CN105552340A - Cathode material for lithium-ion battery and preparation method of cathode material - Google Patents

Cathode material for lithium-ion battery and preparation method of cathode material Download PDF

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CN105552340A
CN105552340A CN201610074046.7A CN201610074046A CN105552340A CN 105552340 A CN105552340 A CN 105552340A CN 201610074046 A CN201610074046 A CN 201610074046A CN 105552340 A CN105552340 A CN 105552340A
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lithium
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source compound
cathode material
life
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CN105552340B (en
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李靖
孙伟
李文
余心亮
何文祥
赵冲冲
施利勇
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Zhejiang Tianneng Energy Storage Technology Development Co.,Ltd.
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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/362Composites
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B82NANOTECHNOLOGY
    • B82YSPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
    • B82Y30/00Nanotechnology for materials or surface science, e.g. nanocomposites
    • 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
    • H01M10/052Li-accumulators
    • H01M10/0525Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
    • 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
    • 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
    • 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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Abstract

The invention discloses a cathode material for a lithium-ion battery and a preparation method of the cathode material. The cathode material LiFe<x>Mn<y>PO<4>/C for the lithium-ion battery has a spherical structure; a carbon coating is arranged on the outer surface; LiFe<x>Mn<y>PO<4> nanoparticles are contained in the cathode material; the particle sizes of the cathode material for the lithium-ion battery are 5-15 microns; the carbon content is 0.5%-10%; the tap density is 1.3-1.6g/cm<3>; x is smaller than or equal to 0.5 and greater than 0; y is smaller than 1 and greater than or equal to 0.5; and x+y is equal to 1. The nanoscale LiFe<x>Mn<y>PO<4> material is firstly prepared by a hydrothermal-solvothermal method; carbon-containing organic matters and the nanoscale LiFe<x>Mn<y>PO<4> material are mixed; spray drying is carried out; and a carbon-containing compound on the material surface after high-temperature calcination is transformed into a high-conductivity carbon material. The composite cathode material prepared by the method has excellent electrochemical properties, and has good application value for a power lithium-ion battery.

Description

A kind of anode material for lithium-ion batteries and preparation method thereof
Technical field
The present invention relates to technical field of lithium-ion battery, be specifically related to a kind of anode material for lithium-ion batteries and preparation method thereof.
Background technology
Along with lack of energy and to environmental protection requirement; lithium ion battery is clean as one, green battery is widely used; and anode material for lithium-ion batteries is limiting lithium ion cell extensive use in power; in current business-like positive electrode, LiFePO4 has the advantages such as fail safe is good, environmental friendliness, rate charge-discharge characteristic and good cycling stability, abundant raw materials cheapness; but its discharge voltage plateau lower (3.4V), thus have impact on the performance of its energy density.And lithium manganese phosphate has same olivine structural, theoretical gram volume is close to 170mAh/g, and its discharge voltage plateau higher (4.1V), theoretical energy density reaches 697Whkg -1, than the energy density (578Whkg of LiFePO4 -1) exceed 20%, but in charge and discharge process, there is Mn due to it 3+jahn-Teller effect cause the distortion of lattice, Mn 3+dissolving and the unfavorable factor such as lower lithium ion diffusion rate and electronic conductivity, thus cause electrical property effectively not play, so can in conjunction with the advantage of the two, the ratio of Reasonable Regulation And Control Mn and Fe, replaces Fe by the Mn of a part and prepares the lithium ferric manganese phosphate positive electrode with high-energy-density and high conductance.
Synthetic method at present about lithium ferric manganese phosphate has many preparation methods, as far back as 2005, publication No. is the preparation method that patent document discloses a kind of high-density spherical ferric lithium phosphate and iron manganese phosphate for lithium of CN1632970A, its method is first by ferrous sulfate, phosphorus source, complexing agent or add manganese sulfate more wherein, mixture aqueous solution is made in proportion after mixing, use ammonia spirit Reactive Synthesis ferrous ammonium phosphate or manganese phosphate ferrous ammonium presoma again, after washing is dry and lithium carbonate with mol ratio 1:1 Homogeneous phase mixing, under nitrogen atmosphere protection, within 8 ~ 48 hours, LiFePO4 or iron manganese phosphate for lithium is obtained through 600 ~ 900 DEG C of high-temperature heat treatment.But have use ammoniacal liquor in said method, cause preparation condition sometimes uncontrolled, operating environment is poor, not easily suitability for industrialized production.
Publication No. be CN103280579A patent document discloses a kind of high performance lithium ion battery anode material lithium ferric manganese phosphate and preparation method thereof.Utilize solid phase method to prepare lithium ferric manganese phosphate/carbon matrix precursor by after independent source of iron, manganese source, lithium source, phosphorus source and the mixing of carbon source ball milling, then prepare the lithium ferric manganese phosphate/carbon composite of Fe/Mn=4:6 through double sintering.But other mixes to use iron in the lithium ferric manganese phosphate prepared of the method just to reach molecular level by ball grinding method with manganese, is difficult to the Homogeneous phase mixing reaching iron and manganese atom rank, causes the consistency of material poor.
Publication No. is patent document discloses of CN104701536A is the technique that a kind of spray drying process prepares high-performance LiFePO4/C anode material of lithium battery.Its technical scheme is: by adding polyvinyl alcohol (PVA) additive as auxiliary template in precursor solution, adopts organic substance assistant spray seasoning successfully to prepare the high performance spherical LiFePO4/C anode material of lithium battery with secondary structure.Optimize addition and the presoma sintering temperature of PVA, improved process simultaneously, adapt to the needs of industrialization large-scale production.This characteristic feature of an invention is: the specimen material prepared using PVA as organic additive not only has beautiful pattern but also has very excellent chemical property.
Summary of the invention
Not enough for prior art, the invention provides a kind of anode material for lithium-ion batteries LiFe xmn ypO 4/ C and preparation method thereof, utilizes preparation method of the present invention to not only increase the chemical property of material, also improves the tap density of material simultaneously, have good using value for power lithium-ion battery.
A kind of anode material for lithium-ion batteries, be spherical structure, outer surface is carbon coating layer, and inside comprises LiFe xmn ypO 4nano particle, the particle diameter of described anode material for lithium-ion batteries is 5-15 μm, and carbon content is 0.5%-10%, and tap density is 1.3-1.6g/cm 3, wherein 0 < x≤0.5,0.5≤y < 1, x+y=1.
As preferably, the particle diameter of described anode material for lithium-ion batteries is 11.8-14.2 μm, and carbon content is 1.9-3.2%, and tap density is 1.32-1.54g/cm 3.
LiFe provided by the invention xmn ypO 4/ C composite positive pole material with carbon-coated surface is even, has higher specific capacity, can reach more than 150mAh/g; Coulombic efficiency is greater than 95% first; Circulate 100 conservation rates more than 94% under 0.5C.
As preferably, described LiFe xmn ypO 4the particle diameter 200-300nm of nano particle.
Present invention also offers a kind of preparation method of anode material for lithium-ion batteries, comprise the following steps:
(1) carry out hydro-thermal solvent thermal reaction with Li source compound, Fe source compound, manganese source compound, P source compound for raw material, by generate sediment washing, after drying, even with carbonaceous organic material aqueous solution, spraying dry obtains powder;
(2) under Buchholz protection, described powder is calcined, after described carbonaceous organic material carbonization, naturally cool to room temperature, then through grinding, sieving, obtained described anode material for lithium-ion batteries.
First preparation method of the present invention has prepared nanoscale LiFe by hydro-thermal solvent-thermal method xmn ypO 4material, then by carbonaceous organic material and nanoscale LiFe xmn ypO 4after material carries out mixed at high speed, carry out spraying dry, spraying dry can not only by nanoscale LiFe xmn ypO 4material is gathered into micron-sized ball-type second particle, meanwhile effectively carbon containing chemicals can be evenly spread to nanoscale LiFe xmn ypO 4the surface of material, after high-temperature calcination, the carbon compound of material surface is transformed into High-conductivity carbon material.
As preferably, in step (1), Li source compound, Fe source compound, manganese source compound, P source compound are 3.0:x:y:1.0 mixing according to Li:Fe:Mn:P mol ratio, wherein 0 < x≤0.5,0.5≤y < 1, x+y=1.More preferred, x is 0.5 or 0.25.
Described Li source compound is Li 2cO 3, LiNO 3, one or several in LiOH or LiAc.
Described Fe source compound is FeC 2o 4, Fe (Ac) 2, FeSO 4, FeCl 2or Fe (NO 3) 2in one or several.
Described manganese source compound is MnSO 4, MnCl 2, MnCO 3in one or several.
Described P source compound is H 3pO 4, NH 4h 2pO 4, (NH 4) 2hPO 4in one or several.
As preferably, described hydro-thermal solvent thermal reaction is using the mixture of organic solvent and water as reaction medium, and wherein the volume ratio of organic solvent and water is 1:1-10.In this reaction medium, effectively can not only shorten the migration distance of lithium ion, and in the method, the mixing of Fe and Mn reaches the mixing of atomic level, make that end product is dispersed and consistency is good.Described organic solvent is one or several in methyl alcohol, ethanol, glycerol, polyethylene glycol.More preferred, the volume ratio of glycerol and water is 1:1.
Regulate pH value in reaction between 6.0 ~ 12.0 by inorganic acid after raw material mixing, finally reactor sealing is reacted 5 ~ 24 hours at 140 ~ 240 DEG C.As preferably, pH value is 8.0 ~ 10.0, and more preferably, pH value is 8.0.Described inorganic acid is HCl, H 2sO 4, H 3pO 4, HAc, H 2c 2o 4in one or several.
In step (1), the sediment be obtained by reacting need be neutral by washed with de-ionized water to the pH value of solution, then the sediment after cleaning is obtained pale solid powder for 2 ~ 12 hours in 60 ~ 120 DEG C of vacuumizes is nanoscale LiFe xmn ypO 4material.
As preferably, described carbonaceous organic material is one or more in glucose, sucrose, ascorbic acid, polyvinyl alcohol or starch.
As preferably, in step (1), the mass ratio of sediment and carbonaceous organic material is 100:1-20.More preferred, the mass ratio of sediment and glucose is 100:10.
As preferably, in step (2), described gas is N 2, Ar, Ar/H 2mist or N 2/ H 2mist.
As preferably, in step (2), the condition of calcining is heat treatment 1 ~ 24 hour at 400 ~ 800 DEG C.
The beneficial effect that the present invention possesses: (1) the present invention adopts hydro-thermal solvent-thermal method to prepare nanometer LiFe xmn ypO 4, wherein the mixing of Fe and Mn reaches the mixing of atomic level, makes that end product is dispersed and consistency is good; (2) improve composite material tap density by spraying dry, make carbon compound be dispersed in second particle surface simultaneously, be conducive to subsequent calcination and form complete carbon coating layer, improve electric conductivity; (3) preparation method's technical process of the present invention is simple, cheap, is beneficial to enforcement, is very suitable for commercialization and applies.
Accompanying drawing explanation
Fig. 1 is lithium ion anode material preparation principle schematic diagram of the present invention.
Fig. 2 is ball-type LiFe of the present invention 0.5mn 0.5pO 4the SEM figure of/C composite positive pole.
Fig. 3 is the LiFe of Fig. 2 0.5mn 0.5pO 4the enlarged drawing of/C composite positive pole SEM figure.
Fig. 4 is the XRD elementary analysis figure that embodiment 3 obtains composite material.
Embodiment
Below in conjunction with embodiment, the invention will be further described; what be necessary to herein means out is that following examples can only be used for further illustrating for of the present invention; can not be interpreted as and limit protection scope of the present invention, nonessential improvement on this basis and adjustment still belong to protection scope of the present invention.
In order to reach technical purpose of the present invention, the technical solution used in the present invention as shown in Figure 1, specifically can comprise the steps:
Embodiment one
With LiOHH 2o, FeSO 47H 2o, MnCO 3, H 3pO 4for base stock, be that Li:Fe:Mn:P=3.0:0.5:0.5:1 joins respectively in the water and glycerol mixed solution that volume ratio is 1:1 to stir to move in reactor after 30 minutes and is heated to 180 DEG C according to mol ratio, react 5 hours, above-mentioned reactant concentration counts 0.5mol/L with lithium concentration, and passes through H 2sO 4reactant pH value is regulated to be 8.
After above-mentioned reaction completes, be neutral by the sediment deionized water of generation and ethanol purge to the pH value of solution, the sediment obtained obtains pale powder after dry 5 hours under 100 DEG C of vacuum conditions, above-mentioned pale powder and glucose are added in deionized water according to mass ratio 100:10, mix and carry out spraying dry after 2 hours, then by spray-dired powder at H 2under the protection of/Ar mist, under 600 DEG C of conditions, heat treatment naturally cooled to room temperature after 10 hours, and porphyrize sieves, and namely obtained ball-type LiFe 0.5mn 0.5pO 4/ C composite positive pole.SEM electron-microscope scanning result as shown in Figure 2 and Figure 3.
Embodiment two
With LiOHH 2o, FeSO 47H 2o, MnCO 3, H 3pO 4for base stock, be that Li:Fe:Mn:P=3.0:0.5:0.5:1 joins respectively in the water and glycerol mixed solution that volume ratio is 1:1 to stir to move in reactor after 30 minutes and is heated to 180 DEG C according to mol ratio, react 5 hours, above-mentioned reactant concentration counts 0.5mol/L with lithium concentration, and passes through H 2sO 4reactant pH value is regulated to be 10.
After above-mentioned reaction completes, be neutral by the sediment deionized water of generation and ethanol purge to the pH value of solution, the sediment obtained obtains pale powder after dry 5 hours under 100 DEG C of vacuum conditions, above-mentioned pale powder and glucose are added in deionized water according to mass ratio 100:10, mix and carry out spraying dry after 2 hours, then by spray-dired powder at H 2under the protection of/Ar mist, under 700 DEG C of conditions, heat treatment naturally cooled to room temperature after 10 hours, and porphyrize sieves, and namely obtained ball-type LiFe 0.5mn 0.5pO 4/ C composite positive pole.
Embodiment three
With LiOHH 2o, FeSO 47H 2o, MnCO 3, H 3pO 4for base stock, be that Li:Fe:Mn:P=3.0:0.25:0.75:1 joins respectively in the water and glycerol mixed solution that volume ratio is 1:1 to stir to move in reactor after 30 minutes and is heated to 180 DEG C according to mol ratio, react 5 hours, above-mentioned reactant concentration counts 0.5mol/L with lithium concentration, and passes through H 2sO 4reactant pH value is regulated to be 8.
After above-mentioned reaction completes, be neutral by the sediment deionized water of generation and ethanol purge to the pH value of solution, the sediment obtained obtains pale powder after dry 5 hours under 100 DEG C of vacuum conditions, above-mentioned pale powder and glucose are added in deionized water according to mass ratio 100:10, mix and carry out spraying dry after 2 hours, then by spray-dired powder at H 2under the protection of/Ar mist, under 700 DEG C of conditions, heat treatment naturally cooled to room temperature after 8 hours, and porphyrize sieves, and namely obtained ball-type composite positive pole.Through XRD elementary analysis, result as shown in Figure 4, proves that the composite material obtained is LiFe 0.25mn 0.75pO 4/ C composite positive pole.
Embodiment four
With LiOHH 2o, FeSO 47H 2o, MnCO 3, H 3pO 4for base stock, be that Li:Fe:Mn:P=3.0:0.25:0.75:1 joins respectively in the water and glycerol mixed solution that volume ratio is 1:1 to stir to move in reactor after 30 minutes and is heated to 180 DEG C according to mol ratio, react 5 hours, above-mentioned reactant concentration counts 0.5mol/L with lithium concentration, and passes through H 2sO 4reactant pH value is regulated to be 10.
After above-mentioned reaction completes, be neutral by the sediment deionized water of generation and ethanol purge to the pH value of solution, the sediment obtained obtains pale powder after dry 5 hours under 100 DEG C of vacuum conditions, above-mentioned pale powder and glucose are added in deionized water according to mass ratio 100:10, mix and carry out spraying dry after 2 hours, then by spray-dired powder at H 2under the protection of/Ar mist, under 750 DEG C of conditions, heat treatment naturally cooled to room temperature after 12 hours, and porphyrize sieves, and namely obtained ball-type LiFe 0.25mn 0.75pO 4/ C composite positive pole.
Embodiment five
With LiOHH 2o, FeSO 47H 2o, MnCO 3, H 3pO 4for base stock, be that Li:Fe:Mn:P=3.0:0.25:0.75:1 joins respectively in the water and glycerol mixed solution that volume ratio is 1:2 to stir to move in reactor after 30 minutes and is heated to 200 DEG C according to mol ratio, react 10 hours, above-mentioned reactant concentration counts 0.5mol/L with lithium concentration, and passes through H 2sO 4reactant pH value is regulated to be 10.
After above-mentioned reaction completes, be neutral by the sediment deionized water of generation and ethanol purge to the pH value of solution, the sediment obtained obtains pale powder after dry 5 hours under 100 DEG C of vacuum conditions, above-mentioned pale powder and glucose are added in deionized water according to mass ratio 100:10, mix and carry out spraying dry after 2 hours, then by spray-dired powder at H 2under the protection of/Ar mist, under 760 DEG C of conditions, heat treatment naturally cooled to room temperature after 10 hours, and porphyrize sieves, and namely obtained ball-type LiFe 0.25mn 0.75pO 4/ C composite positive pole.
Test example
The composite positive pole prepared by above-described embodiment carries out Performance Detection, and result is as shown in table 1.
Table 1

Claims (10)

1. an anode material for lithium-ion batteries, is characterized in that, be spherical structure, outer surface is carbon coating layer, and inside comprises LiFe xmn ypO 4nano particle, the particle diameter of described anode material for lithium-ion batteries is 5-15 μm, and carbon content is 0.5%-10%, and tap density is 1.3-1.6g/cm 3, wherein 0 < x≤0.5,0.5≤y < 1, x+y=1.
2. anode material for lithium-ion batteries as claimed in claim 1, is characterized in that, described LiFe xmn ypO 4the particle diameter 200-300nm of nano particle.
3. a preparation method for anode material for lithium-ion batteries, comprises the following steps:
(1) carry out hydro-thermal solvent thermal reaction with Li source compound, Fe source compound, manganese source compound, P source compound for raw material, by generate sediment washing, after drying, even with carbonaceous organic material aqueous solution, spraying dry obtains powder;
(2) under Buchholz protection, described powder is calcined, after described carbonaceous organic material carbonization, naturally cool to room temperature, then through grinding, sieving, obtained described anode material for lithium-ion batteries.
4. preparation method as claimed in claim 3, it is characterized in that, in step (1), Li source compound, Fe source compound, manganese source compound, P source compound are 3.0:x:y:1.0 mixing according to Li:Fe:Mn:P mol ratio, wherein 0 < x≤0.5,0.5≤y < 1, x+y=1.
5. preparation method as claimed in claim 3, is characterized in that, described hydro-thermal solvent thermal reaction is using the mixture of organic solvent and water as reaction medium, and wherein the volume ratio of organic solvent and water is 1:1-10.
6. preparation method as claimed in claim 5, is characterized in that, described organic solvent is one or several in methyl alcohol, ethanol, glycerol, polyethylene glycol.
7. preparation method as claimed in claim 3, it is characterized in that, in step (1), the mass ratio of sediment and carbonaceous organic material is 100:1-20.
8. preparation method as claimed in claim 3, it is characterized in that, described carbonaceous organic material is one or more in glucose, sucrose, ascorbic acid, polyvinyl alcohol or starch.
9. preparation method as claimed in claim 3, it is characterized in that, in step (2), described gas is N 2, Ar, Ar/H 2mist or N 2/ H 2mist.
10. preparation method as claimed in claim 3, is characterized in that, in step (2), the condition of calcining is heat treatment 1 ~ 24 hour at 400 ~ 800 DEG C.
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CN106784813A (en) * 2016-11-19 2017-05-31 天津赫维科技有限公司 A kind of preparation method of iron manganese phosphate lithium material
CN106784680A (en) * 2016-12-20 2017-05-31 山东精工电子科技有限公司 One-dimensional silicon-carbon cathode material and preparation method thereof
CN107768613A (en) * 2017-09-01 2018-03-06 上海交通大学 A kind of preparation method of the iron manganese phosphate for lithium of carbon coated
CN108408709A (en) * 2018-03-30 2018-08-17 南阳逢源锂电池材料研究所 A kind of preparation process of pollution-free inexpensive iron manganese phosphate for lithium crystalline material
CN108461786A (en) * 2016-12-10 2018-08-28 中国科学院大连化学物理研究所 A kind of preparation method and fuel cell of fuel cell membrane electrode
CN111816851A (en) * 2020-06-22 2020-10-23 南昌大学 Hierarchical porous LiMnxFe1-xPO4Template-free hydrothermal preparation method of/C composite microsphere cathode material
CN114843474A (en) * 2022-05-17 2022-08-02 天能新能源(湖州)有限公司 High-rate lithium ion battery positive electrode material and preparation method thereof
CN116374987A (en) * 2023-04-12 2023-07-04 安徽洁途新能源科技有限公司 Preparation method of lithium iron manganese phosphate

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CN104871350A (en) * 2012-12-21 2015-08-26 陶氏环球技术有限责任公司 Method for making lithium transition metal olivines using water/cosolvent mixtures
CN103137970A (en) * 2013-03-04 2013-06-05 中国科学院苏州纳米技术与纳米仿生研究所 Porous manganese phosphate lithium-carbon composite material and preparation method

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CN106784813A (en) * 2016-11-19 2017-05-31 天津赫维科技有限公司 A kind of preparation method of iron manganese phosphate lithium material
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CN107768613A (en) * 2017-09-01 2018-03-06 上海交通大学 A kind of preparation method of the iron manganese phosphate for lithium of carbon coated
CN108408709A (en) * 2018-03-30 2018-08-17 南阳逢源锂电池材料研究所 A kind of preparation process of pollution-free inexpensive iron manganese phosphate for lithium crystalline material
CN111816851A (en) * 2020-06-22 2020-10-23 南昌大学 Hierarchical porous LiMnxFe1-xPO4Template-free hydrothermal preparation method of/C composite microsphere cathode material
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CN116374987A (en) * 2023-04-12 2023-07-04 安徽洁途新能源科技有限公司 Preparation method of lithium iron manganese phosphate

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