN113506866 A CN 113506866A CN 202110720807 A CN202110720807 A CN 202110720807A CN 113506866 A CN113506866 A CN 113506866A
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carbon
hard carbon
composite material
coated
sintering
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CN113506866B (en
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时爽二
陈慧龙
戚昌伟
张立君
王瑛
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Shandong Yuhuang New Energy Technology 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
    • H01M4/48Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
    • H01M4/52Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of nickel, cobalt or iron
    • H01M4/523Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of nickel, cobalt or iron for non-aqueous cells
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/054Accumulators with insertion or intercalation of metals other than lithium, e.g. with magnesium or aluminium
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • 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
    • H01M4/583Carbonaceous material, e.g. graphite-intercalation compounds or CFx
    • H01M4/587Carbonaceous material, e.g. graphite-intercalation compounds or CFx for inserting or intercalating light metals
    • 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
    • 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
    • H01M4/628Inhibitors, e.g. gassing inhibitors, corrosion inhibitors
    • 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
    • H01M2004/027Negative 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

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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)
  • Materials Engineering (AREA)
  • Manufacturing & Machinery (AREA)
  • Battery Electrode And Active Subsutance (AREA)

Abstract

The application discloses carbon-coated Fe2O3A preparation method of a hard carbon composite material belongs to the technical field of sodium ion batteries. The method comprises the following steps: s1: washing leaves with water, drying and crushing to obtain leaf particles; s2: soaking the leaf particles in an iron salt solution, filtering the leaf particles, drying, calcining and crushing to obtain Fe2O3Hard carbon material of Fe2O3The grain diameter of the hard carbon material is 10-15 mu m, the porosity is 30-35 percent, and the pore diameter is 500nm-1 mu m; s3: subjecting said Fe to2O3Adding hard carbon material into organic carbon source liquid, mixing to obtain slurry, and subjecting the slurry to vacuum evaporationDrying, sintering and crushing the slurry to obtain the carbon-coated Fe2O3Hard carbon composite material, the carbon coated Fe2O3The grain diameter of the hard carbon composite material is 10.5-15.5 mu m, the porosity is 25-30%, and the pore diameter is 30nm-200 nm.

Description

Carbon-coated Fe2O3Hard carbon composite material and preparation method thereof
Technical Field
The present application relates to a carbon-coated Fe2O3A hard carbon composite material and a preparation method thereof belong to the technical field of sodium ion batteries.
Background
In recent years, the output and sales of China new energy automobiles are continuously increased and stably live at the first place in the world. However, the traditional lead-acid battery and nickel-cadmium battery have low energy efficiency and serious pollution, the lithium ion battery has high cost and needs to be improved in safety, and the market demand of new energy automobiles is increased rapidly, so that the market demand is difficult to meet. The sodium ion battery has the advantages of high safety, low cost, environmental friendliness and the like, is favored by researchers, and promotes the application of the sodium ion battery in the aspect of power batteries.
The hard carbon material is a non-graphitizable amorphous carbon material, has a short-range order and a long-range disorder structure, and can be described as amorphous carbon formed by disordered stacking of countless tiny graphite-like nano chips, wherein defects and gaps are filled. The hard carbon material has good physical and chemical stability due to the unique disordered structure, the carbon-based material has good electrical conductivity, and in addition, the hard carbon material can be obtained by pyrolysis of a high polymer material and a biomass material, so that the structural design is easy to carry out, and the hard carbon material is a good composite material substrate. However, when the hard carbon material is used as a negative electrode material of a battery, the battery has disadvantages of low reversible capacity, low first efficiency, low discharge voltage, and the like, and the use of the hard carbon material is limited.
Disclosure of Invention
In order to solve the above problems, a carbon-coated Fe is provided2O3Method for preparing/hard carbon composite material, carbon-coated Fe prepared by the method2O3The/hard carbon composite material can improve the sodium storage capacity of the material, improve the first charge-discharge efficiency of the hard carbon material, improve the conductivity when used as a battery cathode material, increase the specific capacity and the absorbable stress of a battery, and further improve the cycle and rate performance of the battery.
The carbon-coated Fe2O3The preparation method of the/hard carbon composite material comprises the following steps:
s1: washing leaves with water, drying and crushing to obtain leaf particles;
s2: soaking the leaf particles in an iron salt solution, filtering the leaf particles, drying, calcining and crushing to obtain Fe2O3Hard carbon material, said Fe2O3The grain diameter of the hard carbon material is 10-15 mu m, the porosity is 30-35 percent, and the pore diameter is 50-250 nm;
s3: subjecting said Fe to2O3Adding a hard carbon material into an organic carbon source liquid, mixing to obtain slurry, drying, sintering and crushing the slurry to obtain carbon-coated Fe2O3Hard carbon composite material, said carbon coated Fe2O3The grain diameter of the hard carbon composite material is 10.5-15.5 mu m, the porosity is 25-30%, and the pore diameter is 30nm-200 nm.
Preferably, the carbon-coated Fe2O3The porosity of the hard carbon composite material is 28-30%, and the pore diameter is 50nm-150 nm.
More preferably, the carbon-coated Fe2O3The ratio of the pores with the pore diameter of 80nm-100nm of the/hard carbon composite material is more than 50%, preferably more than 60%, more preferably more than 70%, and most preferably more than 75%, so that more sodium storage space can be provided, and the specific capacity of the battery can be improved.
Fe obtained by immersing leaves in a solution of an iron salt and subsequently calcining them together2O3The hard carbon material has unique dendritic grains on leaves, can provide more sites for embedding sodium ions after being calcined, has strong physical and chemical stability and structural design and ultrahigh theoretical specific capacity, can increase the specific capacity of the hard carbon material, improves the sodium storage capacity of the hard carbon, and can also be used as Fe2O3The buffer matrix of the material reduces the damage of the composite material to the electrode structure caused by volume expansion in the charging and discharging process.
In the synthesis of Fe2O3Adding the hard carbon material into organic carbon source liquid, sintering and crushing to obtain carbon-coated Fe2O3Hard carbonThe coated carbon shell can maintain the stability of the iron oxide material, fully play the synergistic effect of the iron oxide and the carbon, improve the electronic conductivity of the battery, form a short-range ordered carbon layer with larger micropores at the sintering temperature, facilitate the transmission and the attachment of sodium ions with larger ionic radius, improve the first charge-discharge efficiency of the hard carbon and further improve the cycle and the rate performance of the battery.
Synthetic carbon coated Fe2O3Hard carbon composite vs. Fe2O3Carbon coated Fe for hard carbon materials2O3The particle size of the hard carbon composite material is increased, but the change is not large, the pore diameter and the porosity are reduced, the specific surface area of the composite material can be increased, the electrolyte can be favorably permeated into the composite material, the migration rate of sodium ions in the charging and discharging process is improved, the occurrence of dead sodium is avoided, and the first effect and the circulation rate of a sodium ion battery are improved. The porosity of the composite material is favorable for the adsorption of ferric oxide, the specific capacity of the composite material is improved, a small part of ferric oxide is embedded into the pores, and the influence on the embedding and the de-embedding of sodium ions is small; the aperture of the composite material is beneficial to the embedding and the de-embedding of sodium ions, the aperture is too small, the embedding and the de-embedding of the sodium ions in the charging and discharging process are not facilitated, the aperture is too large, the volume expansion is serious in the sodium embedding process, the space between pole pieces is reduced, and the capacity of a battery cannot be normally exerted.
Optionally, the calcination temperature in the step S2 is 300-500 ℃, and the time is 1.5-5 h;
preferably, the calcination in step S2 is a staged calcination, stage I: the calcination temperature is 300-: the calcination temperature is 350-450 ℃, the calcination time is 30-90min, and the stage III: the calcination time is 450-500 ℃, and the calcination time is 30-200 min.
More preferably, stage I: the calcination temperature is 320-350 ℃, the calcination time is 30-50min, and the stage II: the calcination temperature is 400-450 ℃, the calcination time is 50-70min, and the stage III: the calcination time is 470-500 ℃, and the calcination time is 90-120 min.
Most preferably, stage I: calcination temperature 350 ℃, calcination time 40min, stage II: calcination temperature 420 ℃, calcination time 60min, stage iii: the calcination time is 480 ℃, and the calcination time is 100 min.
Calcining in stages at the temperature of 300-500 ℃ to obtain Fe2O3Hard carbon material, the calcining temperature is gradually increased, the initial calcining temperature is lower, the obtained ferric oxide and the components in the hard carbon material are incompletely reacted, the amorphous degree and the porosity of the hard carbon are increased, and the calcining temperature is increased later, so that Fe can be caused to be in an amorphous state2O3The porosity of the hard carbon material is ensured to be higher, and the ferric oxide and the components in the hard carbon material are further promoted to react, so that the obtained ferric oxide and the hard carbon material still keep amorphous, and the porosity can be in a higher range, so that the intercalation and deintercalation of sodium ions are facilitated, the migration rate of the sodium ions is facilitated to be improved, and the first efficiency of the battery is improved.
Optionally, the concentration of the iron salt solution is 2.5-3mol/L, preferably 2.5mol/L, the solvent in the iron salt solution is deionized water, and the weight ratio of the leaf particles to the iron salt solution is 0.01-0.5:1, preferably 0.2: 1.
Alternatively, the Fe2O3Fe in hard carbon material2O3The content of the iron salt solution is 2-5%, and the iron salt solution also comprises 1% of ethanol, 0.1-0.5% of magnesium carbonate and 0.2-1% of organic silicon resin.
The content of the ferric oxide is controlled to be 2% -5%, so that the high specific capacity of the ferric oxide can be exerted, and the over-high content can be avoided, so that the hard carbon sodium intercalation site is occupied, and the migration of sodium ions is not facilitated. The concentration of the iron salt solution is favorable for fully infiltrating leaf particles, magnesium carbonate and organic silicon resin are added into the iron salt, the magnesium carbonate and the organic silicon resin can be attached to the leaf particles together with the iron salt in the soaking process of the leaf particles, when the magnesium carbonate is calcined at the back, the magnesium carbonate can produce carbon dioxide, larger holes can be generated in the hard carbon material, sites are provided for the adsorption of the ferric oxide material, a magnesium oxide material is generated at the same time, and Fe can be stabilized2O3Hard carbon material structure, avoiding collapse of hard carbon material interior caused by over-high porosity, reducing hard carbon and electricityThe side reaction of the electrolyte can be cooperated with ferric oxide to further improve the specific capacity of the hard carbon material.
The organic silicon resin can increase the adsorption effect of the ferric oxide, improve the binding force of the ferric oxide and the hard carbon material, and avoid the ferric oxide from falling off in the charging and discharging processes, thereby influencing the specific capacity of the battery and improving the cycle rate of the battery. Meanwhile, part of the organic silicon resin is ablated in the sintering process of the step S3, and Fe coated with carbon2O3The hard carbon composite material generates holes inside and provides more sites for the intercalation and deintercalation of sodium ions, and preferably, the organic silicon resin is tetraethyl orthosilicate.
Optionally, the sintering temperature in the step S3 is 1000-1500 ℃, and the time is 5-15 h;
preferably, the sintering in the step S3 is staged sintering, and the step I: the sintering temperature is 1000-: the sintering temperature is 1100-: the sintering time is 1300-1500 ℃, and the sintering time is 1-1.5 h.
More preferably, stage I: sintering temperature 1050-: the sintering temperature is 1200-1250 ℃, the sintering time is 5-8h, and the stage III: the sintering time is 1350 ℃ and 1400 ℃, and the sintering time is 1-1.5 h.
Most preferably, stage I: sintering temperature 1050 ℃, sintering time 1.5h, stage II: sintering temperature 1200 ℃, sintering time 6h, stage III: the sintering time is 1350 ℃ and 1.5 h.
Sintering by stages to obtain carbon-coated Fe2O3The hard carbon composite material can enable hard carbon in the composite material to form a short-range ordered structure and a long-range disordered structure, the short-range ordered structure is favorable for adsorption of the surface of sodium ions, the long-range disordered structure is favorable for a large amount of embedding of the sodium ions, the sodium ions can be guaranteed to be rapidly separated in the discharging process of the sodium ion battery, and the first discharging efficiency of the battery is improved.
Optionally, the concentration of the organic carbon source solution is 1.0-2.0mol/L, preferably 1.5mol/L, and the Fe2O3Hard carbon material and the sameThe weight ratio of the organic carbon source solution is 1:5-10, preferably 1:6-8, and more preferably 1: 7. The proportion can ensure the uniform coating Fe of the carbon layer2O3Hard carbon material, forming a dense and uniform carbon layer.
Optionally, the carbon coating amount is 2% -8%, and the carbon-coated Fe2O3The thickness of the carbon coating layer in the hard carbon composite material is 20-50 nm. The carbon coating amount can promote Fe2O3And the composite material has enough sodium insertion sites under the synergistic action of the hard carbon, so that sodium ions can be conveniently inserted, and the capacity of the battery is further improved. The carbon coating amount is too small, the structure of the composite material is unstable, side reaction is easy to occur, the cycle performance of the battery is reduced, the carbon coating amount is too large, sodium intercalation sites can be occupied to a certain extent, and the specific capacity of the battery is reduced.
Optionally, the calcining in the step S2 and the sintering in the step S3 are both performed under a protective gas, and the protective gas is any one or more of nitrogen, argon and helium. Calcining and sintering under protective gas can reduce the adverse effect of harmful components (water and oxygen) in the atmosphere on the product, is helpful for removing impurities such as silicon, aluminum, magnesium, calcium and the like or oxides thereof, and plays a role of purifying materials.
Optionally, the leaf particles are mixed in the iron salt solution, then the iron salt solution is heated to 40-60 ℃, and is filtered after being soaked for 2-5h, wherein the mixing method is any one or more of ball milling, stirring and ultrasonic dispersion. The temperature of the ferric salt is controlled to be 40-60 ℃, which is beneficial to fully infiltrating leaf particles by the ferric salt solution and is convenient for the adsorption and combination of the ferric oxide and the hard carbon material.
Optionally, the negative ion of the iron salt is any one or more of acetate, propionate, oxalate, malonate, succinate, citrate, benzoic acid, phthalic acid, lactic acid, glycinate and salicylate, and is preferably citrate; the negative ions are stable and easy to dissolve in hot water, and the operation is simple.
The organic carbon source is any one or more of citric acid, sucrose, glucose, polyvinylpyrrolidone, starch, dextrin, polyaniline, asphalt, phenolic resin, epoxy resin and polyimide, preferably glucose, is easy to obtain and dissolve, has small influence on the environment, and is suitable for mass production.
According to yet another aspect of the present application, there is provided a carbon-coated Fe2O3A/hard carbon composite material prepared by the preparation method of any one of the above.
Benefits of the present application include, but are not limited to:
1. according to the preparation method of the composite material, the hard carbon material is obtained by calcining the unique dendritic grains in the leaves, more sites can be provided for the embedding of sodium ions, the iron oxide material is strong in physical and chemical stability and structural design, has ultrahigh theoretical specific capacity, can increase the specific capacity of the hard carbon material and improve the sodium storage capacity of the hard carbon, and meanwhile, the hard carbon material can also be used as Fe2O3The buffer matrix of the material reduces the damage of the composite material to the electrode structure caused by volume expansion in the charging and discharging process.
2. According to the method for preparing the composite material, the coated carbon shell can promote Fe2O3The hard carbon material plays a synergistic role, improves the specific capacity of the battery, stabilizes various performances of the battery, reduces the heat release of the battery during charging and discharging, improves the cycle performance of the battery, and prolongs the service life of the battery.
3. According to the preparation method of the composite material, the specific surface area of the composite material can be increased by 25-30% of the porosity, so that the migration of sodium ions in the composite material can be facilitated, the migration rate is increased, the occurrence of dead sodium is avoided, the energy density of a sodium ion battery is increased, the porosity is favorable for the adsorption of ferric oxide, and the specific capacity of the battery is increased.
4. According to the preparation method of the composite material, the small holes with the size of 30-50 nm are beneficial to the embedding and the de-embedding of sodium ions, the charging and discharging efficiency is improved, the holes with the size larger than 50nm are beneficial to the migration of the sodium ions in the hard carbon material, and the volume expansion in the sodium embedding is reduced.
Detailed Description
The present application will be described in detail with reference to examples, but the present application is not limited to these examples.
Unless otherwise specified, the raw materials and catalysts in the examples of the present application were all purchased commercially, and included iron salts, organic carbon sources, magnesium carbonate, and silicone resins.
The batteries manufactured in the examples and comparative examples of the present application were divided into three batches, five of which were manufactured for each batch, and the batteries were analyzed and tested after removing the defective products.
Analysis of the instrument information used for the test:
the types of the testing instruments of the grain diameter and the porosity are respectively as follows: mastersizer 3000, NOVA 2000e, pore size testing was performed using NOVA touch, a pore size analyzer, purchased from anto pa (shanghai) trade ltd, and the prepared composite material was subjected to electron microscope scanning to observe the pore size distribution.
The test uses the instrument model: CT-4008T-5V12A-S1-F, purchased from Shenzhen New Wille electronics, Inc.
Analysis and test conditions:
testing the first effect, the charge and discharge capacity and the energy density under the conditions that the voltage range is 1.0-4.2V and the current density is 0.1-5C;
and performing a discharge test of 100 cycles under the conditions that the voltage range is 1.0-4.2V and the current density is 1C to obtain the capacity retention rate after 100 cycles.
Example 1
(1) Washing leaves with water, drying and crushing to obtain leaf particles;
(2) and (2) placing the leaf particles in the step (1) in an iron salt solution, heating to 50 ℃ for soaking, wherein negative ions of iron salt are citrate, the concentration of the iron salt solution is 2.5mol/L, the iron salt solution comprises 1% of ethanol, 0.1% of magnesium carbonate and 1% of organic silicon resin, the weight ratio of the leaf particles to the iron salt solution is 0.2:1, soaking for 4 hours, filtering out the leaf particles, drying, calcining and crushing, wherein the calcining is divided into three stages, and the stage I is as follows: calcination temperature 350 ℃, calcination time 40min, stage II: calcination temperature 420 ℃, calcination time 60min, stage iii: the calcining time is 480 ℃, and the calcining time is 100 min;
(3) mixing the above Fe2O3Adding the hard carbon material into organic carbon source solution, and mixing to obtain slurry, wherein the concentration of the organic carbon source solution is 1.5mol/L, and Fe2O3The weight ratio of the hard carbon material to the organic carbon source solution is 1:7, the slurry is dried, sintered and crushed, and the sintering is divided into three stages, namely stage I: sintering temperature 1050 ℃, sintering time 1.5h, stage II: sintering temperature 1200 ℃, sintering time 6h, stage III: the sintering time is 1350 ℃, and the sintering time is 1.5 h;
thus obtaining the composite material 1 #.
Example 2
(1) Same as example 1;
(2) and (2) placing the leaf particles in the step (1) in an iron salt solution, heating to 50 ℃ for soaking, wherein negative ions of iron salt are citrate, the concentration of the iron salt solution is 2.5mol/L, the weight ratio of the leaf particles to the iron salt solution is 0.2:1, soaking for 4 hours, filtering out the leaf particles, drying, calcining and crushing, wherein the calcining is divided into three stages, and stage I: calcination temperature 350 ℃, calcination time 40min, stage II: calcination temperature 420 ℃, calcination time 60min, stage iii: the calcining time is 480 ℃, and the calcining time is 100 min;
(3) same as example 1;
thus obtaining the composite material No. 2.
Example 3
(1) Same as example 1;
(2) and (2) placing the leaf particles in the step (1) in an iron salt solution, heating to 50 ℃ for soaking, wherein negative ions of iron salt are citrate, the concentration of the iron salt solution is 0.5mol/L, the iron salt solution comprises 1% of ethanol, 0.1% of magnesium carbonate and 1% of organic silicon resin, the weight ratio of the leaf particles to the iron salt solution is 0.5:1, soaking for 4 hours, filtering out the leaf particles, drying, calcining and crushing, wherein the calcining is divided into three stages, and the stage I is as follows: calcination temperature 350 ℃, calcination time 40min, stage II: calcination temperature 420 ℃, calcination time 60min, stage iii: the calcining time is 480 ℃, and the calcining time is 100 min;
(3) same as example 1;
thus obtaining the composite material No. 3.
Example 4
(1) (2) same as example 1;
(3) mixing the above Fe2O3Adding the hard carbon material into organic carbon source solution, and mixing to obtain slurry, wherein the concentration of the organic carbon source solution is 1.5mol/L, and Fe2O3The weight ratio of the hard carbon material to the organic carbon source solution is 1:10, the slurry is dried, sintered and crushed, the sintering is divided into three stages, stage I: sintering temperature 1050 ℃, sintering time 1.5h, stage II: sintering temperature 1200 ℃, sintering time 6h, stage III: the sintering time is 1350 ℃, and the sintering time is 1.5 h;
thus obtaining the composite material No. 4.
Example 5
(1) (2) same as example 1;
(3) mixing the above Fe2O3Adding the hard carbon material into the organic carbon source solution, and mixing to obtain slurry, wherein the concentration of the organic carbon source solution is 0.5mol/L, and Fe2O3The weight ratio of the hard carbon material to the organic carbon source solution is 1:3, the slurry is dried, sintered and crushed, and the sintering is divided into three stages, namely stage I: sintering temperature 1050 ℃, sintering time 1.5h, stage II: sintering temperature 1200 ℃, sintering time 6h, stage III: the sintering time is 1350 ℃, and the sintering time is 1.5 h;
thus obtaining the composite material No. 5.
Comparative example 1
(1) Same as example 1;
(2) placing the leaf particles in the step (1) in an iron salt solution, heating to 50 ℃ for soaking, wherein negative ions of iron salt are citrate, the concentration of the iron salt solution is 2.5mol/L, the leaf particles comprise 1% of ethanol, 0.1% of magnesium carbonate and 1% of organic silicon resin, the weight ratio of the leaf particles to the iron salt solution is 0.2:1, soaking for 4 hours, filtering out the leaf particles, drying, calcining and crushing, the calcining temperature is 500 ℃, and the calcining time is 3 hours;
(3) same as in example 1.
Thus obtaining the comparative composite material No. 1.
Comparative example 2
(1) Same as example 1;
(2) and (2) placing the leaf particles in the step (1) in an iron salt solution, heating to 50 ℃ for soaking, wherein negative ions of iron salt are citrate, the concentration of the iron salt solution is 2.5mol/L, the iron salt solution comprises 1% of ethanol, 1% of magnesium carbonate and 5% of organic silicon resin, the weight ratio of the leaf particles to the iron salt solution is 0.2:1, soaking for 4 hours, filtering out the leaf particles, drying, calcining and crushing, wherein the calcining is divided into three stages, and the stage I is as follows: calcination temperature 350 ℃, calcination time 40min, stage II: calcination temperature 420 ℃, calcination time 60min, stage iii: the calcining time is 480 ℃, and the calcining time is 100 min;
(3) same as example 1;
thus obtaining the comparative composite material No. 2.
Comparative example 3
(1) (2) same as in example 1
(3) Mixing the above Fe2O3Adding the hard carbon material into organic carbon source solution, and mixing to obtain slurry, wherein the concentration of the organic carbon source solution is 1.5mol/L, and Fe2O3The weight ratio of the hard carbon material to the organic carbon source solution is 1:7, and the slurry is dried, sintered and crushed, wherein the sintering temperature is 1200 ℃, and the sintering time is 9 hours;
thus obtaining the comparative composite material No. 3.
The prepared composite material 1# -5# and the comparative composite material 1# -3# were tested for particle size, pore size and porosity, and the results are shown in table 1:
TABLE 1
Figure BDA0003136441920000101
Examples of the experiments
Respectively mixing the composite material No. 1-5 prepared in the embodiment and the comparative composite material No. 1-3 prepared in the comparative example, conductive carbon black and sodium carboxymethylcellulose according to a mass ratio of 80: 10: 10 mixing in deionized water, grinding into paste, coating on copper foil current collector, drying at 80 deg.C for 12 hr, cutting into pieces with diameter of 12mm, weighing, calculating the mass of hard carbon material (active substance), and adding argonIn the gas-shielded glove box, a metal sodium sheet is used as a positive electrode, glass fiber is used as a diaphragm, and 1mol/L NaClO is used4And the/PC solution is used as electrolyte, a 2032 button type half cell is assembled, and a sodium ion half cell is subjected to charge-discharge test in a constant current charge-discharge mode, wherein the voltage range is 1.0-4.2V. The test results are shown in table 2:
TABLE 2
Figure BDA0003136441920000111
The experimental data show that when the composite material prepared by the invention is used as the cathode material of the sodium ion battery, the side reaction of the cathode material and the electrolyte can be reduced, the cycle performance of the battery is improved, meanwhile, the pore diameter of the composite material is beneficial to the permeation of the electrolyte, the migration rate of sodium ions in the electrolyte is improved, the phenomenon of dead sodium is reduced, the first effect and the energy density of the sodium ion battery are improved, the adsorption of ferric oxide is facilitated, the specific capacity of the composite material is improved, the service life of the sodium ion battery is prolonged, and the large-scale production is facilitated.
The above description is only an example of the present application, and the protection scope of the present application is not limited by these specific examples, but is defined by the claims of the present application. Various modifications and changes may occur to those skilled in the art. Any modification, equivalent replacement, improvement, etc. made within the technical idea and principle of the present application should be included in the protection scope of the present application.

Claims (10)

1. Carbon-coated Fe2O3The preparation method of the/hard carbon composite material is characterized by comprising the following steps:
s1: washing leaves with water, drying and crushing to obtain leaf particles;
s2: soaking the leaf particles in an iron salt solution, filtering the leaf particles, drying, calcining and crushing to obtain Fe2O3Hard carbon material, said Fe2O3The grain diameter of the hard carbon material is 10-15 mu m,the porosity is 30-35%, and the pore diameter is 50-250 nm;
s3: subjecting said Fe to2O3Adding a hard carbon material into an organic carbon source liquid, mixing to obtain slurry, drying, sintering and crushing the slurry to obtain carbon-coated Fe2O3Hard carbon composite material, said carbon coated Fe2O3The grain diameter of the hard carbon composite material is 10.5-15.5 mu m, the porosity is 25-30%, and the pore diameter is 30nm-200 nm.
2. Carbon-coated Fe according to claim 12O3The preparation method of the hard carbon composite material is characterized in that the calcination temperature in the step S2 is 300-500 ℃, and the time is 1.5-5 h;
preferably, the calcination in step S2 is a staged calcination, stage I: the calcination temperature is 300-: the calcination temperature is 350-450 ℃, the calcination time is 30-90min, and the stage III: the calcination time is 450-500 ℃, and the calcination time is 30-200 min.
3. Carbon-coated Fe according to claim 22O3The preparation method of the hard carbon composite material is characterized in that the concentration of the ferric salt solution is 2.5-3mol/L, preferably 2.5mol/L, and the solvent in the ferric salt solution is deionized water;
the weight ratio of the leaf particles to the iron salt solution is 0.01-0.5:1, preferably 0.2: 1.
4. Carbon-coated Fe according to claim 12O3The preparation method of the hard carbon composite material is characterized in that the sintering temperature in the step S3 is 1000-1500 ℃, and the time is 5-15 h;
preferably, the sintering in the step S3 is staged sintering, and the step I: the sintering temperature is 1000-: the sintering temperature is 1100-: the sintering time is 1300-1500 ℃, and the sintering time is 1-1.5 h.
5. Carbon-coated Fe according to claim 42O3The preparation method of the hard carbon composite material is characterized in that the concentration of the organic carbon source solution is 1.0-2.0mol/L, preferably 1.5 mol/L;
said Fe2O3The weight ratio of the hard carbon material to the organic carbon source solution is 1:5-10, preferably 1: 7.
6. Carbon-coated Fe according to claim 52O3The preparation method of the hard carbon composite material is characterized in that the carbon coating amount is 2% -8%, and the carbon-coated Fe2O3The thickness of the carbon coating layer in the hard carbon composite material is 20-50 nm.
7. Carbon-coated Fe according to claim 12O3A method for producing a hard carbon composite material, characterized in that Fe is used2O3Fe in hard carbon material2O3The content of the iron salt solution is 2-5%, and the iron salt solution also comprises 1% of ethanol, 0.1-0.5% of magnesium carbonate and 0.2-1% of organic silicon resin.
8. Carbon-coated Fe according to claim 12O3The preparation method of the hard carbon composite material is characterized in that the calcination in the S2 step and the sintering in the S3 step are both carried out under a protective gas, and the protective gas is any one or more of nitrogen, argon and helium; and/or
The leaf particles are mixed in the ferric salt solution, then the ferric salt solution is heated to 40-60 ℃, soaked for 2-5h and then filtered, and the mixing method is any one or more of ball milling, stirring and ultrasonic dispersion.
9. Carbon-coated Fe according to claim 12O3The preparation method of the hard carbon composite material is characterized in that the negative ions of the ferric salt are acetate, propionate, oxalate, malonate, succinate, citrate, benzoic acid and phthalic acidAny one or more of lactic acid, glycinate and salicylate, preferably citrate;
the organic carbon source is any one or more of citric acid, sucrose, glucose, polyvinylpyrrolidone, starch, dextrin, polyaniline, asphalt, phenolic resin, epoxy resin and polyimide, and is preferably glucose.
10. Carbon-coated Fe2O3A/hard carbon composite material, characterized in that it is produced by the production method according to any one of claims 1 to 9.
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