CN105140489A - Titanium-doped carbon-coated sodium ferric phosphate material and preparation method thereof - Google Patents

Titanium-doped carbon-coated sodium ferric phosphate material and preparation method thereof Download PDF

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CN105140489A
CN105140489A CN201510617363.4A CN201510617363A CN105140489A CN 105140489 A CN105140489 A CN 105140489A CN 201510617363 A CN201510617363 A CN 201510617363A CN 105140489 A CN105140489 A CN 105140489A
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doped carbon
phosphoric acid
titanium doped
titanium
acid ferrisodium
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张宝
刘益
明磊
张佳峰
王小玮
童汇
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Central South University
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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/362Composites
    • 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
    • H01M4/13Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • H01M4/136Electrodes based on inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFy
    • 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
    • H01M4/13Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • H01M4/139Processes of manufacture
    • H01M4/1397Processes of manufacture of electrodes based on inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFy
    • 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
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    • H01M4/02Electrodes composed of, or comprising, active material
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    • H01M4/626Metals
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    • H01ELECTRIC ELEMENTS
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    • H01M2004/026Electrodes composed of, or comprising, active material characterised by the polarity
    • H01M2004/028Positive electrodes
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
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Abstract

The invention relates to a titanium-doped carbon-coated sodium ferric phosphate material and a preparation method thereof. The titanium-doped carbon-coated sodium ferric phosphate material is prepared by virtue of the following method: taking cane sugar as a carbon source, taking ethanol as a dispersing agent, ball milling FeC2O4, NaH2PO4.2H2O, cane sugar and TiO2 in the ethanol, drying, re-milling, and calcining, to obtain the titanium-doped carbon-coated sodium ferric phosphate material. The particle size of primary particles of the titanium-doped carbon-coated sodium ferric phosphate material is 100nm to 300nm, the titanium-doped carbon-coated sodium ferric phosphate material has characteristics of short sodium ion dispersion distance, high transmission rate, high specific surface area, high conductivity, high ion transmission speed and the like, and is excellent in electrochemical performance, capable of being used as a positive material of a secondary sodium-ion battery, high in safety, cheap in price, wide in application range and applicable to an energy storage device, a backup power supply, a reserved power supply and the like. The preparation method is low in synthetic temperature, simple in procedures, easy for obtaining raw materials and convenient in industrialization.

Description

A kind of titanium doped carbon coated phosphoric acid ferrisodium material and preparation method thereof
Technical field
The present invention relates to a kind of sodium-ion battery positive material and preparation method thereof, be specifically related to a kind of titanium doped carbon coated phosphoric acid ferrisodium material and preparation method thereof.
Background technology
From the nineties in 20th century, lithium ion battery, because having the advantages such as high-energy-density, quality be light, is now widely used in the electronic installations such as mobile device.But there is the defects such as price is high, reserves are limited in lithium ion battery.
CN102013496A discloses a kind of metallic titanium doped carbon-coating lithium iron phosphate and preparation method thereof, and its step is as follows: (1) is by lithium source, Fe 2o 3, TiO 2and NH 4h 2pO 4lithium in molar ratio: iron: titanium: the ratio of phosphorus=1:1-x:x:1 weighs prepares burden, wherein 0 < x≤0.2; (2) configured powder is added acetone to be placed on to rotate 2 ~ 10h under the speed of 200 ~ 500r/min in ball mill, the amount of acetone is 3 ~ 5 times of powder volume; (3) slurry in an oven at 100 ~ 110 DEG C after drying and grinding, the saturated aqueous solution adding citric acid afterwards makes the covert precursor of stream, and wherein the amount of citric acid is step (1) Raw lithium source, Fe by its phosphorus content 2o 3, TiO 2and NH 4h 2pO 420% of quality sum calculates; (4) by above-mentioned precursor under an inert atmosphere, heat up with the 1 DEG C/min rate of heat addition, in 100 DEG C of constant temperature 2 ~ 5h, then be warming up to 400 DEG C of constant temperature 3 ~ 6h, take out grinding with after stove cooling, under 100 ~ 200MPa pressure, be pressed into tight cylinder; (5) cylinder pressed is warming up to 500 ~ 900 DEG C of constant temperature calcining 5 ~ 15h under an inert atmosphere, is cooled to room temperature with stove and obtains the titanium doped carbon-covering lithium iron phosphate of anode material for lithium-ion batteries.Although the metallic titanium doped carbon-coating lithium iron phosphate of this method synthesis has higher specific discharge capacity, its cost is high, operating procedure is complicated, energy consumption is high.
Sodium-ion battery is lithium ion battery comparatively, and its cost of material is lower than lithium ion battery, and cell potential is higher than corresponding lithium ion battery current potential, and security performance is good.
The people such as AnnSun, FaithR.Beck (AnnSun, FaithR.Beck, etal.Synthesis, characterization, andelectrochemicalstudiesofchemicallysynthesizedNaFePO 4.materialsScienceandEngineering:B, Volume177, Issue20,1December2012, Pages1729-1733) with NaNO 3with Fe (NO 3) 29H 2o is raw material, adds citric acid and ethylene glycol, prepares NaFePO by sol-gel process 4presoma, at high temperature calcining obtains NaFePO 4material.Its concrete steps are as follows: the mol ratio of (1) metal ion total amount and citric acid and ethylene glycol is 1:0.5:0.5; (2) described sol gel reaction temperature is 60 DEG C, and the reaction time is 24h; (3) NaFePO 4presoma bake out temperature is 120 DEG C, and drying time is 24h; (4) described calcination atmosphere is inert atmosphere, and calcining heat is 550 ~ 600 DEG C.The NaFePO of this method synthesis 4though material cycle performance is higher, the capability retention after 30 times that circulates is that to enclose discharge capacity be 27.9mAhg to 138.1%(the 30th -1), but discharge capacity is not high, and 0.1C first discharge capacity is 20.2mAhg -1.
Summary of the invention
Technical problem to be solved by this invention is, overcome the above-mentioned defect that prior art exists, there is provided a kind of technique simple, be convenient to industrialization and control, product has high discharge capacity, titanium doped carbon coated phosphoric acid ferrisodium material of high rate cyclic superior performance and preparation method thereof.
The technical solution adopted for the present invention to solve the technical problems is as follows: a kind of titanium doped carbon coated phosphoric acid ferrisodium material, is made up: take sucrose as carbon source, ethanol is dispersant, by FeC of following methods 2o 4, NaH 2pO 42H 2o, sucrose and TiO 2carry out ball milling in ethanol, through drying, returning mill, after calcining, obtaining titanium doped carbon coated phosphoric acid ferrisodium material.
Further, be specifically made up of following methods:
(1) by FeC 2o 4, NaH 2pO 42H 2o, sucrose and TiO 2be placed in ball grinder according to the ratio of mol ratio 0.8 ~ 1.0:1:0.18 ~ 0.28:0.01 ~ 0.2, then add ethanol, mix, ball milling, dry, obtain presoma;
(2) step (1) gained presoma is placed in ball mill to carry out returning mill, obtains Powdered presoma;
(3) the Powdered presoma of step (2) gained is calcined under an inert atmosphere, obtain titanium doped carbon coated phosphoric acid ferrisodium material.
In step (1), FeC 2o 4, NaH 2pO 42H 2o and TiO 2ratio be according to synthesized presoma NaFe 1-xti xpO 4in (0.01≤x≤0.2) chemical formula, the mol ratio of each component is determined, each component addition too much or very few all can causing can not obtain target product or synthetic product poor-performing.
Further, in step (3), described calcining refers under an inert atmosphere, at 550 ~ 650 DEG C, and calcining 6 ~ 10h.The formation of final material is more conducive to, if the too high meeting of calcining heat causes material burning, if the too low meeting of calcining heat causes sintering insufficient under described calcination parameter condition.Due to glucose pyrogenetic decomposition under an inert atmosphere, make part carbon be coated on bulk material surface, being coated with of carbon is beneficial to the conductivity increasing material.
Further, in step (3), described calcining refers under an inert atmosphere, at 580 ~ 620 DEG C, and calcining 7 ~ 9h.
Further, in step (1), the ratio of described amount of alcohol added and material gross mass is 1 ~ 3:1.
Further, in step (1), the speed of described ball milling is 100 ~ 300r/min, and the time of ball milling is 3 ~ 7h.Described ball milling can make to be able to sufficient mechanical activation and dispersion between raw material, the milling intensity between the selection described raw material preferably of described ball milling speed and time conditions.
Further, in step (1), the speed of described ball milling is 150 ~ 250r/min, and the time of ball milling is 4 ~ 6h.
Further, in step (1), the temperature of described oven dry is 60 ~ 90 DEG C, and the time of oven dry is 10 ~ 24h.Oven dry can make material more easily carry out subsequent treatment, and whether described bake out temperature and time are according to the speed of drying materials and oxidizedly select.
Further, in step (2), described in return mill rotating speed be 100 ~ 200r/min, the time returning mill is 0.5 ~ 2h.Compare the ball milling of step (1), the rotating speed that step (2) returns mill is lower, time is shorter, returning mill can make material more even in follow-up sintering process, the selection returning abrasive stick part determines the impact of material pattern with returning to grind according to milling intensity, returning mill only need by non-Powdered presoma grinds powder, therefore time and rotating speed are all lower.
Further, in step (2), described in return mill rotating speed be 120 ~ 180r/min, the time returning mill is 0.8 ~ 1.5h.
Step (3) described inert atmosphere refers to that calcination process carries out under the protection such as high pure nitrogen, high-purity argon gas, high-purity gas purity >=99.99%.
The primary particle particle diameter of the carbon coated phosphoric acid ferrisodium material that the present invention is titanium doped is 100 ~ 300nm, has the characteristics such as sodium ion diffusion length is short, transmission rate fast, high-specific surface area, high conductivity, ion transfer are fast.Coated for titanium doped carbon phosphoric acid ferrisodium material is assembled into battery, and in 2.0 ~ 4.5V voltage range, under 1C multiplying power, first charge-discharge gram volume reaches as high as 63.7mAhg -1; In charge and discharge process, have good cycle performance due to stable structure, 1C circulates after 50 times, and capability retention can reach 96.8%, and electrode and electrolyte side reaction reduce.Titanium doped carbon coated phosphoric acid ferrisodium material list has revealed excellent chemical property, and can be used as the positive electrode of secondary sodium-ion battery, fail safe is high, and low price is widely used, and can be applicable to energy storage device, back-up source, redundant electrical power etc.Preparation method's synthesis temperature of the present invention is low, and step is simple, and raw material is easy to get, and is convenient to industrialization.
Accompanying drawing explanation
Fig. 1 is the XRD figure of the titanium doped carbon coated phosphoric acid ferrisodium material of the embodiment of the present invention 1 gained;
Fig. 2 is the SEM figure of the titanium doped carbon coated phosphoric acid ferrisodium material of the embodiment of the present invention 1 gained;
Fig. 3 is the EDX figure of the titanium doped carbon coated phosphoric acid ferrisodium material of the embodiment of the present invention 1 gained;
Fig. 4 is the 1C first charge-discharge curve chart of the titanium doped carbon coated phosphoric acid ferrisodium material of the embodiment of the present invention 1 gained;
Fig. 5 is 1C specific discharge capacity and the capability retention figure of the titanium doped carbon coated phosphoric acid ferrisodium material of the embodiment of the present invention 1 gained;
Fig. 6 is the 1C first charge-discharge curve chart of comparative example 1 gained carbon of the present invention coated phosphoric acid ferrisodium material.
Embodiment
Below in conjunction with embodiment and accompanying drawing, the invention will be further described.
The embodiment of the present invention uses high-purity argon gas purity >=99.99%; The density of the ethanol used is 0.789g/mL; Other chemical reagent used, if no special instructions, is all obtained by routine business approach.
embodiment 1
(1) by 0.09mol(12.96g) FeC 2o 4, 0.1mol(15.6g) NaH 2pO 42H 2o, 0.022mol(7.53g) sucrose and 0.01mol(0.8g) TiO 2be placed in ball grinder, then add 60mL ethanol as dispersant, mix, with the rotating speed ball milling 4h of 200r/min, then in an oven, dry 15h with 80 DEG C, obtain presoma; (2) step (1) gained presoma is placed in ball mill, returns mill 1h with the rotating speed of 150r/min, obtain Powdered presoma; (3) by the Powdered presoma of step (2) gained under high-purity argon gas, at 600 DEG C, calcining 8h, obtain the coated NaFePO of titanium doped carbon 4material.
As shown in Figure 1, the titanium doped carbon coated phosphoric acid ferrisodium positive electrode degree of crystallinity of gained is high, and crystal formation is complete, and what detect is phosphoric acid ferrisodium.
As shown in Figure 2, the primary particle of the carbon coated phosphoric acid ferrisodium positive electrode that gained is titanium doped is comparatively homogeneous, and spherical in class, and particle diameter is 100 ~ 300nm.
As shown in Figure 3, titanium is effectively doped in the titanium doped carbon of gained coated phosphoric acid ferrisodium positive electrode.
Battery is assembled: take the NaFePO that 0.24g the present embodiment gained is titanium doped respectively 4material is as positive electrode, add 0.03g acetylene black (SP) and make conductive agent and 0.03gPVDF(HSV-900) make binding agent, 2mLNMP dispersion mixing is added after abundant grinding, slurry on 16 μm of thick aluminium foils of sizing mixing evenly makes anode pole piece, in anaerobism glove box with sodium metal sheet for negative pole, with WhatmanGF/D glass fibre for barrier film, 1mol/LNaClO 4/ EC:PC(volume ratio 1:1) be electrolyte, be assembled into the button cell of CR2025.
As shown in Figure 4, by battery in 2.0 ~ 4.5V voltage range, under 1C multiplying power, surveying its first charge-discharge gram volume is 63.7mAhg -1.
As shown in Figure 5, by battery in 2.0 ~ 4.5V voltage range, under 1C multiplying power, circulate after 50 times, capability retention is 96.8%.
embodiment 2
(1) by 0.099mol(14.256g) FeC 2o 4, 0.1mol(15.6g) NaH 2pO 42H 2o, 0.019mol(6.5g) sucrose and 0.001mol(0.08g) TiO 2be placed in ball grinder, then add 120mL ethanol as dispersant, mix, with the rotating speed ball milling 3h of 100r/min, then in an oven, dry 10h with 60 DEG C, obtain presoma; (2) step (1) gained presoma is placed in ball mill, returns mill 0.5h with the rotating speed of 100r/min, obtain Powdered presoma; (3) by the Powdered presoma of step (2) gained under high-purity argon gas, at 550 DEG C, calcining 6h, obtain the coated NaFePO of titanium doped carbon 4material.
Battery is assembled: take the NaFePO that 0.24g the present embodiment gained is titanium doped respectively 4material is as positive electrode, add 0.03g acetylene black (SP) and make conductive agent and 0.03gPVDF(HSV-900) make binding agent, 2mLNMP dispersion mixing is added after abundant grinding, slurry on 16 μm of thick aluminium foils of sizing mixing evenly makes anode pole piece, in anaerobism glove box with sodium metal sheet for negative pole, with WhatmanGF/D glass fibre for barrier film, 1mol/LNaClO 4/ EC:PC(volume ratio 1:1) be electrolyte, be assembled into the button cell of CR2025, by battery in 2.0 ~ 4.5V voltage range, under 1C multiplying power, surveying its first charge-discharge gram volume is 51.9mAhg -1.
embodiment 3
(1) by 0.08mol(11.52g) FeC 2o 4, 0.1mol(15.6g) NaH 2pO 42H 2o, 0.0263mol(9.0g) sucrose and 0.02mol(1.6g) TiO 2be placed in ball grinder, then add 90mL ethanol as dispersant, mix, with the rotating speed ball milling 7h of 300r/min, then in an oven, dry 24h with 90 DEG C, obtain presoma; (2) step (1) gained presoma is placed in ball mill, returns mill 2h with the rotating speed of 200r/min, obtain Powdered presoma; (3) by the Powdered presoma of step (2) gained under high-purity argon gas, at 650 DEG C, calcining 10h, obtain the coated NaFePO of titanium doped carbon 4material.
Battery is assembled: take the NaFePO that 0.24g the present embodiment gained is titanium doped respectively 4material is as positive electrode, add 0.03g acetylene black (SP) and make conductive agent and 0.03gPVDF(HSV-900) make binding agent, 2mLNMP dispersion mixing is added after abundant grinding, slurry on 16 μm of thick aluminium foils of sizing mixing evenly makes anode pole piece, in anaerobism glove box with sodium metal sheet for negative pole, with WhatmanGF/D glass fibre for barrier film, 1mol/LNaClO 4/ EC:PC(volume ratio 1:1) be electrolyte, be assembled into the button cell of CR2025, by battery in 2.0 ~ 4.5V voltage range, under 1C multiplying power, surveying its first charge-discharge gram volume is 58.7mAhg -1.
comparative example 1
The difference of this comparative example technical scheme and embodiment 1 is only: in step (1), do not add TiO 2, finally obtain the coated NaFePO of carbon 4material.
Battery is assembled: take this comparative example of 0.24g gained NaFePO respectively 4material is as positive electrode, add 0.03g acetylene black (SP) and make conductive agent and 0.03gPVDF(HSV-900) make binding agent, 2mLNMP dispersion mixing is added after abundant grinding, slurry on 16 μm of thick aluminium foils of sizing mixing evenly makes anode pole piece, in anaerobism glove box with sodium metal sheet for negative pole, with WhatmanGF/D glass fibre for barrier film, 1mol/LNaClO 4/ EC:PC(volume ratio 1:1) be electrolyte, be assembled into the button cell of CR2025, by battery in 2.0 ~ 4.5V voltage range, under 1C multiplying power, surveying its first charge-discharge gram volume is 39.87mAhg -1, as shown in Figure 6.Illustrate compared with comparative example 1, the doping of embodiment 1 titanium is more conducive to the chemical property improving battery.

Claims (10)

1. a titanium doped carbon coated phosphoric acid ferrisodium material, is characterized in that, be made up of following methods: take sucrose as carbon source, ethanol is dispersant, by FeC 2o 4, NaH 2pO 42H 2o, sucrose and TiO 2carry out ball milling in ethanol, through drying, returning mill, after calcining, obtaining titanium doped carbon coated phosphoric acid ferrisodium material.
2. carbon titanium doped according to claim 1 coated phosphoric acid ferrisodium material, is characterized in that, be specifically made up of following methods:
(1) by FeC 2o 4, NaH 2pO 42H 2o, sucrose and TiO 2be placed in ball grinder according to the ratio of mol ratio 0.8 ~ 1.0:1:0.18 ~ 0.28:0.01 ~ 0.2, then add ethanol, mix, ball milling, dry, obtain presoma;
(2) step (1) gained presoma is placed in ball mill to carry out returning mill, obtains Powdered presoma;
(3) the Powdered presoma of step (2) gained is calcined under an inert atmosphere, obtain titanium doped carbon coated phosphoric acid ferrisodium material.
3. carbon titanium doped according to claim 2 coated phosphoric acid ferrisodium material, is characterized in that: in step (3), described calcining refers under an inert atmosphere, at 550 ~ 650 DEG C, and calcining 6 ~ 10h.
4. carbon titanium doped according to Claims 2 or 3 coated phosphoric acid ferrisodium material, is characterized in that: in step (3), described calcining refers under an inert atmosphere, at 580 ~ 620 DEG C, and calcining 7 ~ 9h.
5., according to the described titanium doped carbon of one of claim 2 ~ 4 coated phosphoric acid ferrisodium material, it is characterized in that: in step (1), the ratio of described amount of alcohol added and material gross mass is 1 ~ 3:1.
6., according to the described titanium doped carbon of one of claim 2 ~ 5 coated phosphoric acid ferrisodium material, it is characterized in that: in step (1), the speed of described ball milling is 100 ~ 300r/min, and the time of ball milling is 3 ~ 7h.
7., according to the described titanium doped carbon of one of claim 2 ~ 6 coated phosphoric acid ferrisodium material, it is characterized in that: in step (1), the speed of described ball milling is 150 ~ 250r/min, and the time of ball milling is 4 ~ 6h.
8., according to the described titanium doped carbon of one of claim 2 ~ 7 coated phosphoric acid ferrisodium material, it is characterized in that: in step (1), the temperature of described oven dry is 60 ~ 90 DEG C, and the time of oven dry is 10 ~ 24h.
9., according to the described titanium doped carbon of one of claim 2 ~ 8 coated phosphoric acid ferrisodium material, it is characterized in that: in step (2), described in return mill rotating speed be 100 ~ 200r/min, the time returning mill is 0.5 ~ 2h.
10., according to the described titanium doped carbon of one of claim 2 ~ 9 coated phosphoric acid ferrisodium material, it is characterized in that: in step (2), described in return mill rotating speed be 120 ~ 180r/min, the time returning mill is 0.8 ~ 1.5h.
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CN108039491A (en) * 2017-11-30 2018-05-15 华南理工大学 A kind of anode material of lithium-ion battery triphosphoric acid ferrisodium and preparation method thereof
CN109449417A (en) * 2018-11-01 2019-03-08 中科廊坊过程工程研究院 A kind of phosphoric acid ferrisodium composite positive pole and its preparation method and application
CN111477872A (en) * 2020-03-26 2020-07-31 合肥国轩电池材料有限公司 Water-based lithium/sodium ion battery with iron-doped sodium titanium phosphate as negative electrode active material and preparation method thereof
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CN114824205A (en) * 2022-04-15 2022-07-29 宁波市稻禾科技有限公司 Titanium-based fast ion conductor modified sodium iron phosphate positive electrode material, preparation method thereof and battery prepared from positive electrode material
CN115924878A (en) * 2023-01-15 2023-04-07 西安交通大学 Positive electrode material sodium iron phosphate for sodium ion battery and preparation method thereof
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CN115924878A (en) * 2023-01-15 2023-04-07 西安交通大学 Positive electrode material sodium iron phosphate for sodium ion battery and preparation method thereof
CN116750741A (en) * 2023-05-29 2023-09-15 浙江鑫钠新材料科技有限公司 Preparation method and application of titanium-doped carbon-coated sodium ferric pyrophosphate material
CN116750741B (en) * 2023-05-29 2024-09-06 浙江鑫钠新材料科技有限公司 Preparation method and application of titanium-doped carbon-coated sodium ferric pyrophosphate material
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