CN104600273B - A kind of phosphorous anode material for lithium-ion batteries and preparation method thereof - Google Patents

A kind of phosphorous anode material for lithium-ion batteries and preparation method thereof Download PDF

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CN104600273B
CN104600273B CN201310524631.9A CN201310524631A CN104600273B CN 104600273 B CN104600273 B CN 104600273B CN 201310524631 A CN201310524631 A CN 201310524631A CN 104600273 B CN104600273 B CN 104600273B
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nickel
cobalt
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CN104600273A (en
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卢世刚
尹艳萍
庄卫东
卢华权
李永伟
王琳
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Youyan New Energy Materials (Jiangxi) Co.,Ltd.
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China Automotive Battery Research Institute 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
    • H01M4/50Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of manganese
    • H01M4/505Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of manganese of mixed oxides or hydroxides containing manganese for inserting or intercalating light metals, e.g. LiMn2O4 or LiMn2OxFy
    • 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
    • H01M4/131Electrodes based on mixed oxides or hydroxides, or on mixtures of oxides or hydroxides, e.g. LiCoOx
    • 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
    • H01M4/485Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of mixed oxides or hydroxides for inserting or intercalating light metals, e.g. LiTi2O4 or LiTi2OxFy
    • 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
    • H01M4/525Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of nickel, cobalt or iron of mixed oxides or hydroxides containing iron, cobalt or nickel for inserting or intercalating light metals, e.g. LiNiO2, LiCoO2 or LiCoOxFy
    • 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
    • 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
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    • Y02E60/10Energy storage using batteries

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Abstract

The present invention relates to a kind of phosphorous anode material for lithium-ion batteries and preparation method thereof.The group of phosphorous anode material for lithium-ion batteries becomes LiaMnbNicMdPeZfOg, wherein M is at least one of Co, Al, Ti, Fe, Cr, Cu, Zr, Mg, at least one of Z S, Si, and 0.95≤a<1.6,0≤b<1,0≤c≤0.9,0≤d≤0.5,0.001≤e<0.05,0≤f<0.2,1.95≤g<2.5.The method for preparing this positive electrode at least contains following 4 steps:1) with lithium source, phosphorus source, manganese source and nickel source, and selected from least one of cobalt source, silicon source, titanium source, source of iron, chromium source, copper source, zirconium source, magnesium source, and at least one of sulphur source and silicon source is selected from and is used as raw material, weigh corresponding raw material in molar ratio;2) liquid is added in the feed, is ground;3) ground slurry is dried;4) material after drying is roasted.This method and process process is simple, at low cost, and the positive electrode for being easy to industrialized production, and preparing in this way has high specific capacity.The invention further relates to use this material as the battery of active material.

Description

A kind of phosphorous anode material for lithium-ion batteries and preparation method thereof
Technical field
The present invention relates to field of lithium ion battery anode, specifically a kind of phosphorous anode material for lithium-ion batteries and Preparation method.
Background technology
The continuous development of industrial technology causes the getting worse of the present situations such as current resource, the shortage of the energy and environmental pollution, In recent years, the exploitation that policy promotes the development and new energy of energy-conserving and emission-cutting technology was competitively put into effect in countries in the world.Lithium ion battery because For have operating voltage it is high, it is light-weight, have extended cycle life, allow wide working range, memory-less effect, it is pollution-free the advantages that, and Extensive concern has been obtained, has become the oversize vehicles such as bus, electric vehicle, hybrid electric vehicle, it is electric bicycle, small-sized The major impetus source of the light electric vehicle such as platform batter car and electric tool.But lithium ion battery is as oversize vehicle Power battery is not met by requirement than various aspects of performance such as energy, cycle life, safeties.Inhibit power battery development Key factor be the positive electrode of battery, so develop novel positive electrode become now the most urgently solve ask Topic.
In recent years, rich lithium solid solution cathode material became the research hotspot of anode material for lithium-ion batteries, because it has Specific capacity height, good cycling stability, it is higher than energy the advantages that.Rich lithium solid-solution material is the Li by stratiform2MnO3And LiMO2(M= Mn, Ni, Co) by the solid solution of different proportion formation, chemical formula can be write as xLi2MnO3·(1-x)LiMO2Or xLi2O· yMOb(x/y>0.51).According to the literature, the method for preparing above-mentioned positive electrode have very much, as coprecipitation, sol-gal process, High temperature solid-state method, hydrothermal synthesis method etc., wherein coprecipitation is the most commonly used.A.Manthiram etc. is prepared for using coprecipitation Lithium-rich anode material Li&#91;Li0.2Mn0.54Ni0.13Co0.13]O2, first discharge specific capacity reaches 250mAh/g (J.Phys.Chem.C., 114 (2010) 9528-9533), but recycle and be short of with high rate performance, and preparation process engineering is multiple It is miscellaneous, it is of high cost, be not suitable for the large-scale production of industrialization.Samsung uses the compound L i of general formulaxMnA2(1)、 LixMnO2-zAz(2)、LixMn1-yM′yA2(3)、LixMn2A4(4)、LixMn2O4-zAz(5)、LixMn2-yM′yA4(6)、LixBO2 (7)、LixBO2-zAz(8)、LixB1-yM″yA2(9)、LixB1-yM″yO2-zAz(10)、LixNiCoA2(11)、LixNiCoO2-zAz (12)、LixNi1-y-zCoyM″zA2(13) (wherein 0<X≤1.5,0.01≤y≤0.1,0.01≤z≤0.5, M ' be selected from Al, Cr, At least one of Co, Mg, La, Ce, Sr, V, M " are to be selected from selected from least one of Al, Cr, Mn, Fe, Mg, LA, Ce, Sr, V, A O, F, S and P and B are selected from Ni or Co) and selected from semimetal, metal and its oxide composition anode active material composition (CN1181580C), this composition easily causes component and is unevenly distributed.Samsung, which chooses, states (1)~(13) general formula statement Compound, these compounds surface coating vanadic anhydride (CN1150645C), metal oxide (CN1209832C), Coating there are coating thickness not grade, complex technical process, operability poor the problems such as, to influence the performance of material, and increase Process costs.
Invention content
For above-mentioned anode material for lithium-ion batteries the problems of, the present invention provides a kind of phosphorous lithium-ion electric Pond positive electrode and preparation method thereof, and it is fabricated to the anode and lithium ion battery of lithium ion battery.Wherein, phosphorus is with phosphatic Form, which is added to, prepares phosphorous anode material for lithium-ion batteries in raw material, give phosphorus institute in anode material for lithium-ion batteries The range of accounting example can improve material high rate performance and cycle performance in this way, and then meet power battery to lithium ion battery The demand of positive electrode.
A kind of phosphorous anode material for lithium-ion batteries, chemical formula LiaMnbNicMdPeZfOg,
Wherein M is at least one of Co, Al, Ti, Fe, Cr, Cu, Zr, Mg, at least one of Z S, Si, and 0.95≤a< 1.6;0≤b≤1, preferably 0<B≤0.9, preferably 0.05≤b≤0.9;0≤c≤0.9, preferably 0.1≤c≤0.9;0≤d≤ 0.5;0.001≤e<0.050, preferably 0.001≤e≤0.040, preferably 0.006≤e≤0.020;0≤f<0.2, preferably 0.01 ≤ f≤0.15, preferably 0.02≤f≤0.05;1.95≤g<2.5.
It is one kind in consisting of according to positive electrode recited above: Li0.95Mn0.21Ni0.72Co0.19P0.04S0.01O2.03、Li1.17Mn0.52Ni0.12Co0.11P0.04S0.02O2.07、 Li1.18Mn0.53Ni0.14Co0.13P0.04S0.05O2.235、Li1.21Mn0.52Ni0.13Co0.12P0.02Si0.01O2.025、 Li1.21Mn0.53Ni0.13Co0.13P0.006Si0.02O2.14、LiMn0.25Ni0.52Co0.28Al0.049P0.001S0.05O2.116、 Li1.211Mn0.534Ni0.129Co0.124P0.002S0.05O2.144、LiMn0.055Ni0.75Co0.21Al0.12Mg0.08P0.005S0.05O2.08、 LiMn0.28Ni0.58Co0.18Al0.03Zr0.03P0.02S0.08O2.305、 Li0.98Mn0.28Ni0.78Co0.16Ti0.02Al0.02Mg0.03P0.03S0.01O2.261、 Li1.04Mn0.16Ni0.76Fe0.16Al0.05Mg0.03P0.006S0.05O2.11、Li1.5Mn0.453Ni0.28Cr0.15P0.007S0.01O2.209、 Li1.2Mn0.54Ni0.13Cr0.05Al0.03Mg0.03P0.02S0.03O2.1、Li1.17Mn0.50Ni0.29P0.04S0.05O2.125、 Li1.25Mn0.40Ni0.32Co0.05Mg0.05P0.04S0.05O2.12、LiMn0.35Ni0.582Mg0.20P0.008S0.01O2.032、 LiMn0.15Ni0.75Co0.15Cr0.05P0.04S0.02O2.01、Li1.2Mn0.6Ni0.15Cu0.05P0.02Si0.01O2.07、 Li1.35Mn0.52Ni0.15Cu0.08Cr0.03P0.006Si0.01O2.025、Li1.25Mn0.62Ni0.06Co0.02Cu0.03P0.03Si0.02O2.1、 Li0.95Mn0.28Ni0.70Al0.05Cu0.05P0.04Si0.05O2.06、Li1.25Mn0.62Ni0.06Co0.04P0.015Si0.1O2.223
The invention also provides a kind of methods for the positive electrode preparing phosphorous lithium ion battery, at least contain following 4 A step:1) with lithium source, phosphorus source, manganese source and nickel source, and selected from cobalt source, silicon source, titanium source, source of iron, chromium source, copper source, zirconium source and At least one of magnesium source and sulphur source and/or silicon source, weigh corresponding raw material in molar ratio;2) it presses solid content and is not more than 50 weights Measure % i.e. 0 weight %<The weight % of solid content≤50, surplus is liquid, liquid is added in the feed, carries out wet-milling, wherein liquid Body is water, ethyl alcohol or aqueous organopolysiloxane, and the concentration of aqueous organopolysiloxane is not more than 50 weight % i.e. 0 weight %<Aqueous organopolysiloxane The weight % of concentration≤50, remaining is water;3) ground slurry is dried;4) material after drying is roasted, is roasted It is 750~1100 DEG C to burn temperature, and preferred calcination temperature is 800~1000 DEG C, and roasting time is 5~60h.
Lithium source is at least one of anhydrous lithium hydroxide, the water lithium hydroxide containing crystallization, lithium carbonate;Phosphorus source is phosphate, excellent Select at least one of dihydrogen phosphate, ammonium di-hydrogen phosphate, phosphoric acid ammonia;Manganese source is manganese metal, manganese monoxide, manganese dioxide, carbonic acid At least one of manganese;Nickel source is at least one of metallic nickel, nickel protoxide, nickel sesquioxide, nickel hydroxide, nickelous carbonate;Cobalt source For at least one of metallic cobalt, cobaltosic oxide, cobalt sesquioxide, cobalt protoxide, cobalt hydroxide, cobalt carbonate;Silicon source is metal At least one of aluminium, alundum (Al2O3), aluminium hydroxide;Titanium source is at least one of titanium dioxide or titanium isopropoxide;Source of iron is At least one of metallic iron, di-iron trioxide, ferroso-ferric oxide, iron hydroxide or ferrous hydroxide;Chromium source is crome metal, three oxygen Change at least one of two chromium, chromium hydroxide;Copper source is at least one of copper oxide, cuprous oxide, copper carbonate;Zirconium source is oxidation At least one of zirconium, zirconium hydroxide;Magnesium source is at least one of magnesium carbonate, magnesia;Manganese source, nickel source and cobalt source are closed for manganese nickel cobalt At least one of gold, manganous hydroxide nickel cobalt, hydroxyl oxidation manganese nickel cobalt, oxalic acid manganese nickel cobalt, carbonic acid manganese nickel cobalt, oxidation manganese nickel cobalt;Manganese Source and nickel source are at least one in manganese-nickel, manganous hydroxide nickel, hydroxyl manganese oxide nickel, manganese oxalate nickel, manganese carbonate nickel, manganese oxide nickel Kind;Manganese source and cobalt source are in manganese cobalt alloy, manganous hydroxide cobalt, hydroxyl manganese oxide cobalt, manganese oxalate cobalt, manganese carbonate cobalt, manganese oxide cobalt It is at least one;Nickel source and cobalt source are nickel cobalt (alloy), hydroxide nickel cobalt, hydroxy cobalt nickel oxide, oxalic acid nickel cobalt, carbonic acid nickel cobalt, oxidation At least one of nickel cobalt;Sulphur source is the hydride of sulfate, sulphite, sulfur oxide or sulphur, the sulphur in preferably sulfuric acid salt At least one of sour nickel or ammonium sulfate.Silicon source is silica.The liquid used in process of lapping is deionized water, ethyl alcohol, second At least one of the aqueous solution of alcohol, PVA aqueous solutions, aqueous sucrose solution;Dry slurry is using vacuum drying, forced air drying, spraying At least one of dry, microwave drying;The temperature of roasting is 800~1000 DEG C.
The positive electrode prepared according to the method described above is mixed with conductive carbon and bonding agent, and obtained mixture is applied Apply the anode that the lithium ion battery is formed on support conducting base.By the anode anode compatible with electricity, diaphragm, electrolyte It is placed in container and forms lithium ion battery.
It is mixed with conductive agent, binder with the positive electrode prepared by the method for the present invention, dissolving in organic solvent, is formed Anode sizing agent is coated on supporter, makes the anode of lithium ion battery.
Using this anode, and the cathode for selecting the positive electrode electricity prepared with the present invention compatible is as the negative of lithium ion battery Diaphragm, electrolyte is added in pole, forms lithium ion battery.
It is an advantage of the invention that:
Compared with prior art, the present invention provides a kind of phosphorous anode material for lithium-ion batteries and preparation method thereof, This positive electrode has higher chemical property, and simple for process, is readily synthesized material, to reduce cost, favorably In industrialization continuous production.
Description of the drawings
Fig. 1 be synthetic example 1 of the present invention, 4 positive electrode of embodiment 2, embodiment 3 and embodiment X-ray diffractogram The full spectrum &#91 of spectrum;Fig. 1 a&#93;&#91 is composed in amplification with 18~19.5 °;Fig. 1 b&#93;.
Fig. 2 be the present invention synthesize embodiment 1,4 positive electrode of embodiment 2, embodiment 3 and embodiment in 0.1C, 4.8 The first charge-discharge curve comparison figure of material under~2.0V.
Fig. 3 be the present invention synthesize embodiment 1,4 positive electrode of embodiment 2, embodiment 3 and embodiment in 0.1C, 4.8 The high rate performance curve comparison figure of material under~2.0V.
Fig. 4 be the present invention synthesize embodiment 4 and comparative example 1, comparative example 2 and comparative example 3 in 4.8~2.0V, material First charge-discharge curve comparison figure.
Fig. 5 be the present invention synthesize embodiment 4 and comparative example 1, comparative example 2 and comparative example 3 in 4.8~2.0V, material High rate performance curve comparison figure.
Specific implementation mode
Technical scheme of the present invention is further described with embodiment below, contributes to the preparation method to the present invention It is further understood from, protection scope of the present invention is not limited to the examples, and protection scope of the present invention is wanted by right Book is sought to determine.
Embodiment 1:
Prepare Li1.204Mn0.533Ni0.132Co0.131P0.001O2.02, weigh 52.052g lithium carbonates, 71.692g manganese carbonates, 12.304g cobaltosic oxides, 11.537g nickel protoxides and 0.136g ammonium dihydrogen phosphates, mixing are added 1000g deionized waters, add It after entering into grinder grinding, is spray-dried, the powder obtained after point spray drying is through 900 DEG C of calcination 36h, with furnace cooling But, the powder of acquisition is ground, and crosses 300 mesh sieve.
Embodiment 2:
Prepare Li1.18Mn0.53Ni0.14Co0.13P0.04S0.05O2.235, weigh 52.246g lithium carbonates, 73.010g manganese carbonates, 12.505g cobaltosic oxides, 12.531g nickel protoxides, 5.512g ammonium dihydrogen phosphates and 7.918g ammonium sulfate mix, and are added 1000g deionized waters are added to after being ground in grinder, are spray-dried, and the powder obtained after point spray drying is through 900 DEG C calcination 36h, the powder of furnace cooling, acquisition is ground, and crosses 300 mesh sieve.
Embodiment 3:
Prepare Li1.21Mn0.53Ni0.13Co0.13P0.006Si0.02O2.4, weigh 48.615g lithium carbonates, 66.252g manganese carbonates, 11.347g cobaltosic oxides, 10.559g nickel protoxides, 0.750g ammonium dihydrogen phosphates and 1.307g silica mix, and are added 1000g deionized waters are added to after being ground in grinder, are spray-dried, and the powder obtained after point spray drying is through 900 DEG C calcination 36h, the powder of furnace cooling, acquisition is ground, and crosses 300 mesh sieve.
Embodiment 4:
Prepare Li1.21Mn0.52Ni0.13Co0.12P0.02Si0.01O2.025, weigh 52.612g lithium carbonates, 70.346g manganese carbonates, 11.335g cobaltosic oxides, 11.427g nickel protoxides, 2.706g ammonium dihydrogen phosphates and 0.707g silica mix, and are added 800g deionized waters are added to after being ground in grinder, are spray-dried, and the powder obtained after point spray drying is through 900 DEG C calcination 36h, the powder of furnace cooling, acquisition is ground, and crosses 300 mesh sieve.
Embodiment 5:
Prepare Li1.211Mn0.534Ni0.129Co0.124P0.002S0.05O2.144, weigh 54.038g lithium carbonates, 74.137g carbonic acid Manganese, 12.021g cobaltosic oxides, 11.637g nickel protoxides, 0.278g ammonium dihydrogen phosphates and 15.874g nickel sulfates, mixing, add Enter 1000g deionized waters, is added to after being ground in grinder, is spray-dried, the powder warp obtained after point spray drying 900 DEG C of calcination 48h, the powder of furnace cooling, acquisition are ground, and cross 300 mesh sieve.
Embodiment 6:
Prepare Li1.17Mn0.50Ni0.29P0.04S0.05O2.125, weigh 48.323g lithium carbonates, 64.250g manganese carbonates, 24.214g nickel protoxides, 5.141g ammonium dihydrogen phosphates and 14.292g nickel sulfates, mixing are added 1000g deionized waters, are added to After being ground in grinder, it is spray-dried, the powder that obtains is through 900 DEG C of calcination 48h after point spray drying, furnace cooling, The powder of acquisition is ground, and crosses 300 mesh sieve.
Embodiment 7:
Prepare Li1.17Mn0.50Ni0.29P0.04S0.05O2.125, weigh 48.323g lithium carbonates, 48.595g manganese dioxide, 1000g deionizations are added in 26.806g11.520g nickel sesquioxides, 5.141g ammonium dihydrogen phosphates and 7.386g ammonium sulfate, mixing Water is added to after being ground in grinder, is spray-dried, and the powder obtained after point spray drying is calcined 48h through 900 DEG C, The powder of furnace cooling, acquisition is ground, and crosses 300 mesh sieve.
Embodiment 8:
Prepare Li1.2Mn0.54Ni0.13Cr0.05Al0.03Mg0.03P0.02S0.03O2.1, weigh 54.801g lithium carbonates, 76.725g Manganese carbonate, 12.002g nickel protoxides, 3.214g crome metals, 2.094g alundum (Al2O3)s, 1.495g magnesia, 2.842g phosphoric acid 1000g deionized waters are added in ammonium and 4.900g ammonium sulfate, mixing, are added to after being ground in grinder, carry out microwave drying, warp The powder obtained after drying is ground through 900 DEG C of calcination 36h, the powder of furnace cooling, acquisition, crosses 300 mesh sieve.
Embodiment 9:
Prepare Li1.35Mn0.52Ni0.15Cu0.08Cr0.03P0.006Si0.01O2.025, weigh 60.717g lithium carbonates, 55.035g bis- Manganese oxide, 10.717g metallic nickels, 7.747g copper oxide, 1.900g crome metals, 0.840g ammonium dihydrogen phosphates and 0.732g titanium dioxides 1000g deionized waters are added in silicon, mixing, are added to after being ground in grinder, are dried in vacuo, the powder obtained after drying Body is ground through 900 DEG C of calcination 36h, the powder of furnace cooling, acquisition, crosses 300 mesh sieve.
Embodiment 10:
Prepare Li1.25Mn0.62Ni0.06Co0.02Cu0.03P0.03Si0.02O2.1, weigh 54.694g lithium carbonates, 63.838g dioxies Change manganese, 4.170g metallic nickels, 1.396g metallic cobalts, 2.826g copper oxide, 4.085g ammonium dihydrogen phosphates and 1.423g silica, 1000g deionized waters are added in mixing, are added to after being ground in grinder, carry out microwave drying, the powder warp obtained after drying 900 DEG C of calcination 12h, the powder of furnace cooling, acquisition are ground, and cross 300 mesh sieve.
Embodiment 11:
Prepare Li1.2Mn0.6Ni0.15Cu0.05P0.02Si0.01O2.07, weigh 50.787g lithium carbonates, 59.756g manganese dioxide, 1000g is added in 12.834g nickel protoxides, 4.556g copper oxide, 3.024g diammonium hydrogen phosphates and 0.688g silica, mixing Deionized water is added to after being ground in grinder, carries out forced air drying, and the powder obtained after drying is calcined for 24 hours through 950 DEG C, The powder of furnace cooling, acquisition is ground, and crosses 300 mesh sieve.
Embodiment 12:
Prepare Li1.25Mn0.62Ni0.06Co0.04P0.015Si0.1O2.223, weigh 52.834g lithium carbonates, 81.486g manganese carbonates, 5.124g nickel protoxides, 3.671g cobaltosic oxides, 1.672g ammonium dihydrogen phosphates and 6.871g silica mix, and are added 1200g deionized waters are added to after being ground in grinder, are spray-dried, and the powder obtained after point spray drying is through 950 DEG C calcination 12h, the powder of furnace cooling, acquisition is ground, and crosses 300 mesh sieve.
Embodiment 13
Prepare Li1.15Ni0.52Co0.15Al0.05Ti0.30P0.006Si0.01O2.03, weigh 44.259g lithium carbonates, 24.182g oxygen Change sub- nickel, 12.993g cobaltosic oxides, 3.047g alundum (Al2O3)s, 43.099g titanium dioxide, 0.745g ammonium dihydrogen phosphates and 1200g deionized waters are added in 0.649g silica, mixing, are added to after being ground in grinder, are spray-dried, through dividing The powder obtained after spray drying is ground through 950 DEG C of calcination 12h, the powder of furnace cooling, acquisition, crosses 300 mesh sieve.
Embodiment 14
Prepare Li1.2Mn0.6Co0.10Cu0.05P0.02S0.01O2.07, weigh 52.514g lithium carbonates, 81.693g manganese carbonates, 9.507g cobaltosic oxides, 2.724g ammonium dihydrogen phosphates and 1.565g ammonium sulfate, mixing are added 1200g deionized waters, are added to After being ground in grinder, it is spray-dried, the powder that obtains is through 950 DEG C of calcination 12h after point spray drying, furnace cooling, The powder of acquisition is ground, and crosses 300 mesh sieve.
Comparative example 1:
Prepare Li1.20Mn0.54Ni0.13Co0.13O2, weigh 37.371g lithium carbonates, 50.797g manganese carbonates, 8.539g tetra- and aoxidize 800g deionized waters are added in three cobalts, 7.946g nickel protoxides, mixing, are added to after being ground in grinder, are spray-dried, The powder obtained after spray-dried is ground through 900 DEG C of calcination 36h, the powder of furnace cooling, acquisition, crosses 300 mesh sieve.
Comparative example 2:
Prepare Li1.19Mn0.53Ni0.15Co0.13P0.0005O2.01, weigh 51.113g lithium carbonates, 70.824g manganese carbonates, 12.131g cobaltosic oxides, 13.025g nickel protoxides and 0.403g ammonium sulfate, mixing are added 800g deionized waters, are added to After being ground in grinder, it is spray-dried, the powder that obtains is through 900 DEG C of calcination 36h after point spray drying, furnace cooling, The powder of acquisition is ground, and crosses 300 mesh sieve.
Comparative example 3:
Prepare Li1.132Mn0.490Ni0.123Co0.120P0.136Si0.005O2.289, weigh 46.446g lithium carbonates, 65.551g carbonic acid Manganese, 10.202g nickel protoxides, 10.696g cobaltosic oxides, 17.366g ammonium dihydrogen phosphates and 0.334g silica, mixing, 1000g deionized waters are added, is added to after being ground in grinder, is spray-dried, the powder obtained after point spray drying Through 900 DEG C of calcination 36h, the powder of furnace cooling, acquisition is ground, and crosses 300 mesh sieve.
Fig. 1 is the X-ray diffraction entirely &#91 entirely of material prepared by embodiment 1,2,3 and 4;Fig. 1 a&#93;(prepared by other specific embodiments Material XRD spectrum it is similar, omit) and 18~19.6 ° of the X-ray diffraction of material for preparing of embodiment 1,2,3 and 4 compose &#91;Figure 1b&#93;, it can be seen that from FIG. 1 a that the material prepared is stratiform α-NaFeO2Layer structure can be seen that the spy of material from Fig. 1 b It is slightly moved to low-angle at sign peak.
It is prepared by anode
The material prepared using embodiment 1,2,3,4 and comparative example 1~3 is as active material, with conductive agent (SP), bonding Agent (PVDF) is according to 8:1:1 proportioning weighs, and first by active material and the dry-mixed 4h of conductive agent, PVDF is dissolved in N-N dimethyl In formamide, then the conductive agent of the active material mixed is added thereto, is stirred evenly, forms anode sizing agent, it will be positive Slurry is coated on aluminium foil, is dried in drying box.
Testing of materials is prepared with half-cell
By the electrode cutting dried at 1 × 1cm, then roll-in is dried in vacuum drying chamber, as the anode of battery, The cathode of battery uses lithium metal, and the ingredient of electrolyte is mainly the LiPF of 1M6And DMC/EC/DEC (1:1:It 1), will be positive, negative Pole and electrolyte are placed in composition test battery in container.
The electrochemical property test of material
It is 20mA/g (0.1C), charging/discharging voltage 4.8~2V of range, test in current density by the test battery of composition The charge-discharge property of battery.The high rate performance of battery is tested under 0.1C, 0.2C, 0.5C, 1C, 2C, 3C multiplying power.
The positive electrode prepared using embodiment 1, embodiment 2, embodiment 3 and embodiment 4, the battery of assembling are filled for the first time The comparison diagram that discharges is as shown in Figure 2.From figure 2 it can be seen that the initial charge specific capacity of embodiment 1 is 346.8mAh/g, electric discharge Specific capacity is 259.9mAh/g, and the initial charge specific capacity of coulombic efficiency 74.9%, embodiment 2 is 328.2mAh/g, electric discharge Specific capacity is 263.9mAh/g, and the initial charge specific capacity of coulombic efficiency 80.2%, embodiment 3 is 353.9mAh/g, electric discharge Specific capacity is 277.1mAh/g, and the initial charge specific capacity of coulombic efficiency 78.3%, embodiment 4 is 369.7mAh/g, electric discharge Specific capacity is 283.6mAh/g, coulombic efficiency 76.7%.
Fig. 3 is the high rate performance comparison diagram of the lithium ion battery of positive electrode assembling prepared by embodiment 1,2,3 and 4, real The positive electrode of the preparation of example 1 is applied, lithium ion battery is assembled, battery is 259.9mAh/g in the specific discharge capacity of 0.1C, 0.2C's Specific discharge capacity is 235.5mAh/g, and the specific discharge capacity of 0.5C is 217.8mAh/g, and the specific discharge capacity of 1C is 197.2mAh/ The specific discharge capacity of g, 3C are 154.1mAh/g, and the specific discharge capacity for eventually passing back to 0.1C is 236.1mAh/g.It is prepared by embodiment 2 Positive electrode, assemble lithium ion battery, battery 0.1C specific discharge capacity be 263.9mAh/g, the specific discharge capacity of 0.2C Specific discharge capacity for 249.3mAh/g, 0.5C is 225.3mAh/g, and the specific discharge capacity of 1C is 196.2mAh/g, the electric discharge of 3C Specific capacity is 157.3mAh/g, and the specific discharge capacity for eventually passing back to 0.1C is 252.5mAh/g.Positive material prepared by embodiment 3 Material assembles lithium ion battery, and specific discharge capacity of the battery in 0.1C is 277.1mAh/g, and the specific discharge capacity of 0.2C is The specific discharge capacity of 253.5mAh/g, 0.5C are 232.8mAh/g, and the specific discharge capacity of 1C is 210.0mAh/g, the electric discharge ratio of 3C Capacity is 173.2mAh/g, and the specific discharge capacity for eventually passing back to 0.1C is 257.2mAh/g.Positive electrode prepared by embodiment 4, Lithium ion battery is assembled, battery is 283.6mAh/g in the specific discharge capacity of 0.1C, and the specific discharge capacity of 0.2C is 258.0mAh/ The specific discharge capacity of g, 0.5C are 235.4mAh/g, and the specific discharge capacity of 1C is 220.9mAh/g, and the specific discharge capacity of 3C is 185.5mAh/g, the specific discharge capacity for eventually passing back to 0.1C are 262.1mAh/g.
Fig. 4 is filling for the first time for the battery of positive electrode assembling prepared by embodiment 4 and comparative example 1, comparative example 2, comparative example 3 Discharge comparison diagram, from figure 5 it can be seen that the initial charge specific capacity of embodiment 4 is 369.7mAh/g, specific discharge capacity is 283.6mAh/g, coulombic efficiency 76.7%, and the initial charge specific capacity of comparative example 1 is 319.7mAh/g, specific discharge capacity Initial charge specific capacity for 248.8mAh/g, coulombic efficiency 77.8%, comparative example 2 is 335.7mAh/g, specific discharge capacity Initial charge specific capacity for 231.6mAh/g, coulombic efficiency 69.0%, comparative example 3 is 252.8mAh/g, specific discharge capacity For 195.2mAh/g, coulombic efficiency 77.2%.Comparative example 1 is to be added without phosphorus, and the phosphorus that comparative example 2 is added is relatively low, and comparative example 3 adds High phosphorus and too low silicon, the data excessively entered are shown:It is added without or is added inappropriate phosphorus and silicon or sulphur, the ratio of electric discharge for the first time of material Capacity can be all adversely affected.
Fig. 5 is the lithium ion battery of positive electrode assembling prepared by embodiment 4 and comparative example 1, comparative example 2, comparative example 3 The high rate performance of high rate performance comparison diagram, embodiment 4 is mentioned above, and positive electrode prepared by comparative example 1 assembles lithium-ion electric Pond, battery are 248.8mAh/g in the specific discharge capacity of 0.1C, and the specific discharge capacity of 0.2C is 220.4mAh/g, the electric discharge of 0.5C Specific capacity is 198.4mAh/g, and the specific discharge capacity of 1C is 179.9mAh/g, and the specific discharge capacity of 3C is 146.7mAh/g, finally The specific discharge capacity for returning to 0.1C is 230.5mAh/g.Positive electrode prepared by comparative example 2, assembles lithium ion battery, and battery exists The specific discharge capacity of 0.1C is 231.6mAh/g, and the specific discharge capacity of 0.2C is 193.4mAh/g, and the specific discharge capacity of 0.5C is The specific discharge capacity of 178.1mAh/g, 1C are 169.9mAh/g, and the specific discharge capacity of 3C is 124.7mAh/g, eventually passes back to 0.1C Specific discharge capacity be 202.1mAh/g.Positive electrode prepared by comparative example 3, assembles lithium ion battery, and battery is put 0.1C's Electric specific capacity is 195.2mAh/g, and the specific discharge capacity of 0.2C is 184.3mAh/g, and the specific discharge capacity of 0.5C is 163.8mAh/ The specific discharge capacity of g, 1C are 146.5mAh/g, and the specific discharge capacity of 3C is 123.1mAh/g, eventually passes back to the electric discharge ratio of 0.1C Capacity is 194.5mAh/g.Data show that the electric discharge of positive electrode prepared by embodiment 4 under high magnification is better than comparative example 1,2 With 3, silicon or sulphur are added in phosphorous rich lithium material, can not only improve the charge-discharge property of material, but also in high power Material also shows excellent chemical property under rate.In conjunction with above-mentioned data, method provided by the invention is not only in technique Cost is saved, and the performance of material has also reached the requirement of power battery, this method can be applied in industrial production.
Positive electrode prepared by embodiment 5~14 assembles lithium ion battery, is 4.8~2.0V in voltage range, different times Discharge performance tables of data under rate is as shown in the table.

Claims (36)

1. a kind of phosphorous anode material for lithium-ion batteries, chemical formula LiaMnbNicMdPeZfOg, wherein M be Co, Al, Ti, At least one of Fe, Cr, Cu, Zr, Mg, at least one of Z S, Si, and 0.95≤a<1.6,0≤b≤1,0≤c≤0.9,0 ≤ d≤0.5,0.006≤e≤0.020,0.01≤f≤0.15,1.95≤g<2.5.
2. a kind of phosphorous anode material for lithium-ion batteries according to claim 1, which is characterized in that 0<b≤0.9.
3. a kind of phosphorous anode material for lithium-ion batteries according to claim 1, which is characterized in that 0.05≤b≤ 0.9。
4. a kind of phosphorous anode material for lithium-ion batteries according to claim 1, which is characterized in that 0.1≤c≤0.9.
5. a kind of phosphorous anode material for lithium-ion batteries according to claim 1, which is characterized in that 0.02≤f≤ 0.05。
6. a kind of phosphorous anode material for lithium-ion batteries according to claim 1, which is characterized in that the positive material Material is one kind in consisting of:Li1.21Mn0.52Ni0.13Co0.12P0.02Si0.01O2.025、 Li1.21Mn0.53Ni0.13Co0.13P0.006Si0.02O2.14、、LiMn0.28Ni0.58Co0.18Al0.03Zr0.03P0.02S0.08O2.305、 Li1.04Mn0.16Ni0.76Fe0.16Al0.05Mg0.03P0.006S0.05O2.11、Li1.5Mn0.453Ni0.28Cr0.15P0.007S0.01O2.209、 Li1.2Mn0.54Ni0.13Cr0.05Al0.03Mg0.03P0.02S0.03O2.1、、LiMn0.35Ni0.582Mg0.20P0.008S0.01O2.032、 Li1.2Mn0.6Ni0.15Cu0.05P0.02Si0.01O2.07、Li1.35Mn0.52Ni0.15Cu0.08Cr0.03P0.006Si0.01O2.025、 Li1.25Mn0.62Ni0.06Co0.04P0.015Si0.1O2.223
7. a kind of method preparing phosphorous anode material for lithium-ion batteries described in claim 1, which is characterized in that at least contain There are following 4 steps:
1) with lithium source, phosphorus source, manganese source and nickel source, and in cobalt source, silicon source, titanium source, source of iron, chromium source, copper source, zirconium source and magnesium source At least one, and it is used as raw material selected from least one of sulphur source and silicon source, weigh corresponding original by the molar ratio of the chemical formula Material;
2) liquid is added in the feed, carries out wet-milling, is not more than 50 weight % i.e. 0 weight %&lt by solid content;The weight of solid content≤50 % is measured, surplus is liquid, and liquid is water, ethyl alcohol or aqueous organopolysiloxane, wherein the concentration of aqueous organopolysiloxane is no more than 50 weights Measure % i.e. 0 weight %<The weight % of the concentration of aqueous organopolysiloxane≤50, remaining is water;
3) the good slurry of wet-milling is dried;
4) material after drying is roasted, calcination temperature is 750~1100 DEG C, and roasting time is 5~60h.
8. the preparation method of positive electrode according to claim 7, which is characterized in that the lithium source is anhydrous hydroxide At least one of lithium, the water lithium hydroxide containing crystallization, lithium carbonate.
9. the preparation method of positive electrode according to claim 7, which is characterized in that the phosphorus source is phosphate or phosphorus Oxide.
10. the preparation method of positive electrode according to claim 9, which is characterized in that the phosphorus source is phosphate.
11. the preparation method of positive electrode according to claim 10, which is characterized in that the phosphorus source is phosphoric acid hydrogen two At least one of ammonia, ammonium di-hydrogen phosphate, phosphoric acid ammonia.
12. the preparation method of positive electrode according to claim 10, which is characterized in that the phosphorus source is phosphoric acid hydrogen two Ammonia.
13. the preparation method of positive electrode according to claim 10, which is characterized in that the phosphorus source is biphosphate Ammonia.
14. the preparation method of positive electrode according to claim 7, which is characterized in that the manganese source is manganese metal, one At least one of manganese oxide, manganese dioxide, manganese carbonate.
15. the preparation method of positive electrode according to claim 7, which is characterized in that the nickel source is metallic nickel, oxygen Change at least one of sub- nickel, nickel sesquioxide, nickel hydroxide, nickelous carbonate.
16. the preparation method of positive electrode according to claim 7, which is characterized in that the cobalt source is metallic cobalt, four At least one of Co 3 O, cobalt sesquioxide, cobalt protoxide, cobalt hydroxide, cobalt carbonate.
17. the preparation method of positive electrode according to claim 7, which is characterized in that the silicon source is metallic aluminium, three At least one of Al 2 O, aluminium hydroxide.
18. the preparation method of positive electrode according to claim 7, which is characterized in that the titanium source be titanium dioxide, At least one of titanium isopropoxide.
19. the preparation method of positive electrode according to claim 7, which is characterized in that the source of iron is metallic iron, three Aoxidize at least one of two iron, ferroso-ferric oxide, iron hydroxide, ferrous hydroxide.
20. the preparation method of positive electrode according to claim 7, which is characterized in that the chromium source is crome metal, three Aoxidize at least one of two chromium, chromium hydroxide.
21. the preparation method of positive electrode according to claim 7, which is characterized in that the copper source is copper oxide, oxygen Change at least one of cuprous, copper carbonate.
22. the preparation method of positive electrode according to claim 7, which is characterized in that the zirconium source is zirconium oxide, hydrogen At least one of zirconium oxide.
23. the preparation method of positive electrode according to claim 7, which is characterized in that the magnesium source is magnesium carbonate, oxygen Change at least one of magnesium.
24. the preparation method of positive electrode according to claim 7, which is characterized in that manganese source, nickel source and the cobalt source It is aoxidized in manganese nickel cobalt, oxalic acid manganese nickel cobalt, carbonic acid manganese nickel cobalt, oxidation manganese nickel cobalt extremely for manganese nickel cobalt alloy, manganous hydroxide nickel cobalt, hydroxyl Few one kind.
25. the preparation method of positive electrode according to claim 7, which is characterized in that the manganese source and nickel source is manganese At least one of nickel alloy, manganous hydroxide nickel, hydroxyl manganese oxide nickel, manganese oxalate nickel, manganese carbonate nickel, manganese oxide nickel.
26. the preparation method of positive electrode according to claim 7, which is characterized in that the manganese source and cobalt source is manganese At least one of cobalt alloy, manganous hydroxide cobalt, hydroxyl manganese oxide cobalt, manganese oxalate cobalt, manganese carbonate cobalt, manganese oxide cobalt.
27. the preparation method of positive electrode according to claim 7, which is characterized in that the nickel source and cobalt source is nickel At least one of cobalt alloy, hydroxide nickel cobalt, hydroxy cobalt nickel oxide, oxalic acid nickel cobalt, carbonic acid nickel cobalt, cobalt nickel oxide.
28. the preparation method of positive electrode according to claim 7, which is characterized in that the sulphur source is sulfate, Asia The hydride of sulfate, sulfur oxide or sulphur.
29. the preparation method of positive electrode according to claim 28, which is characterized in that the sulphur source is sulfate.
30. the preparation method of positive electrode according to claim 28, which is characterized in that the sulphur source be nickel sulfate or At least one of ammonium sulfate.
31. the preparation method of positive electrode according to claim 7, which is characterized in that the silicon source is silica.
32. the preparation method of positive electrode according to claim 7, which is characterized in that the water is deionized water;Institute The aqueous organopolysiloxane stated is at least one of aqueous solution, PVA aqueous solutions, aqueous sucrose solution of ethyl alcohol.
33. the preparation method of positive electrode according to claim 7, which is characterized in that the drying be vacuum drying, At least one of forced air drying, spray drying, microwave drying.
34. the preparation method of positive electrode according to claim 7, which is characterized in that the temperature of roasting is 800~1000 ℃。
35. a kind of anode of lithium ion battery, which is characterized in that with described in any one of claim 1-6 positive electrode or The positive electrode prepared according to any one of claim 7-34 the methods is mixed with conductive carbon and bonding agent, and will To mixture coated in the anode for forming the lithium ion battery on support conducting base.
36. a kind of lithium ion battery, which is characterized in that by the anode compatible with electricity of the anode described in claim 35, diaphragm, electricity Solution matter, which is placed in container, forms lithium ion battery.
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