[go: up one dir, main page]
More Web Proxy on the site http://driver.im/

CN102024940A - Process for producing anode slurry and cathode slurry for lithium ion power battery core - Google Patents

Process for producing anode slurry and cathode slurry for lithium ion power battery core Download PDF

Info

Publication number
CN102024940A
CN102024940A CN2010105271340A CN201010527134A CN102024940A CN 102024940 A CN102024940 A CN 102024940A CN 2010105271340 A CN2010105271340 A CN 2010105271340A CN 201010527134 A CN201010527134 A CN 201010527134A CN 102024940 A CN102024940 A CN 102024940A
Authority
CN
China
Prior art keywords
slurry
solvent
binding agent
cathode
anode
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.)
Granted
Application number
CN2010105271340A
Other languages
Chinese (zh)
Other versions
CN102024940B (en
Inventor
李春生
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.)
ANHUI ZHONGLING ELECTRIC MOTOR Co Ltd
Original Assignee
ANHUI ZHONGLING ELECTRIC MOTOR Co Ltd
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 ANHUI ZHONGLING ELECTRIC MOTOR Co Ltd filed Critical ANHUI ZHONGLING ELECTRIC MOTOR Co Ltd
Priority to CN201010527134.0A priority Critical patent/CN102024940B/en
Publication of CN102024940A publication Critical patent/CN102024940A/en
Application granted granted Critical
Publication of CN102024940B publication Critical patent/CN102024940B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • 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

Landscapes

  • Battery Electrode And Active Subsutance (AREA)

Abstract

The invention relates to a process for producing anode slurry and cathode slurry for a lithium ion power battery core. When the anode slurry and the cathode slurry are produced, anode and cathode active substances are pretreated and then prepared into the anode slurry and the cathode slurry respectively. The process comprises the following steps of: when the anode slurry is prepared, mixing acetylene black serving as a conductive agent and adhesive, then adding a solvent and the pretreated active substances, and fully stirring the mixture uniformly to produce the anode slurry; and when the cathode slurry is prepared, fully dissolving adhesive into deionized water, adding a solvent, stirring the solution uniformly, adding the pretreated cathode active substance graphite, stirring the solution uniformly, and finally adding neutral vinyltriethoxysilane to produce the cathode slurry. The active substances of a lithium ion power battery produced by using the anode slurry and the cathode slurry have high specific capacity, and high battery capacity still can be kept after multiple times of recycling.

Description

A kind of production technology of electric core of lithium ion power battery positive and negative electrode slurry
Technical field
The present invention relates to lithium battery manufacturing technology field, be specifically related to a kind of production technology of electric core of lithium ion power battery positive and negative electrode slurry.
Background technology
Electric core of lithium ion power battery generally is made up of positive pole, negative pole, diaphragm paper, electrolyte and housing, its manufacture craft at first is after positive and negative pole material is handled, high molecular polymer, inorganic compound and auxiliary material are fully mixed under stirring state, through sieving, make dispersion: amount in accordance with regulations will disperse somaplasm cloth on the template of regulatory specifications then, after roll-in, cut, reel (stacked), the welding, promptly through the aging check; Carry out the charging measurement packing at last.
By the electric core of lithium ion power battery that existing technology is made, the specific capacity of its active material is lower, and after repeatedly recycling, the decline of battery capacity is comparatively obvious, and these deficiencies all await further being improved.
Summary of the invention
The objective of the invention is to deficiency at existing technology for manufacturing electric core of lithium ion power battery, a kind of specific capacity that improves the lithium-ion-power cell active material is provided, and after repeatedly recycling, still can keep the production technology of the electric core of lithium ion power battery positive and negative electrode slurry of higher battery capacity.
The following technical scheme of employing of the present invention:
A kind of collocation method of electric core of lithium ion power battery positive and negative electrode slurry is characterized in that: specifically may further comprise the steps:
(1) preliminary treatment of positive electrode
A, usefulness bolting anode active material of phosphate iron lithium particle, the particle diameter that requires LiFePO4 is 3.6~9um
B, the isolated LiFePO4 of step (a) is dewatered, under the normal pressure, 110-130 ℃ of baking 1.5-2.5 hour;
C, with conductive agent dehydration, require under the normal pressure 190-210 ℃ of baking 1.5-2.5 hour;
D, with binding agent dehydration, 120-140 ℃ of normal pressure baking 1.5-2.5 hour;
(2) negative material preliminary treatment
A, graphite is mixed; ,
B, the graphite that mixes is toasted at normal pressure, remove surperficial oily matter, baking temperature is 300-400 ℃;
C, suitably dilute binding agent with deionized water;
(3) preparation of anode sizing agent
A, be 1 by weight with conductive agent and binding agent: the ratio of (58~62) is fully mixed;
B, solvent is joined in the compound that step (a) mixes, fully mix with the mode that the ultrasonic wave dissolving disperses, the weight ratio of compound and solvent is 1: (14-16);
C, join in the abundant mixed compound of step (b) with conductive agent with through the mixture of the pretreated anode active material of phosphate iron lithium of step (1), after vacuum stirring dissolving evenly, produce anode sizing agent, wherein, carbon black: LiFePO4: solvent three's weight ratio is 3.5: (98-102): (40-50);
Wherein, described conductive agent is an acetylene black; Described binding agent is polyvinylidene fluoride resin (PVDF); Described solvent is a N-methyl pyrrole Lip river alkane ketone;
(4) preparation of cathode size
A, elder generation fully are dissolved in binding agent in the deionized water, add solvent again, stir, and wherein binding agent, deionized water and solvent three's weight ratio is (1-1.5): (42-48): (5.0-5.5);
B, will join in the material that step (a) mixes through the pretreated negative electrode active material graphite of step (2), and stir, wherein the weight ratio of graphite and deionized water is 100: (42-48);
C, neutral vinyltriethoxysilane is joined in the step (b) again, through vacuum stirring evenly after, produce cathode size, wherein, the weight ratio of the negative pole mixed slurry of neutral vinyltriethoxysilane and step (b) is 1: (285-290);
Wherein, described binding agent is sodium carboxymethylcellulose CMC; Described solvent is a styrene-butadiene latex.
The production technology of described electric core of lithium ion power battery positive and negative electrode slurry, it is characterized in that: the described vibrating screen of step is three layers of screen cloth, the ground floor screen cloth sifts out the LiFePO4 particle of particle diameter greater than 9um, and the second layer and the 3rd layer of mesh screen are fallen particle diameter less than the ultra-fine LiFePO4 particle of 3.5um.
Advantage of the present invention:
1, the specific capacity of active material is improved in the anode sizing agent, the present invention is when the anode sizing agent of preparation electric core of lithium ion power battery, mix with conductive agent acetylene black and binding agent earlier, and then add solvent and active material, make the specific capacity of active material bring up to 140mAh/g by original 135mAh/g; And anode active material of phosphate iron lithium after separating treatment tap density be greatly improved, bring up to 1.8-2.0g/cm3 from 1.3g/cm3, thereby have 5~8% to improve the electric core of lithium ion power battery capacity.
2, when the preparation cathode size, add neutral vinyltriethoxysilane, make electric core after repeatedly recycling, still can keep higher capacity.
Embodiment
Below in conjunction with specific embodiment the present invention is described in detail.
1, before the anode sizing agent that is formulated in the preparation electric core of lithium ion power battery of anode sizing agent, with fully separating with vibrating screen (three layers) with the composition of desired 3.6~9um particle diameter of anode active material of phosphate iron lithium, obtain required LiFePO4 more than or equal to the 10um super-size and smaller or equal to the composition of 3.5um ultra-fine grain diameter.
Take by weighing 0.047 gram conductive agent acetylene black and 2.8 gram binding agent polyvinylidene fluoride resins, add then in the 45 gram solvent n methyl pyrrole Lip river alkane ketone, fully mix with the mode that the ultrasonic wave dissolving disperses, the mixture that adds 3.5 gram conductive agent carbon blacks and 100 gram anode active material of phosphate iron lithium again, after vacuum stirring dissolving evenly, produce anode sizing agent.
2, before the cathode size that is formulated in the preparation electric core of lithium ion power battery of cathode size, it is 300-400 ℃ of baking that negative active core-shell material graphite is mixed back temperature under normal pressure, removes surperficial oily matter;
Take by weighing 1.2 gram binding agent sodium carboxymethylcelluloses, fully be dissolved in the 45 gram deionized waters, adding 5.3 gram styrene-butadiene latexes more fully dissolves, add the treated negative electrode active material graphite of 100 grams then, vacuumize stirring until mixing, add neutral vinyltriethoxysilane 0.525 gram then, after vacuum stirring is even, produce cathode size.

Claims (2)

1. the production technology of an electric core of lithium ion power battery positive and negative electrode slurry is characterized in that: specifically may further comprise the steps:
(1) preliminary treatment of positive electrode
A, usefulness bolting anode active material of phosphate iron lithium particle, the particle diameter that requires LiFePO4 is 3.6~9um;
B, the isolated LiFePO4 of step (a) is dewatered, under the normal pressure, 110-130 ℃ of baking 1.5-2.5 hour;
C, with conductive agent dehydration, require under the normal pressure 190-210 ℃ of baking 1.5-2.5 hour;
D, with binding agent dehydration, 120-140 ℃ of normal pressure baking 1.5-2.5 hour;
(2) negative material preliminary treatment
A, graphite is mixed; ,
B, the graphite that mixes is toasted at normal pressure, remove surperficial oily matter, baking temperature is 300-400 ℃;
C, suitably dilute binding agent with deionized water;
(3) preparation of anode sizing agent
A, be 1 by weight with conductive agent and binding agent: the ratio of (58~62) is fully mixed;
B, solvent is joined in the compound that step (a) mixes, fully mix with the mode that the ultrasonic wave dissolving disperses, the weight ratio of compound and solvent is 1: (14-16);
C, join in the abundant mixed compound of step (b) with conductive agent with through the mixture of the pretreated anode active material of phosphate iron lithium of step (1), after vacuum stirring dissolving evenly, make anode sizing agent, wherein, carbon black: LiFePO4: solvent three's weight ratio is 3.5: (98-102): (40-50);
Wherein, described conductive agent is an acetylene black; Described binding agent is polyvinylidene fluoride resin (PVDF); Described solvent is a N methyl pyrrole Lip river alkane ketone;
(4) preparation of cathode size
A, elder generation fully are dissolved in binding agent in the deionized water, add solvent again, stir, and wherein binding agent, deionized water and solvent three's weight ratio is (3-4.2): (42-48): (5.0-5.5);
B, will join in the material that step (a) mixes through the pretreated negative electrode active material graphite of step (2), and stir, wherein the weight ratio of graphite and deionized water is 100: (42-48);
C, neutral vinyltriethoxysilane is joined in the step (b) again, through vacuum stirring evenly after, make cathode size, wherein, the weight ratio of the negative pole mixed slurry of neutral vinyltriethoxysilane and step (b) is 1: (285-290);
Wherein, described binding agent is the mixture that polytetrafluoroethylene (PTFE) and sodium carboxymethylcellulose (CMC) mix, and the weight ratio of the two is (1.8-3.0): 1.2; Described solvent is a styrene-butadiene latex.
2. the production technology of electric core of lithium ion power battery positive and negative electrode slurry according to claim 1, it is characterized in that: the described vibrating screen of step is three layers of screen cloth, the ground floor screen cloth sifts out the LiFePO4 particle of particle diameter greater than 9um, and the second layer and the 3rd layer of mesh screen are fallen particle diameter less than the ultra-fine LiFePO4 particle of 3.5um.
CN201010527134.0A 2010-10-29 2010-10-29 Process for producing anode slurry and cathode slurry for lithium ion power battery core Expired - Fee Related CN102024940B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201010527134.0A CN102024940B (en) 2010-10-29 2010-10-29 Process for producing anode slurry and cathode slurry for lithium ion power battery core

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201010527134.0A CN102024940B (en) 2010-10-29 2010-10-29 Process for producing anode slurry and cathode slurry for lithium ion power battery core

Publications (2)

Publication Number Publication Date
CN102024940A true CN102024940A (en) 2011-04-20
CN102024940B CN102024940B (en) 2014-09-17

Family

ID=43865986

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201010527134.0A Expired - Fee Related CN102024940B (en) 2010-10-29 2010-10-29 Process for producing anode slurry and cathode slurry for lithium ion power battery core

Country Status (1)

Country Link
CN (1) CN102024940B (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102983306A (en) * 2012-12-24 2013-03-20 天津力神电池股份有限公司 Method for preparing negative pole slurry for lithium ion batteries
CN105609702A (en) * 2014-11-25 2016-05-25 江苏永昌新能源科技有限公司 Formula of lithium battery negative plate and preparation technology thereof
CN106450169A (en) * 2016-08-31 2017-02-22 湖北宇电能源科技股份有限公司 Manufacturing method of negative plate of safety lithium-ion battery
CN111146436A (en) * 2020-03-04 2020-05-12 广东博龙能源科技有限公司 Oily negative electrode material and preparation process thereof
WO2024098410A1 (en) * 2022-11-11 2024-05-16 宁德时代新能源科技股份有限公司 Preparation method for positive electrode slurry, secondary battery, battery pack and electric device

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101414694A (en) * 2007-10-17 2009-04-22 江苏和信电气制造有限公司 Technology for manufacturing electric core of lithium ion power battery
CN101615668A (en) * 2009-08-07 2009-12-30 焦作市亿星锂电厂 Be used to produce the distribution of lithium battery

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101414694A (en) * 2007-10-17 2009-04-22 江苏和信电气制造有限公司 Technology for manufacturing electric core of lithium ion power battery
CN101615668A (en) * 2009-08-07 2009-12-30 焦作市亿星锂电厂 Be used to produce the distribution of lithium battery

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102983306A (en) * 2012-12-24 2013-03-20 天津力神电池股份有限公司 Method for preparing negative pole slurry for lithium ion batteries
CN105609702A (en) * 2014-11-25 2016-05-25 江苏永昌新能源科技有限公司 Formula of lithium battery negative plate and preparation technology thereof
CN106450169A (en) * 2016-08-31 2017-02-22 湖北宇电能源科技股份有限公司 Manufacturing method of negative plate of safety lithium-ion battery
CN111146436A (en) * 2020-03-04 2020-05-12 广东博龙能源科技有限公司 Oily negative electrode material and preparation process thereof
WO2024098410A1 (en) * 2022-11-11 2024-05-16 宁德时代新能源科技股份有限公司 Preparation method for positive electrode slurry, secondary battery, battery pack and electric device

Also Published As

Publication number Publication date
CN102024940B (en) 2014-09-17

Similar Documents

Publication Publication Date Title
CN105932229B (en) A kind of preparation method of high capacity lithium ion cells cathode piece
CN106129357B (en) Deep glue-type spy consolidates lead carbon battery lead plaster
CN100492721C (en) Lithium ion battery pole piece with high multiplying power and production thereof
CN107785549B (en) Preparation method of carbon composite negative electrode material and carbon composite negative electrode material
CN104577012A (en) Rate cycling improved lithium iron phosphate battery and preparation method thereof
CN109687013A (en) A kind of high magnification, high safety, long-life ferric phosphate lithium cell and preparation method thereof
CN104810506A (en) High-energy density lithium ion battery
CN103682307B (en) Nickel ion doped/lithium titanate battery and preparation method thereof
CN102024940B (en) Process for producing anode slurry and cathode slurry for lithium ion power battery core
CN101916861A (en) Cathode lead plaster capable of prolonging fast charge-discharge circulating life of battery and preparation method thereof
CN113675365B (en) Negative plate and lithium ion battery
CN110289401A (en) A kind of lead storage battery cathode carbon composite and cathode lead plaster, lead storage battery
CN103682413A (en) High-rate long-cycle-life lithium iron phosphate battery and preparation method thereof
CN101937990A (en) Preparation method of nano lithium iron phosphate positive slurry
CN105702938B (en) A kind of iron-based oxide lithium ion battery negative material and preparation method and application
CN108172744B (en) Sb for lithium-sulfur battery diaphragm2Se3Method for preparing composite material
CN112635773A (en) Positive pole piece for primary battery and primary battery
CN111554881B (en) MXene-based flexible self-supporting electrode material and preparation method thereof
CN104282933B (en) A kind of low-temperature lithium iron phosphate power and preparation method thereof
CN109888191A (en) Lithium ion battery pole piece containing nano diamond and preparation method thereof
CN109888234B (en) Composite active material, lithium ion battery composite anode material, lithium ion battery anode, lithium ion battery, preparation method and application
CN101414694A (en) Technology for manufacturing electric core of lithium ion power battery
CN113161157B (en) Silicon-based composite anode active material, silicon-based composite anode, and preparation method and application thereof
CN108448056A (en) A kind of preparation method of high-energy density anode pole piece and its lithium ion battery
CN107221639A (en) A kind of preparation method of lithium ion battery negative material

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20140917

Termination date: 20151029

EXPY Termination of patent right or utility model