CN111293365B - Preparation method of lithium manganate battery - Google Patents

Preparation method of lithium manganate battery Download PDF

Info

Publication number
CN111293365B
CN111293365B CN202010107700.6A CN202010107700A CN111293365B CN 111293365 B CN111293365 B CN 111293365B CN 202010107700 A CN202010107700 A CN 202010107700A CN 111293365 B CN111293365 B CN 111293365B
Authority
CN
China
Prior art keywords
slurry
life
voltage
negative electrode
electrolyte
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN202010107700.6A
Other languages
Chinese (zh)
Other versions
CN111293365A (en
Inventor
陆晨杰
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Zhejiang Gepai cobalt industry new material Co.,Ltd.
Original Assignee
Greatpower Jinchuan Advanced Battery Materials Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Greatpower Jinchuan Advanced Battery Materials Corp filed Critical Greatpower Jinchuan Advanced Battery Materials Corp
Priority to CN202010107700.6A priority Critical patent/CN111293365B/en
Publication of CN111293365A publication Critical patent/CN111293365A/en
Application granted granted Critical
Publication of CN111293365B publication Critical patent/CN111293365B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • 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
    • H01M10/058Construction or manufacture
    • 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
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/056Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes
    • H01M10/0564Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes the electrolyte being constituted of organic materials only
    • H01M10/0566Liquid materials
    • H01M10/0567Liquid materials characterised by the additives
    • 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
    • H01M4/04Processes of manufacture in general
    • H01M4/0402Methods of deposition of the material
    • H01M4/0404Methods of deposition of the material by coating on electrode collectors
    • 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
    • H01M4/13Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • H01M4/136Electrodes based on inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFy
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/13Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • H01M4/139Processes of manufacture
    • H01M4/1391Processes 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
    • H01M4/13Electrodes 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
    • H01M4/362Composites
    • H01M4/364Composites as mixtures
    • 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
    • H01M4/50Selection 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
    • H01M4/36Selection 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
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M2300/00Electrolytes
    • H01M2300/0017Non-aqueous electrolytes
    • H01M2300/0025Organic electrolyte
    • 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
    • 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50Manufacturing or production processes characterised by the final manufactured product

Landscapes

  • 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)
  • Composite Materials (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • Condensed Matter Physics & Semiconductors (AREA)
  • General Physics & Mathematics (AREA)
  • Battery Electrode And Active Subsutance (AREA)
  • Secondary Cells (AREA)

Abstract

The invention provides a preparation method of a lithium manganate battery, wherein an active substance in a positive electrode of the lithium manganate battery is LiMn0.83Co0.15Al0.02O2And LiFe0.9Mn0.1PO4The electrolyte of the lithium manganate battery contains an additive, the additive consists of 1-propylene-1, 3-sultone (PST) and 1-propylene-1, 3-sultone (MMDS), and the volume ratio of PST: MMDS =1: 1.35-1.40; and the additive accounts for 3-5% of the volume of the electrolyte; the preparation method comprises the step of adding LiMn0.83Co0.15Al0.02O2And LiFe0.9Mn0.1PO4Mixing the materials according to a preset proportion, preparing a first slurry, and mixing the LiFe0.9Mn0.1PO4Preparing a second slurry, coating and drying the first slurry and the second slurry on a current collector in sequence to obtain a positive electrode, preparing natural graphite into a negative electrode slurry, coating the negative electrode slurry on the current collector and drying to obtain a negative electrode, laminating the positive electrode into a battery cell, placing the battery cell in a shell, injecting electrolyte,the lithium manganate battery prepared by the method has good high-temperature storage and high-temperature cycle characteristics.

Description

Preparation method of lithium manganate battery
Technical Field
The invention relates to a preparation method of a lithium manganate battery.
Background
The lithium manganate has the advantages of high safety, low cost, environmental protection and the like, is one of common materials of the lithium ion battery, but the lithium manganate battery has poor cycle performance due to the volume effect, and particularly has serious influence on the application range of the lithium manganate battery due to the dissolution of manganese and the generation of gas caused by the decomposition of electrolyte on the surface of an electrode in a high-temperature environment.
Disclosure of Invention
The invention provides a preparation method of a lithium manganate battery, wherein an active substance in a positive electrode of the lithium manganate battery is LiMn0.83Co0.15Al0.02O2And LiFe0.9Mn0.1PO4The electrolyte of the lithium manganate battery contains an additive, the additive consists of 1-propylene-1, 3-sultone (PST) and 1-propylene-1, 3-sultone (MMDS), and the volume ratio of PST: MMDS ═ 1: 1.35-1.40; and the additive accounts for 3-5% of the volume of the electrolyte; the preparation method comprises the step of adding LiMn0.83Co0.15Al0.02O2And LiFe0.9Mn0.1PO4Mixing the materials according to a preset proportion, preparing a first slurry, and mixing the LiFe0.9Mn0.1PO4Preparing a second slurry, sequentially coating and drying the first slurry and the second slurry on a current collector to obtain a positive electrode, then placing natural graphite into a negative electrode slurry, coating the negative electrode slurry on the current collector and drying to obtain a negative electrode, laminating the positive electrode, a diaphragm and the negative electrode into a battery core, placing the battery core into a shell, injecting electrolyte, and carrying out formation within a preset voltage range to obtain the lithium manganate battery.
The specific scheme is as follows:
a process for preparing the lithium manganate battery whose positive electrode contains LiMn as active component0.83Co0.15Al0.02O2And LiFe0.9Mn0.1PO4The electrolyte of the lithium manganate battery contains an additive accounting for 3-5 vol% of the electrolyte, and the additive consists of 1-propylene-1, 3-sultone (PST) and 1-propylene-1, 3-sultone (MMDS), wherein the volume ratio of PST: MMDS ═ 1: 1.35-1.40; the preparation method comprises the step of adding LiMn0.83Co0.15Al0.02O2And LiFe0.9Mn0.1PO4Mixing the materials in a predetermined ratio to prepare a first slurry, and mixing the first slurry with LiFe0.9Mn0.1PO4Preparing a second slurry, sequentially coating and drying the first slurry and the second slurry on a current collector to obtain a positive electrode, preparing natural graphite into a negative electrode slurry, coating the negative electrode slurry on the current collector and drying to obtain a negative electrode, laminating the positive electrode, a diaphragm and the negative electrode into a battery core, placing the battery core in a shell, injecting electrolyte, and performing formation within a preset voltage range to obtain the lithium manganate battery.
Further, the preparation method comprises the following steps:
1) mixing LiMn0.83Co0.15Al0.02O2And LiFe0.9Mn0.1PO4Ball milling and mixing the LiMn and the LiMn in a ratio of 8:2-9:10.83Co0.15Al0.02O2The average grain diameter is 1.8-2.0 mu m, and the LiFe0.9Mn0.1PO4The average grain diameter is 1.2-1.4 μm;
2) adding a solvent into a stirring kettle, then adding a binder and a conductive agent, uniformly stirring, then adding the mixed active material obtained in the step (1), and uniformly stirring to obtain a first slurry, wherein the active material is prepared from the following components in percentage by mass: adhesive: the conductive agent is 100:3-5: 3-5;
3) adding a solvent into a stirring kettle, then adding a dispersing agent, a binder and a conductive agent, uniformly stirring, and then adding LiFe0.9Mn0.1PO4(ii) a The LiFe0.9Mn0.1PO4The average particle size is 0.8-1 mu m, and the second slurry is obtained by uniformly stirring, wherein the mass ratio of the LiFe to the first slurry is0.9Mn0.1PO4: dispersing agent: adhesive: the conductive agent is 100:3-5:3-5: 6-10;
4) coating and drying the first slurry and the second slurry on the aluminum foil to obtain the anode;
5) adding a solvent into a stirring kettle, then adding a binder and a conductive agent, uniformly stirring, and adding natural graphite to obtain negative electrode slurry;
6) coating and drying the negative electrode slurry on the copper foil to obtain the negative electrode;
7) laminating the positive electrode, the diaphragm and the negative electrode into a battery cell, placing the battery cell in a shell, and injecting electrolyte;
8) and forming to obtain the lithium manganate battery.
Further, the formation comprises the following steps:
1) charging to a first preset voltage by constant current, wherein the first preset voltage is 3.2-3.3V;
2) performing constant-current charge-discharge circulation for a plurality of times between a first preset voltage and a second preset voltage, wherein the second preset voltage is 3.4-3.5V;
3) charging at constant current to a charging cut-off voltage, and then charging at constant voltage by using the charging cut-off voltage until the charging current is less than a preset value;
4) constant current charge and discharge cycles are performed between the charge cutoff voltage and the discharge cutoff voltage for several times.
Further, the coating thickness ratio of the first slurry to the second slurry is 6:4-9: 1.
Further, the negative active material is a graphite material.
Further, the charge cut-off voltage is 4.25V, and the discharge cut-off voltage is 2.75V.
Further, the organic solvent of the electrolyte is selected from cyclic carbonate, chain carbonate, functional group-substituted cyclic carbonate or functional group-substituted chain carbonate.
The invention has the following beneficial effects:
1) the inventors found that LiMn0.83Co0.15Al0.02O2The material has good rate performance and high-temperature stability, and LiFe0.9Mn0.1PO4The material has good high-temperature electrolyte stability, and the LiFe is prepared by mixing LiFe and water0.9Mn0.1PO4The material is arranged on the surface of the active layer, so that the high-temperature stability of the anode can be improved, the working voltages of the two materials are relatively close, and the phenomena of voltage polarization and the like can not be generated even if the two materials are mixed for use.
2) The researchers found that by selecting the specific particle size range of the particle size of the active material of the first layer and the surface layer, the first layer can be formed after mixing the two active materials, and the volume expansion rate of the first layer is close to that of the surface layer material, so that the stability of the material layer can be improved, and the active material can be prevented from being separated due to interlayer stress.
3) For LiFe0.9Mn0.1PO4The inventor finds that the addition of 1-propene-1, 3-sultone (PST) and 1-propene-1, 3-sultone (MMDS) in the electrolysis can effectively improve the capacity performance of the battery in a high-temperature environment.
4) Particularly, after the two additives are added in a specific ratio, the capacity performance is obviously improved.
5) According to the specific active material and electrolyte components of the invention, researchers set a specific voltage interval to perform charge-discharge cycle, which is more beneficial to forming a stable SEI film and prolonging the cycle life.
Detailed Description
The present invention will be described in more detail below with reference to specific examples, but the scope of the present invention is not limited to these examples.
The active material of the positive electrode is LiMn0.83Co0.15Al0.02O2Materials and LiFe0.9Mn0.1PO4The material comprises a positive electrode binder and a negative electrode slurry, wherein the positive electrode binder is polyvinylidene fluoride, a dispersing agent is sodium carboxymethylcellulose, a solvent of the positive electrode slurry is NMP, a solvent of the negative electrode slurry is deionized water, and a binder of the negative electrode slurry is SBR; the electrolyte comprises 1M lithium hexafluorophosphate, and the organic solvent is DMC + EC + PC in a ratio of 1:1: 1; the active material of the negative electrode is a natural graphite negative electrode; the positive and negative electrode active material layers were each 60 μm thick on one side.
Example 1
1) Mixing LiMn0.83Co0.15Al0.02O2And LiFe0.9Mn0.1PO4Ball milling and mixing the LiMn and the LiMn in a mass ratio of 8:20.83Co0.15Al0.02O2The average particle diameter is 1.8 mu m, and the LiFe0.9Mn0.1PO4The average particle diameter is 1.2 mu m;
2) adding NMP into a stirring kettle, then adding PVDF and conductive carbon black, stirring uniformly, then adding the mixed active material obtained in the step (1), and stirring uniformly to obtain a first slurry, wherein the active material is prepared from the following components in percentage by mass: PVDF: conductive carbon black 100:3: 3;
3) adding NMP into a stirring kettle, then adding CMC, PVDF and conductive carbon black, stirring uniformly, and then adding LiFe0.9Mn0.1PO4(ii) a The LiFe0.9Mn0.1PO4The average particle size is 0.8 mu m, and the second slurry is obtained by uniformly stirring, wherein the mass ratio of the LiFe to the first slurry is0.9Mn0.1PO4: CMC: PVDF: conductive carbon black 100:3:3: 6;
4) coating and drying first slurry and second slurry on an aluminum foil, wherein the coating thickness ratio of the first slurry to the second slurry is 6:4, and obtaining the anode;
5) adding deionized water into a stirring kettle, then adding SBR and conductive carbon black, uniformly stirring, and then adding natural graphite to obtain negative electrode slurry, wherein the natural graphite: SBR: conductive carbon black 100:4: 4;
6) coating and drying the negative electrode slurry on the copper foil to obtain the negative electrode;
7) laminating a positive electrode, a diaphragm and a negative electrode into a battery cell, placing the battery cell in a shell, and injecting electrolyte, wherein the content of PST in the electrolyte is 1 volume percent, and the content of MMDS is 1.35 volume percent;
8) charging to 3.2V at a constant current of 0.05C;
9) performing constant current charge and discharge at 0.02C between 3.2V and 3.4V for 5 times;
10) charging to 4.25V at constant current of 0.05C, and then charging at constant voltage of 4.25V until the charging current is less than 0.01C;
11) and performing 0.05C constant-current charge and discharge circulation for 3 times between 4.25V and 2.75V to obtain the battery.
Example 2
1) Mixing LiMn0.83Co0.15Al0.02O2And LiFe0.9Mn0.1PO4Ball milling and mixing the LiMn and the LiMn in a mass ratio of 9:10.83Co0.15Al0.02O2An average particle diameter of 2.0 μm, saidLiFe0.9Mn0.1PO4The average particle diameter is 1.4 mu m;
2) adding NMP into a stirring kettle, then adding PVDF and conductive carbon black, stirring uniformly, then adding the mixed active material obtained in the step (1), and stirring uniformly to obtain a first slurry, wherein the active material is prepared from the following components in percentage by mass: PVDF: conductive carbon black 100:5: 5;
3) adding NMP into a stirring kettle, then adding CMC, PVDF and conductive carbon black, stirring uniformly, and then adding LiFe0.9Mn0.1PO4(ii) a The LiFe0.9Mn0.1PO4The average particle size is 1 mu m, and the second slurry is obtained by uniformly stirring, wherein the mass ratio of the LiFe to the first slurry is0.9Mn0.1PO4: CMC: PVDF: conductive carbon black 100:5:5: 10;
4) coating and drying first slurry and second slurry on an aluminum foil, wherein the coating thickness ratio of the first slurry to the second slurry is 9:1, and obtaining the anode;
5) adding deionized water into a stirring kettle, then adding SBR and conductive carbon black, uniformly stirring, and then adding natural graphite to obtain negative electrode slurry, wherein the natural graphite: SBR: conductive carbon black 100:4: 4;
6) coating and drying the negative electrode slurry on the copper foil to obtain the negative electrode;
7) laminating a positive electrode, a diaphragm and a negative electrode into a battery cell, placing the battery cell in a shell, and injecting an electrolyte, wherein the content of PST in the electrolyte is 2 volume percent, and the content of MMDS is 2.8 volume percent;
8) charging to 3.3V at a constant current of 0.05C;
9) performing constant current charge and discharge at 0.02C between 3.3V and 3.5V for 5 times;
10) charging to 4.25V at constant current of 0.05C, and then charging at constant voltage of 4.25V until the charging current is less than 0.01C;
11) and performing 0.05C constant-current charge and discharge circulation for 3 times between 4.25V and 2.75V to obtain the battery.
Example 3
1) Mixing LiMn0.83Co0.15Al0.02O2And LiFe0.9Mn0.1PO4Ball milling and mixing the LiMn and the LiMn in a mass ratio of 85:150.83Co0.15Al0.02O2An average particle diameter of 1.9 μm, said LiFe0.9Mn0.1PO4The average particle diameter is 1.9 μm;
2) adding NMP into a stirring kettle, then adding PVDF and conductive carbon black, stirring uniformly, then adding the mixed active material obtained in the step (1), and stirring uniformly to obtain a first slurry, wherein the active material is prepared from the following components in percentage by mass: PVDF: conductive carbon black 100:4: 4;
3) adding NMP into a stirring kettle, then adding CMC, PVDF and conductive carbon black, stirring uniformly, and then adding LiFe0.9Mn0.1PO4(ii) a The LiFe0.9Mn0.1PO4The average particle size is 0.9 mu m, and the second slurry is obtained by uniformly stirring, wherein the mass ratio of the LiFe to the first slurry is0.9Mn0.1PO4: CMC: PVDF: conductive carbon black 100:4:4: 8;
4) coating and drying first slurry and second slurry on an aluminum foil, wherein the coating thickness ratio of the first slurry to the second slurry is 8:2, and obtaining the anode;
5) adding deionized water into a stirring kettle, then adding SBR and conductive carbon black, uniformly stirring, and then adding natural graphite to obtain negative electrode slurry, wherein the natural graphite: SBR: conductive carbon black 100:4: 4;
6) coating and drying the negative electrode slurry on the copper foil to obtain the negative electrode;
7) laminating a positive electrode, a diaphragm and a negative electrode into a battery cell, placing the battery cell in a shell, and injecting electrolyte, wherein the content of PST in the electrolyte is 1.5 volume percent, and the content of MMDS is 2.1 volume percent;
8) charging to 3.25V at a constant current of 0.05C;
9) performing constant current charge and discharge at 0.02C between 3.25V and 3.45V for 5 times;
10) charging to 4.25V at constant current of 0.05C, and then charging at constant voltage of 4.25V until the charging current is less than 0.01C;
11) and performing 0.05C constant-current charge and discharge circulation for 3 times between 4.25V and 2.75V to obtain the battery.
Comparative example 1
LiMn as described in step 1)0.83Co0.15Al0.02O2The average particle diameter is 3.0 mu m, and the LiFe0.9Mn0.1PO4The average particle size is 2 μm; said LiFe in step 3)0.9Mn0.1PO4The average particle size was 2 μm, and the other process parameters were the same as in example 3.
Comparative example 2
The first slurry contains only LiMn0.83Co0.15Al0.02O2The other process parameters were the same as in example 3.
Comparative example 3
The coating thickness ratio of the first slurry to the second slurry is 10:0, that is, the positive electrode is obtained by coating all the first slurry, and other process parameters are the same as those in example 3.
Comparative example 4
The electrolyte only contains PST, and other process parameters are the same as those of the embodiment 3.
Comparative example 5
The electrolyte only contains MMDS, and other process parameters are the same as those of the embodiment 3.
Comparative example 6
The electrolyte contains 1.5 volume percent of PST and 3 volume percent of MMDS, and other process parameters are the same as those in example 3.
Comparative example 7
The formation process is carried out for 3 times by carrying out 0.05C constant current charge-discharge circulation between 4.25V and 2.75V, and other parameters are the same as those of the embodiment 3.
Experiment and data
The capacity of the batteries respectively obtained according to the formation methods of examples 1 to 3 and comparative examples 1 to 7 was measured, and then the batteries were subjected to charge and discharge cycles at 0.5C rate at normal temperature and high temperature of 50 ℃ for 100 times to calculate the capacity retention rate, and the results are shown in the following table. Therefore, the structural arrangement and the particle size selection of the material have great influence on the cyclicity; the selection and the proportion of the additive have obvious effect of improving the high-temperature performance; and the formation process can further promote the improvement of the cycle performance.
TABLE 1
At normal temperature% High temperature%
Example 1 98.1 95.2
Example 2 97.5 95.4
Example 3 98.6 96.0
Comparative example 1 92.1 90.2
Comparative example 2 86.4 82.1
Comparative example 3 85.3 80.1
Comparative example 4 88.9 84.5
Comparative example 5 90.2 86.4
Comparative example 6 89.2 85.9
Comparative example 7 94.5 92.1
While the present invention has been described in detail with reference to the preferred embodiments, it should be understood that the above description should not be taken as limiting the invention.

Claims (3)

1. A preparation method of a lithium manganate battery comprises the following steps:
step 1) LiMn0.83Co0.15Al0.02O2And LiFe0.9Mn0.1PO4Ball milling and mixing the LiMn and the LiMn in a ratio of 8:2-9:10.83Co0.15Al0.02O2The average grain diameter is 1.8-2.0 mu m, and the LiFe0.9Mn0.1PO4The average grain diameter is 1.2-1.4 μm;
step 2) adding a solvent into a stirring kettle, then adding a binder and a conductive agent, uniformly stirring, then adding the mixed active material obtained in the step 1, and uniformly stirring to obtain a first slurry, wherein the active material is prepared from the following components in percentage by mass: adhesive: the conductive agent is 100:3-5: 3-5;
step 3) adding a solvent into a stirring kettle, then adding a dispersing agent, a binder and a conductive agent, uniformly stirring, and then adding LiFe0.9Mn0.1PO4(ii) a The LiFe0.9Mn0.1PO4Has an average particle diameter of0.8-1 mu m, and uniformly stirring to obtain a second slurry, wherein the mass ratio of the LiFe to the first slurry is0.9Mn0.1PO4: dispersing agent: adhesive: the conductive agent is 100:3-5:3-5: 6-10;
step 4) coating and drying the first slurry and the second slurry on the aluminum foil, wherein the coating thickness ratio of the first slurry to the second slurry is 6:4-9: 1; obtaining a positive electrode;
step 5) adding a solvent into a stirring kettle, then adding a binder and a conductive agent, uniformly stirring, and adding natural graphite to obtain negative electrode slurry;
step 6), coating and drying the negative electrode slurry on the copper foil to obtain a negative electrode;
and 7) laminating the anode, the diaphragm and the cathode into a battery cell, placing the battery cell in a shell, injecting an electrolyte, wherein the electrolyte contains an additive accounting for 3-5 vol% of the electrolyte, and the additive consists of 1-propylene-1, 3-sultone PST and methylene methanedisulfonate MMDS, and the volume ratio of PST: MMDS ═ 1: 1.35-1.40;
step 8) forming to obtain the lithium manganate battery;
the formation of the step 8) comprises the following steps:
i) constant current charging to a first preset voltage, wherein the first preset voltage is 3.2-3.3V;
II) carrying out constant-current charge-discharge circulation for a plurality of times between a first preset voltage and a second preset voltage, wherein the second preset voltage is 3.4-3.5V;
III) charging at constant current to a charging cut-off voltage, and then charging at constant voltage by using the charging cut-off voltage until the charging current is less than a preset value;
IV) carrying out constant-current charge-discharge circulation for a plurality of times between the charge cut-off voltage and the discharge cut-off voltage.
2. The method of claim 1, wherein the charge cutoff voltage is 4.25V and the discharge cutoff voltage is 2.75V.
3. The method according to claim 1, wherein the organic solvent of the electrolyte is selected from cyclic carbonates and chain carbonates.
CN202010107700.6A 2020-02-21 2020-02-21 Preparation method of lithium manganate battery Active CN111293365B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202010107700.6A CN111293365B (en) 2020-02-21 2020-02-21 Preparation method of lithium manganate battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202010107700.6A CN111293365B (en) 2020-02-21 2020-02-21 Preparation method of lithium manganate battery

Publications (2)

Publication Number Publication Date
CN111293365A CN111293365A (en) 2020-06-16
CN111293365B true CN111293365B (en) 2021-11-26

Family

ID=71019148

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202010107700.6A Active CN111293365B (en) 2020-02-21 2020-02-21 Preparation method of lithium manganate battery

Country Status (1)

Country Link
CN (1) CN111293365B (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112201869B (en) * 2020-10-19 2022-10-11 苏州极闪控电信息技术有限公司 Formation method of ternary lithium ion battery
CN112864467A (en) * 2021-01-28 2021-05-28 苏州酷卡环保科技有限公司 Method for preparing lithium ion battery
CN113823765B (en) * 2021-08-10 2022-12-23 星恒电源股份有限公司 Lithium manganate/lithium manganese iron phosphate composite positive plate and lithium ion battery
CN115458707A (en) * 2022-10-26 2022-12-09 欣旺达电动汽车电池有限公司 Secondary battery and electric equipment

Family Cites Families (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102779998A (en) * 2012-07-19 2012-11-14 东莞新能源科技有限公司 Lithium ion monomer battery capable of preventing overdischarge
CN103441305B (en) * 2013-08-27 2016-09-21 深圳市贝特瑞新能源材料股份有限公司 A kind of power and energy storage lithium ion battery and preparation method thereof
CN105336943A (en) * 2015-11-24 2016-02-17 四川省有色冶金研究院有限公司 Lithium battery formed on basis of lithium nickel manganese oxide and lithium titanate and preparation method of lithium battery
CN105655639B (en) * 2016-01-11 2018-10-12 东莞新能源科技有限公司 electrolyte and lithium ion battery including the electrolyte
US10804567B2 (en) * 2017-05-11 2020-10-13 Korea Institute Of Science And Technology Electrolyte system for lithium metal secondary battery and lithium metal secondary battery including the same
CN109119688A (en) * 2017-06-23 2019-01-01 宁德时代新能源科技股份有限公司 electrolyte and electrochemical energy storage device
CN108054431A (en) * 2017-12-29 2018-05-18 惠州亿纬锂能股份有限公司 A kind of lithium ion cylinder battery suitable for the electrolyte of fast charge system and comprising the electrolyte
CN113594409B (en) * 2018-02-26 2022-09-20 宁德新能源科技有限公司 Pole piece and lithium ion battery
KR102100854B1 (en) * 2018-02-26 2020-04-21 한국과학기술연구원 Anode for lithium metal battery comprising Ti2C thin film, preparation method thereof and lithium metal battery comprising the same
CN109599595B (en) * 2018-11-28 2020-05-19 深圳市山木新能源科技股份有限公司 Formation method of lithium ion battery
CN110416611B (en) * 2019-07-17 2022-02-11 珠海市赛纬电子材料股份有限公司 Non-aqueous electrolyte of lithium ion battery and lithium ion battery using same
CN110534829B (en) * 2019-09-12 2020-12-11 泰州纳新新能源科技有限公司 Long-term storage method of lithium ion battery

Also Published As

Publication number Publication date
CN111293365A (en) 2020-06-16

Similar Documents

Publication Publication Date Title
CN111293365B (en) Preparation method of lithium manganate battery
CN111653829A (en) Lithium ion battery electrolyte and lithium ion battery
CN109473719B (en) Lithium ion battery electrolyte and lithium ion battery containing same
CN104600362A (en) Power battery and lithium ion electrolyte thereof
CN107069093B (en) High-concentration ester electrolyte for lithium-sulfur battery
CN110931843B (en) Novel lithium metal negative electrode high-voltage positive electrode solid-liquid battery
CN110265622B (en) Positive electrode plate and lithium ion secondary battery
CN109888384B (en) Electrolyte and battery containing the same
CN109671982B (en) High-temperature high-safety electrolyte matched with silicon-carbon negative electrode material for lithium ion battery
CN111969183B (en) Positive pole piece, preparation method thereof, and lithium ion secondary battery, electric vehicle and electronic product related to positive pole piece
CN102340029A (en) Functional additive applied to non-aqueou electrolyte of lithium ion battery
CN102479947A (en) Lithium ion battery anode material and preparation method thereof, and lithium ion battery
CN113517470A (en) High-nickel high-voltage ternary lithium ion battery non-aqueous electrolyte and lithium ion battery
CN116646526B (en) Positive electrode interface film of sodium ion battery, preparation method of positive electrode interface film and sodium ion battery
CN110797544A (en) High-performance lithium primary battery and preparation method thereof
CN115020806A (en) Electrolyte and lithium ion battery containing same
CN112216890B (en) Formation method of lithium manganate battery
CN111710829A (en) Preparation method of lithium ion battery
CN116470003A (en) Pre-lithiated negative electrode piece and lithium ion battery
CN116344915A (en) High-temperature quick-charging lithium ion battery
CN111293366B (en) Preparation method of lithium ion battery with lithium iron phosphate anode
CN106941191B (en) Lithium ion battery and non-aqueous electrolyte thereof
CN111416157B (en) Preparation method of ternary lithium ion battery
CN111370687B (en) Preparation method of lithium ion battery
CN112864467A (en) Method for preparing lithium ion battery

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
TA01 Transfer of patent application right

Effective date of registration: 20211104

Address after: 312000 No.19, Weixi Road, Shangyu economic and Technological Development Zone, Hangzhou Bay, Shaoxing City, Zhejiang Province

Applicant after: GREATPOWER JINCHUAN ADVANCED BATTERY MATERIALS Corp.

Address before: 215000 Room 101, building 13, Longgang second village, Wuzhong District, Suzhou City, Jiangsu Province

Applicant before: Lu Chenjie

TA01 Transfer of patent application right
GR01 Patent grant
GR01 Patent grant
CP01 Change in the name or title of a patent holder

Address after: 312000 No.19, Weixi Road, Shangyu economic and Technological Development Zone, Hangzhou Bay, Shaoxing City, Zhejiang Province

Patentee after: Zhejiang Gepai cobalt industry new material Co.,Ltd.

Address before: 312000 No.19, Weixi Road, Shangyu economic and Technological Development Zone, Hangzhou Bay, Shaoxing City, Zhejiang Province

Patentee before: GREATPOWER JINCHUAN ADVANCED BATTERY MATERIALS Corp.

CP01 Change in the name or title of a patent holder