CN106450336A - Lithium ion battery negative electrode slurry and preparation method thereof - Google Patents
Lithium ion battery negative electrode slurry and preparation method thereof Download PDFInfo
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- CN106450336A CN106450336A CN201611110223.9A CN201611110223A CN106450336A CN 106450336 A CN106450336 A CN 106450336A CN 201611110223 A CN201611110223 A CN 201611110223A CN 106450336 A CN106450336 A CN 106450336A
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- lithium ion
- ion battery
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- active substance
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
- H01M4/624—Electric conductive fillers
- H01M4/625—Carbon or graphite
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
- H01M4/621—Binders
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
- H01M4/624—Electric conductive fillers
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
Abstract
The invention provides lithium ion battery negative electrode slurry. The lithium ion battery negative electrode slurry comprises an active substance, a binding agent, a thickening agent and an additive, wherein the mass ratio of the active substance to the binding agent to the thickening agent to the additive is (80-98):(1.0-5.0):(0.5-5.0):(0.5-10.0); the additive is a mixture of graphene, conductive zinc oxide and MoS2; the active substance is one or more of artificial graphite, natural graphite, mesocarbon microbeads, hard carbon and soft carbon; the binding agent is butadiene styrene rubber; and the thickening agent is sodium carboxymethylcellulose. The invention also provides a preparation method of the lithium ion battery negative electrode slurry. The method is simple, and a lithium ion battery prepared by the lithium ion battery negative electrode slurry has high safety and long cycle life.
Description
Technical field
The present invention relates to a kind of cathode size and preparation method thereof, particularly to a kind of lithium ion battery cathode slurry and its
Preparation method.
Background technology
Since the nineties in 20th century, lithium rechargeable battery has obtained extensively should in various portable type electronic products
With.With developing rapidly of modern society's electronic product and going deep into further of the research and development of electric powered motor power supply,
People are increasingly strong to the demand of high performance lithium ion battery, in the urgent need to the lithium-ion electric of exploitation long-life, high safety performance
Pond product.To the significance level of lithium ion battery without superfluous words, for macroscopic view, longer cycle life means cycle performance
Less resource consumption.And, own of common occurrence, the lithium of the fire even report of blast causing with regard to lithium ion battery in recent years
The safety problem of ion battery also causes the universal concern of people.
Content of the invention
The present invention is intended to provide a kind of improve lithium ion battery safety performance and extend cycle life of lithium ion battery
Lithium ion battery cathode slurry, provides its preparation method simultaneously.
The present invention is realized by below scheme:
A kind of lithium ion battery cathode slurry it is characterised in that:Including negative electrode active material, binding agent, thickening agent with add
Plus agent, the mass ratio of described active substance, binding agent, thickening agent and additive is (80~98):(1.0~5.0):(0.5~
5.0):(0.5~10.0);Described additive is Graphene, conductive zinc oxide and MoS2Mixture;Described active substance is behaved
Make one or more of graphite, native graphite, MCMB, hard carbon, soft carbon;Described binding agent is styrene butadiene rubber sbr;
Described thickening agent is sodium carboxymethyl cellulose CMC.
Further, Graphene, conductive zinc oxide and MoS in described additive2Mass ratio be (20~45):(20~
45):(10~40).
Operability in view of painting process and quality level, the solid content general control of cathode size is 35~
60%, viscosity general control is 1000~5000mPa s.
A kind of method preparing lithium ion battery cathode slurry as above, is carried out according to the following steps:
(1) active substance, binding agent, thickening agent, additive and solvent have been weighed in proportion, by active substance, thickening agent
All add low speed premixing in agitating device with additive, mixing time is controlled to 10~60min;General active substance can be first
Sieve, screen cloth selects 150 eye mesh screens;
(2) open the circulation of agitating device, first toward agitating device in addition account for needed for solvent total amount 50%~
70% solvent stirs scraper through multiple, and each mixing time controls in 10~60min, periphery scraper of stopping afterwards;Stir
The revolution rotating speed mixing device is 20~50rpm, and the rotation rotating speed of agitating device is 400~1500rpm;It is typically repeated stirring
Scraper number of times is 2~4 times, and the revolution rotating speed of agitating device and rotation rotating speed all increase with number of times and be stepped up;
(3) add, toward in agitating device, the agitated scraper of solvent accounting for total amount 20%~40% needed for solvent again, stir
Mix time control in 10~60min, periphery scraper of stopping;The revolution rotating speed of agitating device be 20~50rpm, agitating device from
Speed of walking around is 1500~1800rpm;
(4) finally add binding agent and remaining stirring solvent toward in agitating device, until the solid content of cathode size and
Viscosity reaches standard;The revolution rotating speed of agitating device is 20~50rpm, and the rotation rotating speed of agitating device is 800~1300rpm;
The solid content general control of cathode size is 35~60%, and viscosity general control is 1000~5000mPa s, works as cathode size
Solid content and viscosity all reach can stop during standard stir, during actual fabrication mixing time be generally 10~30min.
During actual fabrication, remaining solvent can be gradually added, preferably to control the solid content of cathode size and viscosity to meet
Require, when solid content and the viscosity superelevation of cathode size, can be adjusted by increasing appropriate solvent.
A kind of lithium ion battery cathode slurry of the present invention, its additive is Graphene, conductive zinc oxide and MoS2Mixed
Compound.Graphene is by the planar material of the hexagonal honeycomb lattice of monolayer carbon atomic building, and theoretic throat is only 0.34
Nanometer, has higher electron mobility, adds the conduction that Graphene can be effectively improved negative electrode active material in cathode size
Performance, improves the diffusion transport ability of lithium ion;Conductive zinc oxide is a kind of polyfunctional semi-conducting material, its importance
One of energy is exactly its electric conductivity, and its crystal structure is wurtzite-type, in its structure, is not strict around each ion
Symmetrical, the key before zinc ion and oxonium ion be substantially polarity that is to say, that conductive zinc oxide is polar structure body, be
One of advantage of its high conductivity, under room temperature, the resistivity of conductive zinc oxide can reach 0.068 Ω cm, even lower.
Using conductive zinc oxide as conductive agent, between active substance, play between active substance and collector and collect micro-current
Effect, it is possible to reduce the contact resistance of electrode, accelerates the rate travel of electronics, also can effectively improve lithium ion in electrode simultaneously
Migration rate in material, thus improving the high rate during charging-discharging of battery, extend that battery 1C charge and discharge and 1C fill that 10C puts follows
The ring life-span;MoS2It is a kind of transient metal sulfide, there is very typical S-Mo-S sandwich structure, i.e. two sulfur layer folders one
Individual Mo metal level, links together by strong covalent bond between atom in layer, and then leans on relatively weak model moral between layers
Hua Li is connected with each other, and this structure allows lithium ion quickly to embed and deviate from.The lithium ion battery of the preparation present invention is born
The method of pole slurry, process is simple, directly use existing apparatus.Lithium-ion electric using the cathode size preparation of the present invention
Pond, has longer cycle life and preferable security performance.
Brief description
The 1C charge and discharge cycle life of the lithium ion battery of the cathode size preparation that Fig. 1 prepares for embodiment 1 method is bent
Line chart;
The 1C of the lithium ion battery of the cathode size preparation that Fig. 2 prepares for embodiment 1 method fills 10C puts cycle life
Curve chart.
Specific embodiment
The invention will be further described with reference to embodiments, but the invention is not limited in the statement of embodiment.
Embodiment 1
A kind of preparation method of lithium ion battery cathode slurry, is carried out according to the following steps:
(1) 45kg Delanium through sieving, 2kg styrene butadiene rubber sbr, 1kg sodium carboxymethyl cellulose CMC, 0.6kg are weighed
Graphene, 0.7kg conductive zinc oxide, 0.7kg MoS2With 61kg deionized water, by Delanium, sodium carboxymethyl cellulose CMC,
Graphene, conductive zinc oxide and MoS2All add low speed premixing in agitator, stir 30min;
(2) open the circulation of agitator, first the addition total amount needed for ionized water 66% that accounts for is toward agitator in
The deionized water of 40.26kg through stirring scraper twice, periphery scraper of stopping after stirring 40min for the first time, the public affairs of blender
Speed of walking around is 30rpm, and the rotation rotating speed of blender is 700rpm;Stop after second stirring 30min periphery scraper, blender
Revolution rotating speed is 40rpm, and the rotation rotating speed of blender is 1000rpm;
(3) add the deionized water that the total amount needed for ionized water 30% that accounts for is 18.3kg toward in agitator again, stir 60min
After stop periphery scraper, the revolution rotating speed of blender is 50rpm, and the rotation rotating speed of blender is 1600rpm;
(4) toward in agitator, finally add styrene butadiene rubber sbr and remaining deionized water stirring 20min, the public affairs of blender
Speed of walking around is 30rpm, and the rotation rotating speed of blender is 800rpm.
Take the lithium ion battery cathode slurry preparing through above-mentioned steps on a small quantity to survey its solid content and viscosity, record it
Solid content is 45%, and viscosity is 2300mPa s.
The lithium ion battery cathode slurry that embodiment 1 is prepared is by the work of column lithium ion battery 18650-2300
Skill makes negative plate, and is fabricated to battery by the technique of column lithium ion battery 18650-2300.The battery made is taken to make
It is 4.2V with 1C constant-current constant-voltage charging to blanking voltage, cut-off current is 20mA, using 1C constant-current discharge to 2.75V, its circulation
Life curve figure is as shown in figure 1, it will be seen from figure 1 that circulating battery to 2000 times, battery capacity conservation rate is still on 90% left side
Right;The 1C discharge and recharge of existing heavy-current discharge battery 500 times, battery capacity just can only be maintained at 80% about substantially.Take
The battery made is 4.2V using 1C constant-current constant-voltage charging to blanking voltage, and cut-off current is 20mA, using 10C constant-current discharge
To 2.75V, its cycle life curve chart is as shown in Fig. 2 figure it is seen that circulating battery to 500 times, battery capacity keeps
Rate is still 91% about;And existing its 10C of heavy-current discharge battery electric discharge is in circulation 300 times, battery capacity just exists substantially
Less than 80%.It can be seen that column lithium ion battery prepared by the lithium ion battery cathode slurry that use the present embodiment prepares,
Either 1C charge and discharge or 1C fill 10C and put, and its cycle life is all very good.
Embodiment 2
A kind of preparation method of lithium ion battery cathode slurry, is carried out according to the following steps:
(1) weigh 34kg native graphite through sieving, 2kg styrene butadiene rubber sbr, 1.6kg sodium carboxymethyl cellulose CMC,
0.7kg Graphene, 0.8kg conductive zinc oxide, 0.5kg MoS2With 62.4kg deionized water, by native graphite, carboxymethyl cellulose
Plain sodium CMC, Graphene, conductive zinc oxide and MoS2All add low speed premixing in agitator, stir 40min;
(2) open the circulation of agitator, first the addition total amount needed for ionized water 70% that accounts for is toward agitator in
The deionized water of 43.68kg through triple mixing scraper, periphery scraper of stopping after stirring 30min for the first time, the public affairs of blender
Speed of walking around is 20rpm, and the rotation rotating speed of blender is 600rpm;Stop after second stirring 30min periphery scraper, blender
Revolution rotating speed is 30rpm, and the rotation rotating speed of blender is 800rpm;Stop periphery scraper after third time stirring 25min, blender
Revolution rotating speed be 40rpm, the rotation rotating speed of blender is 1000rpm;
(3) deionized water that the total amount needed for ionized water 20% that accounts for is 12.48kg, stirring are added again toward in agitator
Stop after 40min periphery scraper, the revolution rotating speed of blender is 40rpm, the rotation rotating speed of blender is 1700rpm;
(4) toward in agitator, finally add styrene butadiene rubber sbr and remaining deionized water stirring 30min, the public affairs of blender
Speed of walking around is 40rpm, and the rotation rotating speed of blender is 1000rpm.
Take the lithium ion battery cathode slurry preparing through above-mentioned steps on a small quantity to survey its solid content and viscosity, record it
Solid content is 39%, and viscosity is 1800mPa s.
Embodiment 3
A kind of preparation method of lithium ion battery cathode slurry, is carried out according to the following steps:
(1) 33.2kg native graphite through sieving, 1.6kg styrene butadiene rubber sbr, 1.2kg sodium carboxymethyl cellulose are weighed
CMC, 1.6kg Graphene, 0.8kg conductive zinc oxide, 1.6kg MoS2With 40kg deionized water, will be fine to native graphite, carboxymethyl
The plain sodium CMC of dimension, Graphene, conductive zinc oxide and MoS2All add low speed premixing in agitator, stir 60min;
(2) open the circulation of agitator, first the addition total amount needed for ionized water 55% that accounts for is toward agitator in
Through four stirring scrapers, periphery scraper of stopping after stirring 30min for the first time, the revolution of blender turns the deionized water of 22kg
Speed is 25rpm, and the rotation rotating speed of blender is 700rpm;Stop after second stirring 30min periphery scraper, the revolution of blender
Rotating speed is 35rpm, and the rotation rotating speed of blender is 900rpm;Stop periphery scraper after third time stirring 15min, the public affairs of blender
Speed of walking around is 40rpm, and the rotation rotating speed of blender is 1100rpm;Stop periphery scraper after 4th stirring 10min, blender
Revolution rotating speed be 45rpm, the rotation rotating speed of blender is 1300rpm;
(3) add the deionized water that the total amount needed for ionized water 40% that accounts for is 16kg again toward in agitator, after stirring 60min
Stop periphery scraper, the revolution rotating speed of blender is 50rpm, the rotation rotating speed of blender is 1800rpm;
(4) toward in agitator, finally add styrene butadiene rubber sbr and remaining deionized water stirring 15min, the public affairs of blender
Speed of walking around is 25rpm, and the rotation rotating speed of blender is 1300rpm.
Take the lithium ion battery cathode slurry preparing through above-mentioned steps on a small quantity to survey its solid content and viscosity, record it
Solid content is 50%, and viscosity is 3000mPa s.
It is only presently preferred embodiments of the present invention above, according to the above-mentioned design of the present invention, the common skill of the art
Art personnel also can make various modifications and alterations to this, under the premise without departing from the principles of the invention, also should be considered as the present invention
Protection domain.
Claims (6)
1. a kind of lithium ion battery cathode slurry it is characterised in that:Including active substance, binding agent, thickening agent and additive, institute
The mass ratio stating active substance, binding agent, thickening agent and additive is (80~98):(1.0~5.0):(0.5~5.0):(0.5
~10.0);Described additive is Graphene, conductive zinc oxide and MoS2Mixture;Described active substance is Delanium, sky
So one or more of graphite, MCMB, hard carbon, soft carbon;Described binding agent is butadiene-styrene rubber;Described thickening agent is
Sodium carboxymethyl cellulose.
2. as claimed in claim 1 a kind of lithium ion battery cathode slurry it is characterised in that:Graphene in described additive,
Conductive zinc oxide and MoS2Mass ratio be (20~45):(20~45):(10~40).
3. as claimed in claim 1 or 2 a kind of it is characterised in that:The solid content of cathode size is 35%~60%, and viscosity is
1000~5000mPa s.
4. a kind of method preparing described lithium ion battery cathode slurry as arbitrary in claims 1 to 3 it is characterised in that:Press
Ratio has weighed active substance, binding agent, thickening agent, additive and solvent, and active substance, thickening agent and additive are all added
Enter premixing in agitating device, open the circulation of agitating device afterwards, be initially charged account for needed for solvent total amount 50%~
70% solvent, through repeatedly repeatedly stirring scraper, adds the solvent accounting for total amount 20%~40% needed for solvent through stirring
Mix scraper, be eventually adding binding agent and remaining stirring solvent, until the solid content of cathode size and viscosity reach standard.
5. as claimed in claim 4 a kind of method preparing lithium ion battery cathode slurry it is characterised in that:Described addition accounts for
In the solvent step of total amount 50%~70% needed for solvent, stirring scraper number of times is 2~4 times, and the revolution of agitating device turns
Speed and rotation rotating speed all increase with number of times and are stepped up.
6. a kind of method preparing lithium ion battery cathode slurry as described in claim 4 or 5 it is characterised in that:Described molten
Agent is deionized water.
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CN107086292A (en) * | 2017-03-27 | 2017-08-22 | 湖北猛狮新能源科技有限公司 | A kind of high viscosity lithium ion battery slurry-stirring process |
CN107403914A (en) * | 2017-07-03 | 2017-11-28 | 江西安驰新能源科技有限公司 | A kind of dry mixing process of artificial plumbago negative pole slurry |
CN107819118A (en) * | 2017-10-26 | 2018-03-20 | 深圳市斯诺实业发展股份有限公司 | A kind of shunting cathode of lithium battery blank preparation technicses |
CN108172750A (en) * | 2017-12-07 | 2018-06-15 | 银隆新能源股份有限公司 | The preparation method of graphite negative electrode of lithium ion battery highly viscous slurry |
CN108630884A (en) * | 2018-05-21 | 2018-10-09 | 重庆市紫建电子有限公司 | A kind of lithium ion battery anode slurry preparation method |
CN111180659A (en) * | 2019-12-30 | 2020-05-19 | 江西安驰新能源科技有限公司 | Preparation method of lithium ion battery cathode slurry |
EP3680962A1 (en) * | 2019-01-09 | 2020-07-15 | The Provost, Fellows, Scholars and other Members of Board of Trinity College Dublin | High capacity electrodes enabled by 2d materials in a viscous aqueous ink |
CN113178620A (en) * | 2021-04-30 | 2021-07-27 | 天能帅福得能源股份有限公司 | Preparation method of lithium ion battery with high-power charging performance |
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Publication number | Priority date | Publication date | Assignee | Title |
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CN107086292A (en) * | 2017-03-27 | 2017-08-22 | 湖北猛狮新能源科技有限公司 | A kind of high viscosity lithium ion battery slurry-stirring process |
CN107403914A (en) * | 2017-07-03 | 2017-11-28 | 江西安驰新能源科技有限公司 | A kind of dry mixing process of artificial plumbago negative pole slurry |
CN107819118A (en) * | 2017-10-26 | 2018-03-20 | 深圳市斯诺实业发展股份有限公司 | A kind of shunting cathode of lithium battery blank preparation technicses |
CN108172750A (en) * | 2017-12-07 | 2018-06-15 | 银隆新能源股份有限公司 | The preparation method of graphite negative electrode of lithium ion battery highly viscous slurry |
CN108630884A (en) * | 2018-05-21 | 2018-10-09 | 重庆市紫建电子有限公司 | A kind of lithium ion battery anode slurry preparation method |
EP3680962A1 (en) * | 2019-01-09 | 2020-07-15 | The Provost, Fellows, Scholars and other Members of Board of Trinity College Dublin | High capacity electrodes enabled by 2d materials in a viscous aqueous ink |
WO2020144289A1 (en) | 2019-01-09 | 2020-07-16 | The Provost, Fellows, Scholars And Other Members Of Board Of Trinity College Dublin | High capacity electrodes enabled by 2d materials in a viscous aqueous ink |
CN111180659A (en) * | 2019-12-30 | 2020-05-19 | 江西安驰新能源科技有限公司 | Preparation method of lithium ion battery cathode slurry |
CN111180659B (en) * | 2019-12-30 | 2021-03-12 | 江西安驰新能源科技有限公司 | Preparation method of lithium ion battery cathode slurry |
CN113178620A (en) * | 2021-04-30 | 2021-07-27 | 天能帅福得能源股份有限公司 | Preparation method of lithium ion battery with high-power charging performance |
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