CN107204435A - A kind of moisture control technique of LiFePO4 - Google Patents

A kind of moisture control technique of LiFePO4 Download PDF

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Publication number
CN107204435A
CN107204435A CN201710416013.0A CN201710416013A CN107204435A CN 107204435 A CN107204435 A CN 107204435A CN 201710416013 A CN201710416013 A CN 201710416013A CN 107204435 A CN107204435 A CN 107204435A
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CN
China
Prior art keywords
lifepo4
compressed air
drying
control technique
gas
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.)
Pending
Application number
CN201710416013.0A
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Chinese (zh)
Inventor
孔令涌
刘其峰
陈杰
李意能
徐浩
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FOSHAN DYNANONIC Co Ltd
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FOSHAN DYNANONIC 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
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Priority to CN201710416013.0A priority Critical patent/CN107204435A/en
Publication of CN107204435A publication Critical patent/CN107204435A/en
Pending legal-status Critical Current

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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/13Electrodes 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
    • H01M4/58Selection 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
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

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  • Chemical & Material Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Abstract

The present invention provides a kind of moisture control technique of LiFePO4, comprises the following steps:Discharging:The LiFePO4 material come out from stove is sent directly into drying shed, overturning saggar by mechanical arm makes material enter pneumatic conveyer by changeover valve;Air-flow is conveyed:By the use of cold dry compressed air as carrier, LiFePO4 material is sent to storage tank from tank sending;Crush:By the use of the high temperature compressed air after heating as crushing and drying source of the gas, material is crushed and dried in airflow milling, the material after crushing is sieved into grading wheel;Packaging:Material after screening, which is entered, carries out gas solid separation in dedusting cabin, the material separated is packed into packaging system.LiFePO4 material is not contacted directly with surrounding air in the present invention, Gas grinding and drying are carried out using high temperature compressed air, make product moisture content < 500ppm, have the advantages that technique is simple, with short production cycle, cost is low, energy consumption is low, product water content stable.

Description

A kind of moisture control technique of LiFePO4
Technical field
The present invention relates to electrochemical material manufacturing technology field, and in particular to a kind of moisture control technique of LiFePO4.
Background technology
The water content of LiFePO 4 of anode material finished product directly affects the chemical property of battery, the factory of LiFePO4 Family all can strictly control the water content of LiFePO4 in process of production, typically require moisture within 500ppm.But Because LiFePO 4 powder particle is thin, specific surface area big, cause its water imbibition stronger.If in atmosphere open-assembly time it is slightly long or Ambient humidity is higher, and its moisture can exceed 1000ppm.In order to control the moisture of LiFePO4, the side that most producers take Formula is to increase drying process before packing, or in battery manufacturing process and slurry process before increase material roasting plant, There is producer that air-flow crushing, mixing, packaging process are placed in drying shed to or carried out under nitrogen atmosphere crushing packing, these sides There is time-consuming, power consumption, the problems such as environmental condition requires high in method.It is placed in using by air-flow crushing, mixing, packaging process in drying shed Technology be although easier to realize, process costs are relatively low, but exist and require high to environmental condition, and moisture control is unstable etc. Problem, easily causes moisture exceeded due to environmental change.Although carrying out crushing packing in nitrogen atmosphere can effectively control Product moisture content processed, but be due to that gas consumption is big in Crushing with Jet Mill, the low problem of nitrogen utilization rate will cause cost anxious Play rises, or even higher than increase drying process cost before packing, it is impossible to effectively reduce energy consumption.
The content of the invention
It is an object of the invention to provide a kind of moisture control technique of LiFePO4, LiFePO4 material is in process of production Do not contacted with surrounding air directly, and Gas grinding and drying are carried out using high temperature compressed air, make LiFePO4 product Moisture is qualified, has the advantages that technique is simple, with short production cycle, cost is low, energy consumption is low, product water content stable.
To achieve these goals, the technical solution adopted by the present invention is as follows:
A kind of moisture control technique of LiFePO4, comprises the following steps:
1) discharging:The LiFePO4 material come out from stove is sent directly into drying shed, overturning saggar by mechanical arm makes thing Material enters pneumatic conveyer by changeover valve.
2) air-flow is conveyed:By the use of cold dry compressed air as carrier, LiFePO4 material is sent from pneumatic conveyer To storage tank.
3) crush:Drying compressed air is heated using gas heater, the high temperature compressed air after heating is utilized As crushing and drying source of the gas, material is crushed and dried in airflow milling, the material after crushing is carried out into grading wheel Screening.
4) pack:Material after screening, which is entered, carries out gas solid separation in dedusting cabin, the material separated is directly entered Automatic packaging system is packed.
According to above scheme, the dew point of the cold dry compressed air is less than -20 DEG C.
According to above scheme, the dew point of the drying compressed air is less than -20 DEG C, and the temperature is 120~180 DEG C.
According to above scheme, the automatic packaging system is directly connected to dedusting cabin outlet, and pilot process is not directly and ring Border air is contacted.
LiFePO4 material is not contacted directly with surrounding air in process of production in the present invention, and material is touched The control of compressed air dew point less than -20 DEG C, it is possible to prevente effectively from material absorbs water in process of production;Crushing process makes simultaneously It is 120~180 DEG C with temperature and (is less than 120 degree, drying effect is bad;Higher than 180 degree, oxidation is serious) high temperature compressed air make For grinding source of the gas, there is drying function simultaneously in crushing process, product moisture content is further ensured that.
Produced, can be produced granularity under relatively low cost and energy consumption condition and conformed to using the technique of the present invention Summation moisture < 500ppm LiFePO4 product.
The beneficial effects of the invention are as follows:
1) process of the invention is brief, eliminates the drying, mixing and screening process of traditional processing technology, substantially reduces phosphoric acid The production cycle of iron lithium product;
2) it the present invention relates to equipment requirement low, simple to equipment need to only transform combination, gases used process is pressure Energy consumption can be effectively reduced after contracting air, no extra cost, and simplified process, great amount of cost is saved;
3) material in the present invention is prevented effectively from material water suction, used simultaneously in process of production without outside air is directly contacted High temperature compressed air is as grinding gas and drying source of the gas, under double insurance, and the product moisture content fluctuation of preparation is small, and quality is steady Qualitative increase.
Brief description of the drawings
Fig. 1 is the process flow diagram of the present invention.
In figure:1st, drying shed;2nd, mechanical arm;3rd, pneumatic conveyer;4th, airflow milling storage tank;5th, compressed air inlet pipe; 6th, gas heater;7th, airflow milling;8th, grading wheel;9th, dedusting cabin;10th, automatic packaging system.
Embodiment
Technical scheme is illustrated with embodiment below in conjunction with the accompanying drawings.
Embodiment 1, is shown in Fig. 1:
The present invention provides a kind of moisture control technique of LiFePO4, comprises the following steps (see Fig. 1):
1) discharging:The LiFePO4 material come out from stove is sent directly into drying shed 1, overturning saggar by mechanical arm 2 makes Material enters pneumatic conveyer 3 by changeover valve.
2) air-flow is conveyed:By the use of cold dry compressed air as carrier, LiFePO4 material is sent from pneumatic conveyer 3 To storage tank 4.
3) crush:Drying compressed air is entered in gas heater 6 by compressed air inlet pipe 5, is heated to 160 DEG C, by the use of high temperature compressed air as crushing and drying source of the gas, material is delivered in airflow milling 6, to material in airflow milling 7 Crushed and dried, the material after crushing is sieved into grading wheel 8;
4) pack:Material after screening, which is entered, carries out gas solid separation in dedusting cabin 9, the material separated is directly entered automatically Packaging system 10 is packed.
Further, the cold dry compressed air, the dew point of high temperature compressed air are below -20 DEG C;The automatic packaging System 10 is directly connected to the outlet of the dedusting cabin 9.
After testing, LiFePO4 product moisture content < 500ppm.
Embodiment 2:
Other steps are identical with implementing 1, and difference is step 3) in, drying compressed air, which is heated to after 120 DEG C, to be made To crush and drying source of the gas.
After testing, LiFePO4 product moisture content < 500ppm.
Embodiment 3:
Other steps are identical with implementing 1, and difference is step 3) in, drying compressed air, which is heated to after 180 DEG C, to be made To crush and drying source of the gas.
After testing, LiFePO4 product moisture content < 500ppm.
Above example is only used to illustrative and not limiting technical scheme, although above-described embodiment enters to the present invention Detailed description is gone, the person skilled of this area should be understood:The present invention can be modified or replaced on an equal basis, but Not departing from any modification and local replacement of spirit and scope of the invention all should cover in scope of the presently claimed invention.

Claims (4)

1. the moisture control technique of a kind of LiFePO4, it is characterised in that comprise the following steps:
1) discharging:The LiFePO4 material come out from stove is sent directly into drying shed, overturning saggar by mechanical arm makes thing Material enters pneumatic conveyer by changeover valve;
2) air-flow is conveyed:By the use of cold dry compressed air as carrier, LiFePO4 material is sent to storage from pneumatic conveyer In batch can;
3) crush:Drying compressed air is heated using gas heater, by the use of the high temperature compressed air after heating as Crush and drying source of the gas, material is crushed and dried in airflow milling, the material after crushing is sieved into grading wheel;
4) pack:Material after screening, which is entered, carries out gas solid separation in dedusting cabin, the material separated is directly entered automatically Packaging system is packed.
2. the moisture control technique of LiFePO4 according to claim 1, it is characterised in that the cold dry compressed air Dew point is less than -20 DEG C.
3. the moisture control technique of LiFePO4 according to claim 1, it is characterised in that the gas heater plus Hot temperature is 120~180 DEG C, and the dew point of the high temperature compressed air is less than -20 DEG C.
4. the moisture control technique of LiFePO4 according to claim 1, it is characterised in that the automatic packaging system is straight Dedusting cabin outlet is connected in succession.
CN201710416013.0A 2017-06-06 2017-06-06 A kind of moisture control technique of LiFePO4 Pending CN107204435A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710416013.0A CN107204435A (en) 2017-06-06 2017-06-06 A kind of moisture control technique of LiFePO4

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710416013.0A CN107204435A (en) 2017-06-06 2017-06-06 A kind of moisture control technique of LiFePO4

Publications (1)

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CN107204435A true CN107204435A (en) 2017-09-26

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110436431A (en) * 2019-06-29 2019-11-12 佛山市德方纳米科技有限公司 A kind of preparation method and lithium ion battery of lithium iron phosphate positive material

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105236377A (en) * 2015-08-28 2016-01-13 江苏南大紫金锂电智能装备有限公司 Water removal process of lithium iron phosphate
CN105742577A (en) * 2016-04-20 2016-07-06 绵阳流能粉体设备有限公司 Method and device for superfine grinding and drying of lithium iron phosphate in closed circulation of high-temperature drying gas
CN106129404A (en) * 2016-07-24 2016-11-16 合肥国轩电池材料有限公司 A kind of drying process of LiFePO4

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105236377A (en) * 2015-08-28 2016-01-13 江苏南大紫金锂电智能装备有限公司 Water removal process of lithium iron phosphate
CN105742577A (en) * 2016-04-20 2016-07-06 绵阳流能粉体设备有限公司 Method and device for superfine grinding and drying of lithium iron phosphate in closed circulation of high-temperature drying gas
CN106129404A (en) * 2016-07-24 2016-11-16 合肥国轩电池材料有限公司 A kind of drying process of LiFePO4

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110436431A (en) * 2019-06-29 2019-11-12 佛山市德方纳米科技有限公司 A kind of preparation method and lithium ion battery of lithium iron phosphate positive material
CN110436431B (en) * 2019-06-29 2021-11-02 佛山市德方纳米科技有限公司 Preparation method of lithium iron phosphate cathode material and lithium ion battery

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Application publication date: 20170926

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