CN109728258A - A kind of dispersing technology of lithium iron phosphate positive material - Google Patents
A kind of dispersing technology of lithium iron phosphate positive material Download PDFInfo
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- CN109728258A CN109728258A CN201711035683.4A CN201711035683A CN109728258A CN 109728258 A CN109728258 A CN 109728258A CN 201711035683 A CN201711035683 A CN 201711035683A CN 109728258 A CN109728258 A CN 109728258A
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- iron phosphate
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- 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 belongs to technical field of lithium ion, more particularly to a kind of lithium iron phosphate positive material dispersing technology containing graphene conductive agent, purpose be based on improve ferric phosphate lithium cell specific energy and cycle performance simultaneously, effectively shorten homogenate dispersing technology time, save industrial production cost.It is characterized by: it includes the steps that baking, obtains conductive agent, electrocondution slurry is made, conductive rubber is made, lithium iron phosphate cathode slurry is made.The present invention is sufficiently merged by the way that conductive rubber is made in conductive agent, without shelving, is substantially reduced the homogenate process time, is reduced cost and reduce the wasting of resources.And by four dispersions, including dispersing agent is added and changes graphene surface activity, using the extreme shearing force continuous shear stress of ultra micron pulverizer, manufactured slurry is uniformly dispersed, and stability is good.
Description
Technical field
The invention belongs to technical field of lithium ion, and in particular to a kind of LiFePO4 containing graphene conductive agent is just
Pole material dispersing technology.
Background technique
Ferric phosphate lithium cell is the battery made using lithium iron phosphate positive material, and ferric phosphate lithium cell has high magnification,
High circulation service life, the advantage of high safety performance and low cost and no pollution to the environment are widely used in electric automobiles.With
Domestic electric vehicle industry development and country the landing of new energy electric motor vehicle subsidy policy is implemented, as electric vehicle heart
Lithium ion battery receive more and more attention and test;And dispatch a joint document according to Ministry of Industry and Information, the Department of Science and Technology, the Ministry of Finance " about
Tissue declares the notice of 2012 annual new-energy automobile industrial technology innovation engineering projects ", it is distinctly claimed the ratio energy of battery cell
Amount reaches 150Wh/kg or more, and the specific energy to the year two thousand twenty battery cell reaches 300Wh/kg;Therefore research has higher energy
The battery of density and excellent cycling performance by be all battery Corporation R & Ds emphasis.
LiFePO 4 material possesses rhombic system olivine structural for nickel-cobalt-manganese ternary material, and lithium ion is de-
After out/insertion, crystal structure hardly happens rearrangement, to possess high security performance and cycle life, becomes electronic automobile-used
The mainstay material of battery.But its own conductivity is poor, lithium ion diffusion is slow, and general conductive agent is added and is difficult to have its capacity
Effect plays;And nano-level conducting agent large specific surface area, activity are high, traditional homogenate technique can not effectively disperse, the group of be easy to causeing
Poly- accumulation, manufactured battery with two side terminals not can guarantee, and are assembled into mould group and cause security risk during charge-discharge test.
The two dimensional crystal for only one layer of atomic thickness that graphene is constituted as carbon atom is that discovery conduction is led up to now
A kind of strongest novel nano-material of hot property.It is added in lithium iron phosphate positive material as conductive agent, can effectively be mentioned
The diffusion transport of high-lithium ion reduces the internal resistance of cell, so that the capacity and cycle performance of ferric phosphate lithium cell are increased substantially, it is right
The raising of battery specific energy and the promotion of electric vehicle course continuation mileage have the improvement of essence.
Traditional lithium iron phosphate cathode slurry preparation process time is long, and nano-level conducting agent dispersion effect is poor, equipment energy consumption
Greatly, it causes cost to waste industrialized production, is unfavorable for the environmentally protective concept of electric vehicle production.
Summary of the invention
The purpose of the present invention is simultaneously, effectively shorten homogenate based on the specific energy and cycle performance for improving ferric phosphate lithium cell
The time of dispersing technology saves industrial production cost.
The present invention is implemented as follows:
A kind of dispersing technology of lithium iron phosphate positive material, specifically comprises the following steps:
Step 1: by LiFePO 4 material, conductive black (Super P-Li), graphite powder (KS-6), graphene respectively-
Vacuum bakeout 8h under the conditions of 0.095MPa pressure, 120 DEG C of ± 5 DEG C of temperature.Dispersing agent (Hypermer KD-1), Kynoar
Vacuum bakeout 3h under the conditions of -0.095MPa pressure, 80 DEG C of ± 5 DEG C of temperature respectively.After baking, be naturally cooling to 50 DEG C with
Lower use.
Step 2: conductive black (Super P-Li), graphite powder (KS-6), graphene are added by the mass ratio of 1:1:1
In ball mill mixing tank, conductive black (Super P-Li), graphite powder (KS-6), graphene gross mass and middle or small porcelain ball it is total
Mass ratio is 1:1, wherein middle porcelain bulb diameter 40mm, small porcelain bulb diameter 20mm, the mass ratio of middle or small porcelain ball are 1:1, ball mill mixing
Tank uses 30r/min revolving speed, disperses 30min~60min, obtains conductive agent.
Step 3: conductive agent (including conductive black (Super P-Li), graphite powder after the completion of above-mentioned steps two are dispersed
(KS-6), graphene), dispersing agent and N-Methyl pyrrolidone be added in ultra micron pulverizer in 4.5:0.5:95 ratio;Ultra micro
Grain pulverizer uses the revolving speed of 2000r/min~2500r/min, and 10 microns~30 microns of gap carries out high-speed circulating dispersion
Electrocondution slurry is made in 30min~60min.
Step 4: the ratio of electrocondution slurry in mass ratio 2%~5% made of Kynoar and above-mentioned steps three is added
Enter in planetary dispersion machine, is carried out using the revolving speed of revolution 15r/min~35r/min, rotation 1500r/min~3500r/min
Vacuum dispersion, jitter time are 3h~6h, and conductive rubber is made after the completion of dispersion, takes out from planetary dispersion machine.
Step 5: lithium iron phosphate positive material being added in the conductive rubber of above-mentioned preparation, and the mass ratio of addition is 30%
~70%, it is put into another planetary dispersion machine, uses revolution revolving speed 15r/min~35r/min, rotation revolving speed 1000r/min
~3500r/min is dispersed, jitter time 1h~4h.10% N-Methyl pyrrolidone is added after the completion of dispersion, uses public affairs
Walk around fast 15r/min~35r/min, rotation revolving speed 1000r/min~3500r/min, carries out vacuum and disperses 0.5h~3h, thus
The lithium iron phosphate cathode slurry of solid content and viscosity needed for being made.
The above-mentioned Kynoar PVDF used is U.S. Solef5130.Graphene is the preparation of graphite oxide reduction method
Graphene.Dispersing agent uses the big Hypermer KD-1 of Britain's standing grain.
The beneficial effects of the present invention are:
SP, KS-6, graphene are tentatively mixed by using ball mill mixing method first, three kinds of conductive agents is made divide for the first time
Dissipate mixing.
Secondly conductive agent, the dispersing agent by tentatively dispersing are added into N-methyl pyrrolidones, is crushed using ultra micron
Machine carries out high speed shear with the gap of micron level, and finely dispersed conductive agent slurry is made.
Then third time dispersion is carried out using planetary dispersion machine by the way that Kynoar binder is added, after the completion of dispersion
Obtain conductive rubber.
Lithium iron phosphate positive material is added later, by the solid content of control slurry, carries out efficient high viscosity dispersion, from
And merge material of main part sufficiently with conductive agent, binder.
It ultimately joining N-methyl pyrrolidones and adjusts slurry viscosity, lithium iron phosphate cathode slurry dispersion effect obtained is good,
Modest viscosity, coating performance are excellent.
Conventional commercial production method needs the dispersion Kynoar of 4~5h, and shelve 12h~carry out afterwards for 24 hours using.
And conductive agent is directly added into solvent and carries out planetary dispersion, nanoscale conductive agent can not be uniformly dispersed.
The invention patent sufficiently merges by the way that conductive rubber is made in conductive agent, without shelving, substantially reduces homogenate work
The skill time reduces cost and reduces the wasting of resources.And by four dispersions, including dispersing agent change graphene surface is added and lives
Property, using the extreme shearing force continuous shear stress of ultra micron pulverizer, manufactured slurry is uniformly dispersed, and stability is good.
Detailed description of the invention
Fig. 1 is to use 5Ah soft-package battery made of a kind of dispersing technology of lithium iron phosphate positive material of the invention and make
It is compared with the discharge capacity of the conventional batteries without containing graphene conductive agent, wherein the curve of top is using present invention process system
At the discharge capacity of battery;
Fig. 2 is to use 5Ah soft-package battery made of a kind of dispersing technology of lithium iron phosphate positive material of the invention and make
With 1000 discharge capacitances comparison of the conventional batteries without containing graphene conductive agent, wherein top curve is using this
Discharge capacity of the cell conservation rate is made in invented technology.
Specific embodiment
The present invention is described further with reference to the accompanying drawings and examples.
A kind of lithium iron phosphate positive material dispersing technology containing graphene conductive agent, by LiFePO 4 material, conductive charcoal
Black (Super P-Li), graphite powder (KS-6), graphene carry out 120 DEG C ± 5 DEG C, 8h, vacuum bakeout.Hypermer KD-1 gathers
Vinylidene carries out 80 DEG C ± 5 DEG C, 3h, vacuum bakeout.Baking reaches required temperature with temperature and starts timing, after baking,
Be naturally cooling to 50 DEG C it is used below.By Super P-Li, it is mixed that ball milling is added in the ratio of KS-6, graphene 1:1:1 in mass ratio
In batch can, medium and small porcelain ball (diameter 40mm, 20mm) (ratio 1:1) is added by material ratio (1:1), uses 30r/min revolving speed, dispersion
30min.By the conductive agent after the completion of above-mentioned dispersion, Hypermer KD-1, N-Methyl pyrrolidone 4.5:0.5:95 in mass ratio
Ratio be added in ultra micron pulverizer, using 2000r/min, 10 microns of gap carries out high-speed circulating and disperses 30min, is made
Electrocondution slurry.The ratio of Kynoar and above-mentioned manufactured electrocondution slurry 3:97 in proportion are added in planetary dispersion machine,
Vacuum dispersion is carried out using the revolving speed of revolution 35r/min, rotation 3500r/min, jitter time 3h is made after the completion of dispersion and leads
Electric colloid.Lithium iron phosphate positive material is added in the conductive rubber of above-mentioned preparation, using revolution revolving speed 25r/min, is walked around certainly
Fast 1000r/min is dispersed, jitter time 2h, additional proportion 6:4.A certain amount of N- methylpyrrole is added after the completion of dispersion
Alkanone is carried out vacuum and is dispersed 30min using revolution revolving speed 35r/min, rotation revolving speed 3500r/min, to contain admittedly needed for being made
The lithium iron phosphate cathode slurry of amount and viscosity.
The present invention is first by lithium iron phosphate positive material PT30 (Tianjin Sitelan Energy Science Co., Ltd) graphene (north
The self-control of capital Wanyuan Industrial Co., Ltd) conductive black (Super P-Li) graphite powder (KS-6)
(TIMCAL company).Use 120 DEG C of progress 8h bakings of vacuum drying oven (Dongguan Ke Rui mechanical & electronic equipment corporation, Ltd).It is poly-
Vinylidene (U.S. Solef5130), Hypermer KD-1 (Britain's standing grain is big) carry out 80 DEG C of 3h bakings in vacuum oven.Baking
Reach required temperature with temperature and start timing, after baking, be naturally cooling to 50 DEG C it is used below.By Super P-Li, KS-
6, graphene is added in ball mill mixing tank in the ratio of 1:1:1, by the medium and small porcelain ball of material ratio (1:1) addition (diameter 40mm,
20mm) (ratio 1:1) disperses 30min using 30r/min revolving speed.By the conductive agent after the completion of above-mentioned dispersion, Hypermer
KD-1, N-Methyl pyrrolidone in proportion 4.5:0.5:95 ratio be added ultra micron pulverizer (Japan increase good fortune industry strain formula meeting
Society) in, using 2000r/min, 10 microns of gap carries out high-speed circulating and disperses 30min, electrocondution slurry is made.By polyvinylidene fluoride
The ratio of alkene and above-mentioned manufactured electrocondution slurry 3:97 in proportion are added in planetary dispersion machine that (the sharp electromechanical equipment of Dongguan section is limited
Company), vacuum dispersion, jitter time 3h, after the completion of dispersion are carried out using the revolving speed of revolution 35r/min, rotation 3500r/min
Conductive rubber is made.Lithium iron phosphate positive material PT3 is added in the conductive rubber of above-mentioned preparation, uses revolution revolving speed 25r/
Min, rotation revolving speed 1000r/min are dispersed, jitter time 2h, additional proportion 6:4.It is added after the completion of dispersion a certain amount of
N-Methyl pyrrolidone is carried out vacuum and is dispersed 30min, vacuum degree using revolution revolving speed 35r/min, rotation revolving speed 3500r/min
(- 0.095MPa), it is 40%~50% that obtained anode sizing agent contains admittedly, viscosity 3000mpa~8000mpa;Use 150 mesh screens
It is sieved, final lithium iron phosphate cathode slurry dispersion consistency obtained is excellent, and finished battery is functional.
The present invention is using 5Ah soft-package battery made of the dispersing technology and uses the conventional electricity without containing graphene conductive agent
Pond performance comparison is as shown in table 1, and discharge capacity compares as shown in Figure 1:
The comparison of 1 battery performance of table
It is recycled and is compared using 5Ah soft-package battery made of the dispersing technology and conventional 5Ah soft-package battery, 1C charge and discharge
For 1000 capacity retention ratios 99.5%, conventional batteries capacity retention ratio is 91.6%.Cyclic curve is as shown in Figure 2.
Implementation method of the invention is explained in detail above in conjunction with embodiment, but the present invention is not limited to above-mentioned realities
Example is applied, it within the knowledge of a person skilled in the art, can also be without departing from the purpose of the present invention
Various changes can be made.The content that description in the present invention is not described in detail can use the prior art.
Claims (2)
1. a kind of dispersing technology of lithium iron phosphate positive material, specifically comprises the following steps:
Step 1: by LiFePO 4 material, conductive black, graphite powder, graphene respectively in -0.095MPa pressure, 120 DEG C ± 5
Vacuum bakeout 8h under the conditions of DEG C temperature;Dispersing agent, Kynoar are respectively in -0.095MPa pressure, 80 DEG C of ± 5 DEG C of temperature conditions
Lower vacuum bakeout 3h;After baking, be naturally cooling to 50 DEG C it is used below;
Step 2: conductive black, graphite powder, graphene are added in ball mill mixing tank by the mass ratio of 1:1:1, conductive black,
The total mass ratio of graphite powder, the gross mass of graphene and middle or small porcelain ball is 1:1, wherein middle porcelain bulb diameter 40mm, small porcelain bulb diameter
20mm, the mass ratio of middle or small porcelain ball are 1:1, and ball mill mixing tank uses 30r/min revolving speed, disperse 30min~60min, are led
Electric agent;
Step 3: conductive agent, dispersing agent and N-Methyl pyrrolidone after the completion of above-mentioned steps two are dispersed press 4.5:0.5:95
Ratio is added in ultra micron pulverizer;Ultra micron pulverizer uses the revolving speed of 2000r/min~2500r/min, 10 microns of gap
It~30 microns, carries out high-speed circulating and disperses 30min~60min, electrocondution slurry is made;
Step 4: row is added in the ratio of electrocondution slurry in mass ratio 2%~5% made of Kynoar and above-mentioned steps three
In planetary dispersion machine, vacuum is carried out using the revolving speed of revolution 15r/min~35r/min, rotation 1500r/min~3500r/min
Dispersion, jitter time are 3h~6h, and conductive rubber is made after the completion of dispersion, takes out from planetary dispersion machine;
Step 5: lithium iron phosphate positive material being added in the conductive rubber of above-mentioned preparation, and the mass ratio of addition is 30%~
70%, be put into another planetary dispersion machine, using revolution revolving speed 15r/min~35r/min, rotation revolving speed 1000r/min~
3500r/min is dispersed, jitter time 1h~4h;10% N-Methyl pyrrolidone is added after the completion of dispersion, uses revolution
Revolving speed 15r/min~35r/min, rotation revolving speed 1000r/min~3500r/min carry out vacuum and disperse 0.5h~3h, to make
The lithium iron phosphate cathode slurry of solid content and viscosity needed for obtaining.
2. the dispersing technology of lithium iron phosphate positive material according to claim 1, it is characterised in that: it is above-mentioned use it is poly- partially
Vinyl fluoride is U.S. Solef5130;Graphene is the graphene of graphite oxide reduction method preparation;Dispersing agent is big using Britain's standing grain
Hypermer KD-1。
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Publication number | Priority date | Publication date | Assignee | Title |
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CN111834619A (en) * | 2020-06-19 | 2020-10-27 | 湖北亿纬动力有限公司 | Positive electrode slurry and preparation method and application thereof |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101710619A (en) * | 2009-12-14 | 2010-05-19 | 重庆大学 | Electrode plate for lithium ion battery and manufacturing method thereof |
CN102544502A (en) * | 2010-12-09 | 2012-07-04 | 中国科学院宁波材料技术与工程研究所 | Anode and cathode conductive additive for secondary lithium battery, method for preparing conductive additive, and method for preparing secondary lithium battery |
CN102956894A (en) * | 2012-10-31 | 2013-03-06 | 内蒙古三信实业有限公司 | Preparation method of lithium iron phosphate material anode sheet |
CN103886932A (en) * | 2014-03-25 | 2014-06-25 | 深圳市纳米港有限公司 | Carbon nano tube electric conduction slurry and preparation method and application thereof |
CN104538627A (en) * | 2015-01-05 | 2015-04-22 | 天津市捷威动力工业有限公司 | Preparation method of nanometer lithium iron phosphate anode slurry |
CN105406070A (en) * | 2015-12-18 | 2016-03-16 | 山东精工电子科技有限公司 | Preparation method of lithium ion battery positive pole size |
-
2017
- 2017-10-30 CN CN201711035683.4A patent/CN109728258B/en active Active
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101710619A (en) * | 2009-12-14 | 2010-05-19 | 重庆大学 | Electrode plate for lithium ion battery and manufacturing method thereof |
CN102544502A (en) * | 2010-12-09 | 2012-07-04 | 中国科学院宁波材料技术与工程研究所 | Anode and cathode conductive additive for secondary lithium battery, method for preparing conductive additive, and method for preparing secondary lithium battery |
CN102956894A (en) * | 2012-10-31 | 2013-03-06 | 内蒙古三信实业有限公司 | Preparation method of lithium iron phosphate material anode sheet |
CN103886932A (en) * | 2014-03-25 | 2014-06-25 | 深圳市纳米港有限公司 | Carbon nano tube electric conduction slurry and preparation method and application thereof |
CN104538627A (en) * | 2015-01-05 | 2015-04-22 | 天津市捷威动力工业有限公司 | Preparation method of nanometer lithium iron phosphate anode slurry |
CN105406070A (en) * | 2015-12-18 | 2016-03-16 | 山东精工电子科技有限公司 | Preparation method of lithium ion battery positive pole size |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111834619A (en) * | 2020-06-19 | 2020-10-27 | 湖北亿纬动力有限公司 | Positive electrode slurry and preparation method and application thereof |
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Effective date of registration: 20221013 Address after: No.8, Huancheng Road, Fengcheng Town, Tianzhu County, Qiandongnan Miao and Dong Autonomous Prefecture, Guizhou 556600 Patentee after: Wu Weiyue Address before: 100176 Aerospace Science Park, No. 6, Jinxiu Street, Beijing Economic and Technological Development Zone, Daxing District, Beijing Patentee before: BEIJING WANYUAN INDUSTRY Co.,Ltd. |