CN104393282A - Preparation method of multi-element cathode material coated by graphene - Google Patents

Preparation method of multi-element cathode material coated by graphene Download PDF

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Publication number
CN104393282A
CN104393282A CN201410793069.4A CN201410793069A CN104393282A CN 104393282 A CN104393282 A CN 104393282A CN 201410793069 A CN201410793069 A CN 201410793069A CN 104393282 A CN104393282 A CN 104393282A
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graphene
active material
cobalt
derivative
nickel
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宫香娥
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Xia Linmei
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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
    • 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
    • H01M4/1391Processes of manufacture of electrodes 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
    • H01M4/52Selection 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
    • H01M4/62Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M2004/026Electrodes composed of, or comprising, active material characterised by the polarity
    • H01M2004/028Positive 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

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

Abstract

The invention relates to a preparation method of multi-element cathode material coated by graphene. The active material of the multi-element cathode material comprises an inner layer and an outer layer, wherein the active material has the following chemical formula (1-a) LiNi1-xCoxO2.aLiMn0.3Al0.7O2, wherein a is equal to 0.3-0.35, and the x is equal to 0.25-0.45. The method comprises the following steps: (1) preparing the active material; (2) preparing graphene derivate materials; (3) coating the active material by the graphene derivate materials. The multi-element cathode material prepared by the method disclosed by the invention adopts a two-layer structures with various component matching ratios, the proportion of the nickel in the inner layer is the highest, so that the high capacity of the material is ensured; the outer layer has higher cobalt content, so that the cycling stability of the material is ensured; finally, another layer of graphene derivate material is adopted for coating the active material, so that the activity and the capacity of the material are further improved. Therefore, when the cathode materials are applied to lithium batteries, the specific capacity is higher, and the stability is good.

Description

A kind of preparation method of polynary positive pole material of graphene coated
Technical field
The present invention relates to a kind of preparation method of polynary positive pole material of graphene coated.
Background technology
Along with the development of various new forms of energy, various electronic equipment, as portable electric appts and electric automobile etc., more extensive to the demand of large-capacity high-power chemical power source.
Business-like positive electrode mainly contains cobalt acid lithium (LiCoO at present 2), lithium nickelate (LiNiO 2), LiMn2O4 (LiMnO 2) and nickel-cobalt-manganese ternary material.Stratiform lithium cobaltate cathode material is business-like lithium ion battery the earliest, although its energy density is high, its cost is high, and environmental pollution is also larger; Spinel lithium manganese oxide anode material cost is low, and fail safe is high, but its specific capacity is low and high-temperature behavior is poor; Stratiform lithium nickelate positive electrode capacity is high, but synthesis condition is harsh; Olivine lithium iron phosphate cathode material is moderate, and cycle performance is very good, but cryogenic property is bad, and volumetric specific energy is lower.Make a general survey of several positive electrodes main at present, the advantage that polynary positive pole material display is unique, assemble the advantage of cobalt acid lithium, LiMn2O4 and lithium nickelate three kinds of positive electrodes, i.e. high-energy, high power capacity, high securities etc., charge and discharge platform and cobalt acid lithium is close, is considered to most possible substituting cobalt acid lithium and one of business-like positive electrode.But the cycle performance of this material is general, have impact on the commercial applications of this material.
Summary of the invention
The invention provides a kind of preparation method of polynary positive pole material of graphene coated, the positive electrode using the method to prepare, has higher energy density and good cyclical stability.
To achieve these goals, the invention provides a kind of preparation method of polynary positive pole material of graphene coated, the active material of this polynary positive pole material comprises internal layer and skin, and wherein this active material possesses following chemical formula (1-a) LiNi 1-xco xo 2. aLiMn 0.3al 0.7o 2, wherein a=0.3-0.35, x=0.25-0.45, the method comprises the steps:
(1) active material is prepared
Compound concentration is the acetic acid solution of 1-1.5mol/L, nickelous sulfate, cobaltous sulfate are configured to according to being dissolved in deionized water after mol ratio 1-x:x mixing the mixed nitrate solution that metal ion total concentration is 3-4mol/L, above-mentioned acetic acid solution is placed in the reactor that band stirs, strong agitation, mixing salt solution is instilled in reactor, in regulating and controlling reactor reactant liquor temperature and remain on 55-60 DEG C, after having fed in raw material, continue to stir ageing, wherein the amount of acetic acid solution should enough make all nickel and cobalt ions generate nickel acetate cobalt;
Separation of Solid and Liquid, spends the solid product of deionized water Separation of Solid and Liquid gained, and the product after washing is dry, obtains nickel acetate cobalt powder body, by nickel acetate cobalt powder body air atmosphere 500-550 DEG C calcining 4-6h, and obtained internal layer precursor, pulverize after cooling, for subsequent use;
The sal limonis of cobalt manganese aluminium is dissolved in deionized water, wherein the mol ratio of manganese aluminium element is 3:7, obtain the citrate solution that metal ion total concentration is 0.5-1mol/L, the precursor powder having an internal layer by above-mentioned and dispersant acetone are put into the citrate solution prepared in the lump and are mixed, the mol ratio of the manganese aluminium element total amount in the precursor powder of wherein internal layer in nickel cobalt element total amount and citrate solution is 1-a:a, stir and form suspension, then will obtain active material presoma after spray dried;
By after active material presoma and lithium carbonate mixing with the speed ball milling 4-5h of 300-350r/min, the mol ratio 1:1 of the lithium in the integral molar quantity of the nickel cobalt manganese aluminium wherein in precursor and lithium carbonate, then calcines 8-10h, obtains active material at 850-900 DEG C;
(2) Graphene derivative material is prepared
By graphite oxide dissolve in deionized water, then under agitation add the ethanolic solution of aminopyrimidine, then at the temperature of 70-75 DEG C back flow reaction 30-40h, obtain the aminopyridine derivative of graphene oxide;
The back flow reaction 10-15h at the temperature of 85-90 DEG C by described aminopyridine derivative and enough hydrazine hydrates, obtain the aminopyridine derivative of Graphene, by the aminopyridine derivative of described Graphene at 100-120 DEG C of annealing 5-8h, obtain Graphene derivative material;
(3) the coated active material of Graphene derivative
Above-mentioned active material and the above-mentioned Graphene derivative material ratio by weight 100: 3-4 is mixed, by compound in planetary ball mill with rotating speed 400-450r/min ball milling 3-5h, after the material drying after ball milling, sintering is heat-treated in High Purity Nitrogen air-flow, with 5-10 DEG C/min ramp, at temperature 750-800 DEG C of Isothermal sinter 10-15h, lower the temperature with 10-15 DEG C/min, obtain final products.
Polynary positive pole material prepared by the present invention, there is the two-layer Rotating fields that component proportion is different, wherein internal layer nickel proportion is the highest, to ensure the high power capacity of material, skin has higher cobalt content, to ensure the cyclical stability of material, finally cover activity and capacity that one deck Graphene derivative material improves material further again.Therefore this positive electrode is when for lithium ion battery, has higher specific capacity and good stability.
Embodiment
embodiment one
This active material of this embodiment possesses following chemical formula 0.7LiNi 0.75co 0.25o 2. 0.3LiMn 0.3al 0.7o 2.
Compound concentration is the acetic acid solution of 1mol/L, nickelous sulfate, cobaltous sulfate are configured to according to being dissolved in deionized water after mol ratio 0.75:0.25 mixing the mixed nitrate solution that metal ion total concentration is 3mol/L, above-mentioned acetic acid solution is placed in the reactor that band stirs, strong agitation, mixing salt solution is instilled in reactor, in regulating and controlling reactor reactant liquor temperature and remain on 55 DEG C, after having fed in raw material, continue to stir ageing, wherein the amount of acetic acid solution should enough make all nickel and cobalt ions generate nickel acetate cobalt; Separation of Solid and Liquid, spends the solid product of deionized water Separation of Solid and Liquid gained, and the product after washing is dry, obtains nickel acetate cobalt powder body, by nickel acetate cobalt powder body air atmosphere 500 DEG C calcining 6h, and obtained internal layer precursor, pulverize after cooling, for subsequent use.
The sal limonis of cobalt manganese aluminium is dissolved in deionized water, wherein the mol ratio of manganese aluminium element is 3:7, obtain the citrate solution that metal ion total concentration is 0.5mol/L, the precursor powder having an internal layer by above-mentioned and dispersant acetone are put into the citrate solution prepared in the lump and are mixed, the mol ratio of the manganese aluminium element total amount in the precursor powder of wherein internal layer in nickel cobalt element total amount and citrate solution is 0.7:0.3, stir and form suspension, then will obtain active material presoma after spray dried; By after active material presoma and lithium carbonate mixing with the speed ball milling 5h of 300r/min, the mol ratio 1:1 of the lithium in the integral molar quantity of the nickel cobalt manganese aluminium wherein in precursor and lithium carbonate, then calcines 10h, obtains active material at 850 DEG C.
Graphite oxide is dissolved in deionized water, then the ethanolic solution of aminopyrimidine is under agitation added, back flow reaction 40h at the temperature of 70 DEG C again, obtain the aminopyridine derivative of graphene oxide, the back flow reaction 15h at the temperature of 85 DEG C by described aminopyridine derivative and enough hydrazine hydrates, obtain the aminopyridine derivative of Graphene, by the aminopyridine derivative of described Graphene at 100 DEG C of annealing 8h, obtain Graphene derivative material.
Above-mentioned active material and the above-mentioned Graphene derivative material ratio by weight 100: 3 is mixed, by compound in planetary ball mill with rotating speed 400r/min ball milling 5h, after the material drying after ball milling, sintering is heat-treated in High Purity Nitrogen air-flow, with 5 DEG C/min ramp, at temperature 750 DEG C of Isothermal sinter 15h, lower the temperature with 10 DEG C/min, obtain final products.
embodiment two
This active material of this embodiment possesses following chemical formula 0.65LiNi 0.55co 0.45o 2. 0.35LiMn 0.3al 0.7o 2.
Compound concentration is the acetic acid solution of 1.5mol/L, nickelous sulfate, cobaltous sulfate are configured to according to being dissolved in deionized water after mol ratio 0.55:0.45 mixing the mixed nitrate solution that metal ion total concentration is 4mol/L, above-mentioned acetic acid solution is placed in the reactor that band stirs, strong agitation, mixing salt solution is instilled in reactor, in regulating and controlling reactor reactant liquor temperature and remain on 60 DEG C, after having fed in raw material, continue to stir ageing, wherein the amount of acetic acid solution should enough make all nickel and cobalt ions generate nickel acetate cobalt; Separation of Solid and Liquid, spends the solid product of deionized water Separation of Solid and Liquid gained, and the product after washing is dry, obtains nickel acetate cobalt powder body, by nickel acetate cobalt powder body air atmosphere 550 DEG C calcining 4h, and obtained internal layer precursor, pulverize after cooling, for subsequent use.
The sal limonis of cobalt manganese aluminium is dissolved in deionized water, wherein the mol ratio of manganese aluminium element is 3:7, obtain the citrate solution that metal ion total concentration is 1mol/L, the precursor powder having an internal layer by above-mentioned and dispersant acetone are put into the citrate solution prepared in the lump and are mixed, the mol ratio of the manganese aluminium element total amount in the precursor powder of wherein internal layer in nickel cobalt element total amount and citrate solution is 0.65:0.35, stir and form suspension, then will obtain active material presoma after spray dried; By after active material presoma and lithium carbonate mixing with the speed ball milling 4h of 350r/min, the mol ratio 1:1 of the lithium in the integral molar quantity of the nickel cobalt manganese aluminium wherein in precursor and lithium carbonate, then calcines 8h, obtains active material at 900 DEG C.
Graphite oxide is dissolved in deionized water, then the ethanolic solution of aminopyrimidine is under agitation added, back flow reaction 30h at the temperature of 75 DEG C again, obtain the aminopyridine derivative of graphene oxide, the back flow reaction 10h at the temperature of 90 DEG C by described aminopyridine derivative and enough hydrazine hydrates, obtain the aminopyridine derivative of Graphene, by the aminopyridine derivative of described Graphene at 120 DEG C of annealing 5h, obtain Graphene derivative material.
Above-mentioned active material and the above-mentioned Graphene derivative material ratio by weight 100: 4 is mixed, by compound in planetary ball mill with rotating speed 450r/min ball milling 3h, after the material drying after ball milling, sintering is heat-treated in High Purity Nitrogen air-flow, with 10 DEG C/min ramp, at temperature 800 DEG C of Isothermal sinter 10h, lower the temperature with 15 DEG C/min, obtain final products.
comparative example
Compound concentration is the nickel of 2M, cobalt and manganese salt solution, wherein, and nickel: cobalt: the molar ratio of manganese is 1: 1: 1.The above-mentioned salting liquid prepared is injected with the speed of 1L/h the reactor that rotating speed is 200rps, injects the NaOH solution of 6M simultaneously, note regulating aqueous slkali flow velocity, keep pH value between 10-11.After 27.5h, salting liquid is squeezed in reactor completely, and precursor power has reacted.By the solidliquid mixture after having reacted by centrifugation, wash and at 100 DEG C, dry 10h to neutrality.By presoma and the lithium carbonate after drying in molar ratio 1: 1.05 mix after in Muffle furnace 900 DEG C of roasting 10h, the material after roasting obtains homogeneous LiNi after fragmentation is sieved 1/3co 1/3mn 1/3o 2ternary material.
Take above-described embodiment one, two and the comparative example products therefrom of equal in quality, be assembled into the simulated battery of same dimensions respectively, negative pole is metal lithium sheet, and barrier film is celgard2400, and electrolyte is LiPF 6(EC:DEC:=1:1 :).At probe temperature is 45 DEG C, carry out electric performance test, after tested this embodiment one with two material compared with the product of comparative example, discharge capacity improves 25.5-31.7 mAh/g first, 100 times circulation after capability retention improve more than 10-15%.

Claims (1)

1. a preparation method for the polynary positive pole material of graphene coated, the active material of this polynary positive pole material comprises internal layer and skin, and wherein this active material possesses following chemical formula (1-a) LiNi 1-xco xo 2. aLiMn 0.3al 0.7o 2, wherein a=0.3-0.35, x=0.25-0.45, the method comprises the steps:
(1) active material is prepared
Compound concentration is the acetic acid solution of 1-1.5mol/L, nickelous sulfate, cobaltous sulfate are configured to according to being dissolved in deionized water after mol ratio 1-x:x mixing the mixed nitrate solution that metal ion total concentration is 3-4mol/L, above-mentioned acetic acid solution is placed in the reactor that band stirs, strong agitation, mixing salt solution is instilled in reactor, in regulating and controlling reactor reactant liquor temperature and remain on 55-60 DEG C, after having fed in raw material, continue to stir ageing, wherein the amount of acetic acid solution should enough make all nickel and cobalt ions generate nickel acetate cobalt;
Separation of Solid and Liquid, spends the solid product of deionized water Separation of Solid and Liquid gained, and the product after washing is dry, obtains nickel acetate cobalt powder body, by nickel acetate cobalt powder body air atmosphere 500-550 DEG C calcining 4-6h, and obtained internal layer precursor, pulverize after cooling, for subsequent use;
The sal limonis of cobalt manganese aluminium is dissolved in deionized water, wherein the mol ratio of manganese aluminium element is 3:7, obtain the citrate solution that metal ion total concentration is 0.5-1mol/L, the precursor powder having an internal layer by above-mentioned and dispersant acetone are put into the citrate solution prepared in the lump and are mixed, the mol ratio of the manganese aluminium element total amount in the precursor powder of wherein internal layer in nickel cobalt element total amount and citrate solution is 1-a:a, stir and form suspension, then will obtain active material presoma after spray dried;
By after active material presoma and lithium carbonate mixing with the speed ball milling 4-5h of 300-350r/min, the mol ratio 1:1 of the lithium in the integral molar quantity of the nickel cobalt manganese aluminium wherein in precursor and lithium carbonate, then calcines 8-10h, obtains active material at 850-900 DEG C;
(2) Graphene derivative material is prepared
By graphite oxide dissolve in deionized water, then under agitation add the ethanolic solution of aminopyrimidine, then at the temperature of 70-75 DEG C back flow reaction 30-40h, obtain the aminopyridine derivative of graphene oxide;
The back flow reaction 10-15h at the temperature of 85-90 DEG C by described aminopyridine derivative and enough hydrazine hydrates, obtain the aminopyridine derivative of Graphene, by the aminopyridine derivative of described Graphene at 100-120 DEG C of annealing 5-8h, obtain Graphene derivative material;
(3) the coated active material of Graphene derivative
Above-mentioned active material and the above-mentioned Graphene derivative material ratio by weight 100: 3-4 is mixed, by compound in planetary ball mill with rotating speed 400-450r/min ball milling 3-5h, after the material drying after ball milling, sintering is heat-treated in High Purity Nitrogen air-flow, with 5-10 DEG C/min ramp, at temperature 750-800 DEG C of Isothermal sinter 10-15h, lower the temperature with 10-15 DEG C/min, obtain final products.
CN201410793069.4A 2014-12-20 2014-12-20 Preparation method of multi-element cathode material coated by graphene Pending CN104393282A (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106784654A (en) * 2016-11-28 2017-05-31 荆门市格林美新材料有限公司 A kind of preparation method of graphene coated cobalt acid lithium material
CN108539131A (en) * 2018-03-27 2018-09-14 宁夏汉尧石墨烯储能材料科技有限公司 A kind of graphene is modified the preparation method of nickelic system's positive electrode
CN111492526A (en) * 2018-11-29 2020-08-04 株式会社Lg化学 Electrode assembly
CN113716549A (en) * 2020-12-16 2021-11-30 山东海科创新研究院有限公司 Multi-element coated core-shell structure lithium ion positive electrode material and preparation method thereof

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106784654A (en) * 2016-11-28 2017-05-31 荆门市格林美新材料有限公司 A kind of preparation method of graphene coated cobalt acid lithium material
CN108539131A (en) * 2018-03-27 2018-09-14 宁夏汉尧石墨烯储能材料科技有限公司 A kind of graphene is modified the preparation method of nickelic system's positive electrode
CN111492526A (en) * 2018-11-29 2020-08-04 株式会社Lg化学 Electrode assembly
CN111492526B (en) * 2018-11-29 2023-07-25 株式会社Lg新能源 Electrode assembly, secondary battery, and secondary battery module
US11909040B2 (en) 2018-11-29 2024-02-20 Lg Energy Solution, Ltd. Electrode assembly
CN113716549A (en) * 2020-12-16 2021-11-30 山东海科创新研究院有限公司 Multi-element coated core-shell structure lithium ion positive electrode material and preparation method thereof

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