CN108773839A - A kind of preparation method of high-pressure solid LiFePO4 - Google Patents

A kind of preparation method of high-pressure solid LiFePO4 Download PDF

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CN108773839A
CN108773839A CN201810611876.8A CN201810611876A CN108773839A CN 108773839 A CN108773839 A CN 108773839A CN 201810611876 A CN201810611876 A CN 201810611876A CN 108773839 A CN108773839 A CN 108773839A
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方嘉城
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Hubei Wanrun New Energy Technology Co Ltd
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    • C01B25/00Phosphorus; Compounds thereof
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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
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    • 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
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Abstract

The present invention discloses a kind of preparation method of high-pressure solid LiFePO4.By ferrous oxalate and lithium phosphate according to molar ratio 1:1 mixing, by adding water for ball milling and sand milling, is spray-dried, obtained dry powder through oversintering, obtains primary sintered material under an inert atmosphere;Ferric phosphate and glucose is added in primary sintered material, and the ferric phosphate of addition and the molar ratio of the lithium phosphate of step (1) addition are 2:1, then by adding water for ball milling and sand milling, obtain the material that grain size is 314nm, material is spray-dried to obtain moisture less than the dry powder that 2%, grain size is 1.5 microns, obtained dry powder is under an inert atmosphere through oversintering, and obtained dry powder is under an inert atmosphere through oversintering, obtain double sintering material, it is crushed, sieved in constant temperature and humidity room, except after iron, being filled with nitrogen, then vacuumize packaging again.The method of the present invention is simple, at low cost, and obtained LiFePO4 compacted density is high, good electrical property.

Description

A kind of preparation method of high-pressure solid LiFePO4
Technical field
The present invention relates to a kind of preparation methods of high-pressure solid LiFePO4, belong to anode material of lithium battery technical field.
Background technology
LiFePO4 is a kind of new type lithium ion battery electrode material.Its main feature is that discharge capacity is big, and it is cheap, it is nontoxic Property, do not cause environmental pollution.Just competitively realize industrialization production in countries in the world.But its tap density is low, influences capacitance.It is main The production method wanted is high temperature solid phase synthesis, and product index is more stable.The performance of lithium ion battery depends primarily on positive and negative Pole material, LiFePO4 are the things just occurred in recent years as the positive electrode of lithium ion battery, and domestic-developed goes out large capacity phosphorus Sour lithium iron battery is in July, 2005.Its security performance with cycle life be other materials can not compared with, these are also exactly dynamic The most important technical indicator of power battery.The 1C charge-discharge cycle service life is up to 2000 times.Single battery overcharged voltage 30V does not burn, and punctures It does not explode.Lithium iron phosphate positive material makes high capacity lithium ion battery and is more easy to be used in series.To meet the frequent charge and discharge of electric vehicle The needs of electricity.Have many advantages, such as it is nontoxic, pollution-free, have a safety feature, raw material sources are extensive, cheap, long lifespan is new The ideal positive electrode of generation lithium ion battery.
But the adjustment with country to new-energy automobile subsidy policy, the requirement to LiFePO 4 material is higher and higher, Requirement especially to the compacted density of LiFePO4 is higher and higher, and the > 2.3g/mL from before rise 2.35g/mL till now, And > 2.4g/mL or higher can be promoted later, the requirement simultaneously for the gram volume of 0.1C is maintained above 156mAh.
Invention content
In view of this, the present invention provides a kind of preparation method of high-pressure solid LiFePO4, method is simple, at low cost, and Obtained LiFePO4 compacted density is high, good electrical property, is prepared with ferric phosphate by the LiFePO4 prepared with ferrous oxalate LiFePO4 it is compound, combine the cycle of LiFePO4 and the advantage of low temperature performance well and phosphoric acid of ferrous oxalate preparation The good advantage of iron standby electrochemical performances of lithium iron phosphate, while avoiding ferrous oxalate and prepare LiFePO4 and releasing ammonia Disadvantage, the feature of environmental protection is good, and avoids using raw materials such as lithium carbonates, reduces cost, and by double sintering, it is close to improve compacting Degree does not influence electrical property further through compound, and finally obtained product compacted density is more than 2.45g/mL, and 0.1C is for the first time Discharge capacity is more than 157mAh/g, and the capacity attenuation rate that 0.5C recycles 500 times is less than 15%.
The present invention solves above-mentioned technical problem by following technological means:
A kind of preparation method of high-pressure solid LiFePO4, is following steps:
(1) by ferrous oxalate and lithium phosphate according to molar ratio 1:1 mixing, by adding water for ball milling and sand milling, obtaining grain size is Material is spray-dried to obtain moisture less than the dry powder that 2%, grain size is 1-3 microns, is obtained by the material of 450-480nm Dry powder obtains primary sintered material under an inert atmosphere through oversintering, and sintering total time is 12-15 hour, is sintered and is divided into three sections, the One section is warming-up section, and material is 3-5 hours in the warming-up section residence time, and second segment is soaking zone, and material is when soaking zone stops Between be 5-8 hour, the temperature of soaking zone is 720-750 DEG C, and third section is temperature descending section, and material is 2-4 in the temperature descending section residence time Hour, it is cooled to 80 DEG C of dischargings of temperature of charge <;
(2) ferric phosphate and glucose, ferric phosphate and the step (1) of addition is added in the primary sintered material for obtaining step (1) The molar ratio of the lithium phosphate of addition is 2:1, then through and adding water for ball milling and sand milling, obtains the material that grain size is 300-320nm, it will Material is spray-dried to obtain moisture less than the dry powder that 2%, grain size is 1-3 microns, and obtained dry powder passes through under an inert atmosphere Oversintering, obtained dry powder through oversintering, obtain double sintering material under an inert atmosphere, and sintering total time is 21-23 hours, is burnt Knot is divided into three sections, and first segment is warming-up section, and material is 6-8 hours in the warming-up section residence time, and second segment is soaking zone, and material exists The soaking zone residence time is 10-12 hours, and the temperature of soaking zone is 760-770 DEG C, and third section is temperature descending section, and material is in temperature descending section Residence time is 3-5 hours, is cooled to 50 DEG C of dischargings of temperature of charge <;
(3) the cooling material for obtaining step (2) is crushed in constant temperature and humidity room, is sieved, except after iron, being filled with nitrogen Then gas vacuumizes packaging again.
In the step (1) by ball milling and after being sanded, the solid content of material is 40-41%, spray drying into wind-warm syndrome Degree is 180-200 DEG C, and residence time of the material in spray dryer is 6-10S, and the inert atmosphere is nitrogen, in nitrogen Oxygen content is less than 5ppm, is passed through inert atmosphere and so that the furnace pressure in sintering furnace is 1.05-1.1 atmospheric pressure, material is in saggar Interior charging thickness is 10-12cm.
The weight for the glucose being added in the step (2) is the 14-15% of ferric phosphate weight, passes through ball in step (2) After mill and sand milling, the solid content of material is 30-35%, and the inlet air temperature of spray drying is 180-200 DEG C, and material is being spray-dried Residence time in machine is 6-10S, and the inert atmosphere is nitrogen, and the oxygen content in nitrogen is less than 5ppm, is passed through indifferent gas Atmosphere so that the furnace pressure in sintering furnace is 1.05-1.1 atmospheric pressure, and charging thickness of the material in saggar is 5-8cm.
Temperature is 10-15 DEG C in constant temperature and humidity room in the step (3), and relative humidity≤10% is crushed to the grain of material Diameter is 1-1.5 micron, and when screening crosses 200 mesh and sieves.
The purity of step (1) the mesoxalic acid ferrous iron is more than 99.5%, and granularity is 2-3 microns, BET 6-8m2/ g, mistake 150 mesh sieve, and tap density is more than 1.5g/mL, and impurity content is less than 100ppm.
The iron phosphorus ratio of ferric phosphate is 0.98-0.985 in the step (2), and granularity is 1-3 microns, tap density 0.6- 0.7g/mL, specific surface area 7-10m2/g。
This patent first passes through ferrous oxalate and is carried out once with lithium phosphate using lithium phosphate, ferrous oxalate and ferric phosphate as raw material Sintering, then ferric phosphate is added, remaining lithium is reacted completely, by the compound and double sintering of the two, improves compacted density, Phosphoric acid prepared by the cycle of LiFePO4 and the advantage of low temperature performance well and ferric phosphate prepared in combination with ferrous oxalate The good advantage of iron lithium electrochemical performance, while avoiding ferrous oxalate and preparing the shortcomings that LiFePO4 releases ammonia, the feature of environmental protection It is good, and avoid using raw materials such as lithium carbonates, cost is reduced, and by double sintering, improve compacted density, further through multiple It closes, electrical property is not influenced, finally obtained product compacted density is more than 2.45g/mL, and discharge capacity is more than 0.1C for the first time The capacity attenuation rate that 157mAh/g, 0.5C recycle 500 times is less than 15%.
The beneficial effects of the invention are as follows:Method is simple, at low cost, and obtained LiFePO4 compacted density is high, electrical property It is good.
Specific implementation mode
Below with reference to specific embodiment, the present invention is described in detail, a kind of high-pressure solid LiFePO4 of the present embodiment Preparation method, be following steps:
(1) by ferrous oxalate and lithium phosphate according to molar ratio 1:1 mixing, by adding water for ball milling and sand milling, obtaining grain size is Material is spray-dried to obtain moisture less than the dry powder that 2%, grain size is 1-3 microns, is obtained by the material of 450-480nm Dry powder obtains primary sintered material under an inert atmosphere through oversintering, and sintering total time is 12-15 hour, is sintered and is divided into three sections, the One section is warming-up section, and material is 3-5 hours in the warming-up section residence time, and second segment is soaking zone, and material is when soaking zone stops Between be 5-8 hour, the temperature of soaking zone is 720-750 DEG C, and third section is temperature descending section, and material is 2-4 in the temperature descending section residence time Hour, it is cooled to 80 DEG C of dischargings of temperature of charge <;
(2) ferric phosphate and glucose, ferric phosphate and the step (1) of addition is added in the primary sintered material for obtaining step (1) The molar ratio of the lithium phosphate of addition is 2:1, then through and adding water for ball milling and sand milling, obtains the material that grain size is 300-320nm, it will Material is spray-dried to obtain moisture less than the dry powder that 2%, grain size is 1-3 microns, and obtained dry powder passes through under an inert atmosphere Oversintering, obtained dry powder through oversintering, obtain double sintering material under an inert atmosphere, and sintering total time is 21-23 hours, is burnt Knot is divided into three sections, and first segment is warming-up section, and material is 6-8 hours in the warming-up section residence time, and second segment is soaking zone, and material exists The soaking zone residence time is 10-12 hours, and the temperature of soaking zone is 760-770 DEG C, and third section is temperature descending section, and material is in temperature descending section Residence time is 3-5 hours, is cooled to 50 DEG C of dischargings of temperature of charge <;
(3) the cooling material for obtaining step (2) is crushed in constant temperature and humidity room, is sieved, except after iron, being filled with nitrogen Then gas vacuumizes packaging again.
In the step (1) by ball milling and after being sanded, the solid content of material is 40-41%, spray drying into wind-warm syndrome Degree is 180-200 DEG C, and residence time of the material in spray dryer is 6-10S, and the inert atmosphere is nitrogen, in nitrogen Oxygen content is less than 5ppm, is passed through inert atmosphere and so that the furnace pressure in sintering furnace is 1.05-1.1 atmospheric pressure, material is in saggar Interior charging thickness is 10-12cm.
The weight for the glucose being added in the step (2) is the 14-15% of ferric phosphate weight, passes through ball in step (2) After mill and sand milling, the solid content of material is 30-35%, and the inlet air temperature of spray drying is 180-200 DEG C, and material is being spray-dried Residence time in machine is 6-10S, and the inert atmosphere is nitrogen, and the oxygen content in nitrogen is less than 5ppm, is passed through indifferent gas Atmosphere so that the furnace pressure in sintering furnace is 1.05-1.1 atmospheric pressure, and charging thickness of the material in saggar is 5-8cm.
Temperature is 10-15 DEG C in constant temperature and humidity room in the step (3), and relative humidity≤10% is crushed to the grain of material Diameter is 1-1.5 micron, and when screening crosses 200 mesh and sieves.
The purity of step (1) the mesoxalic acid ferrous iron is more than 99.5%, and granularity is 2-3 microns, BET 6-8m2/ g, mistake 150 mesh sieve, and tap density is more than 1.5g/mL, and impurity content is less than 100ppm.
The iron phosphorus ratio of ferric phosphate is 0.98-0.985 in the step (2), and granularity is 1-3 microns, tap density 0.6- 0.7g/mL, specific surface area 7-10m2/g。
Embodiment 1
A kind of preparation method of high-pressure solid LiFePO4, is following steps:
(1) by ferrous oxalate and lithium phosphate according to molar ratio 1:1 mixing, by adding water for ball milling and sand milling, obtaining grain size is Material is spray-dried to obtain moisture less than 2%, grain size as 2.1 microns of dry powder, obtained dry powder by the material of 465nm Under an inert atmosphere through oversintering, primary sintered material is obtained, sintering total time is 14 hours, and sintering is divided into three sections, and first segment is Warming-up section, material are 4 hours in the warming-up section residence time, and second segment is soaking zone, and material is 8 small in the soaking zone residence time When, the temperature of soaking zone is 745 DEG C, and third section is temperature descending section, and material is 2 hours in the temperature descending section residence time, is cooled to material 80 DEG C of dischargings of temperature <;
(2) ferric phosphate and glucose, ferric phosphate and the step (1) of addition is added in the primary sintered material for obtaining step (1) The molar ratio of the lithium phosphate of addition is 2:1, then by adding water for ball milling and sand milling, the material that grain size is 314nm is obtained, by material It is spray-dried to obtain moisture less than the dry powder that 2%, grain size is 1.5 microns, obtained dry powder is under an inert atmosphere through burning Knot, obtained dry powder through oversintering, obtain double sintering material under an inert atmosphere, and sintering total time is 22 hours, and sintering is divided into Three sections, first segment is warming-up section, and material is 7 hours in the warming-up section residence time, and second segment is soaking zone, and material stops in soaking zone It is 11 hours to stay the time, and the temperature of soaking zone is 766 DEG C, and third section is temperature descending section, and material is 4 small in the temperature descending section residence time When, it is cooled to 50 DEG C of dischargings of temperature of charge <;
(3) the cooling material for obtaining step (2) is crushed in constant temperature and humidity room, is sieved, except after iron, being filled with nitrogen Then gas vacuumizes packaging again.
In the step (1) by ball milling and after being sanded, the solid content of material is 40.5%, the inlet air temperature of spray drying It it is 195 DEG C, residence time of the material in spray dryer is 9S, and the inert atmosphere is nitrogen, the oxygen content in nitrogen Less than 5ppm, it is passed through inert atmosphere and so that the furnace pressure in sintering furnace is 1.08 atmospheric pressure, charging thickness of the material in saggar For 11cm.
The weight for the glucose being added in the step (2) is the 14.5% of ferric phosphate weight, passes through ball milling in step (2) After sand milling, the solid content of material is 31%, and the inlet air temperature of spray drying is 188 DEG C, and material stops in spray dryer It is 9S to stay the time, and the inert atmosphere is nitrogen, and the oxygen content in nitrogen is less than 5ppm, is passed through inert atmosphere and makes sintering furnace Interior furnace pressure is 1.09 atmospheric pressure, and charging thickness of the material in saggar is 7cm.
Temperature is 13 DEG C in constant temperature and humidity room in the step (3), relative humidity≤10%, and the grain size for being crushed to material is 1.25 microns, when screening, crosses 200 mesh sieve.
The purity of step (1) the mesoxalic acid ferrous iron is more than 99.5%, and granularity is 2.1 microns, BET 7.2m2/ g, mistake 150 mesh sieve, and tap density is more than 1.5g/mL, and impurity content is less than 100ppm.
The iron phosphorus ratio of ferric phosphate is 0.981 in the step (2), and granularity is 1.5 microns, tap density 0.66g/mL, Specific surface area is 9.2m2/g。
Finally obtained product index is as follows:
Embodiment 2
A kind of preparation method of high-pressure solid LiFePO4, is following steps:
(1) by ferrous oxalate and lithium phosphate according to molar ratio 1:1 mixing, by adding water for ball milling and sand milling, obtaining grain size is Material is spray-dried to obtain moisture less than 2%, grain size as 1.9 microns of dry powder, obtained dry powder by the material of 465nm Under an inert atmosphere through oversintering, primary sintered material is obtained, sintering total time is 13 hours, and sintering is divided into three sections, and first segment is Warming-up section, material are 3 hours in the warming-up section residence time, and second segment is soaking zone, and material is 6 small in the soaking zone residence time When, the temperature of soaking zone is 745 DEG C, and third section is temperature descending section, and material is 4 hours in the temperature descending section residence time, is cooled to material 80 DEG C of dischargings of temperature <;
(2) ferric phosphate and glucose, ferric phosphate and the step (1) of addition is added in the primary sintered material for obtaining step (1) The molar ratio of the lithium phosphate of addition is 2:1, then by adding water for ball milling and sand milling, the material that grain size is 315nm is obtained, by material It is spray-dried to obtain moisture less than the dry powder that 2%, grain size is 2.5 microns, obtained dry powder is under an inert atmosphere through burning Knot, obtained dry powder through oversintering, obtain double sintering material under an inert atmosphere, and sintering total time is 22 hours, and sintering is divided into Three sections, first segment is warming-up section, and material is 7 hours in the warming-up section residence time, and second segment is soaking zone, and material stops in soaking zone It is 12 hours to stay the time, and the temperature of soaking zone is 760 DEG C, and third section is temperature descending section, and material is 3 small in the temperature descending section residence time When, it is cooled to 50 DEG C of dischargings of temperature of charge <;
(3) the cooling material for obtaining step (2) is crushed in constant temperature and humidity room, is sieved, except after iron, being filled with nitrogen Then gas vacuumizes packaging again.
In the step (1) by ball milling and after being sanded, the solid content of material is 40.3%, the inlet air temperature of spray drying It it is 189 DEG C, residence time of the material in spray dryer is 8S, and the inert atmosphere is nitrogen, the oxygen content in nitrogen Less than 5ppm, it is passed through inert atmosphere and so that the furnace pressure in sintering furnace is 1.06 atmospheric pressure, charging thickness of the material in saggar For 11.5cm.
The weight for the glucose being added in the step (2) is the 14.2% of ferric phosphate weight, passes through ball milling in step (2) After sand milling, the solid content of material is 33%, and the inlet air temperature of spray drying is 185 DEG C, and material stops in spray dryer It is 8S to stay the time, and the inert atmosphere is nitrogen, and the oxygen content in nitrogen is less than 5ppm, is passed through inert atmosphere and makes sintering furnace Interior furnace pressure is 1.08 atmospheric pressure, and charging thickness of the material in saggar is 7.5cm.
Temperature is 13 DEG C in constant temperature and humidity room in the step (3), relative humidity≤10%, and the grain size for being crushed to material is 1.35 microns, when screening, crosses 200 mesh sieve.
The purity of step (1) the mesoxalic acid ferrous iron is more than 99.5%, and granularity is 2.6 microns, BET 7.2m2/ g, mistake 150 mesh sieve, and tap density is more than 1.5g/mL, and impurity content is less than 100ppm.
The iron phosphorus ratio of ferric phosphate is 0.984 in the step (2), and granularity is 1.3 microns, tap density 0.66g/mL, Specific surface area is 9.5m2/g。
Finally obtained product index is as follows:
Embodiment 3
A kind of preparation method of high-pressure solid LiFePO4, is following steps:
(1) by ferrous oxalate and lithium phosphate according to molar ratio 1:1 mixing, by adding water for ball milling and sand milling, obtaining grain size is Material is spray-dried to obtain moisture less than 2%, grain size as 2.8 microns of dry powder, obtained dry powder by the material of 460nm Under an inert atmosphere through oversintering, primary sintered material is obtained, sintering total time is 13 hours, and sintering is divided into three sections, and first segment is Warming-up section, material are 4 hours in the warming-up section residence time, and second segment is soaking zone, and material is 6 small in the soaking zone residence time When, the temperature of soaking zone is 725 DEG C, and third section is temperature descending section, and material is 3 hours in the temperature descending section residence time, is cooled to material 80 DEG C of dischargings of temperature <;
(2) ferric phosphate and glucose, ferric phosphate and the step (1) of addition is added in the primary sintered material for obtaining step (1) The molar ratio of the lithium phosphate of addition is 2:1, then by adding water for ball milling and sand milling, the material that grain size is 305nm is obtained, by material It is spray-dried to obtain moisture less than the dry powder that 2%, grain size is 1.9 microns, obtained dry powder is under an inert atmosphere through burning Knot, obtained dry powder through oversintering, obtain double sintering material under an inert atmosphere, and sintering total time is 21.5 hours, sintering point It it is three sections, first segment is warming-up section, and material is 7.5 hours in the warming-up section residence time, and second segment is soaking zone, and material is being kept the temperature The section residence time is 11 hours, and the temperature of soaking zone is 766 DEG C, and third section is temperature descending section, and material is 3 in the temperature descending section residence time Hour, it is cooled to 50 DEG C of dischargings of temperature of charge <;
(3) the cooling material for obtaining step (2) is crushed in constant temperature and humidity room, is sieved, except after iron, being filled with nitrogen Then gas vacuumizes packaging again.
In the step (1) by ball milling and after being sanded, the solid content of material is 40.7%, the inlet air temperature of spray drying It it is 189 DEG C, residence time of the material in spray dryer is 9S, and the inert atmosphere is nitrogen, the oxygen content in nitrogen Less than 5ppm, it is passed through inert atmosphere and so that the furnace pressure in sintering furnace is 1.09 atmospheric pressure, charging thickness of the material in saggar For 11.5cm.
The weight for the glucose being added in the step (2) is the 14.9% of ferric phosphate weight, passes through ball milling in step (2) After sand milling, the solid content of material is 33%, and the inlet air temperature of spray drying is 195 DEG C, and material stops in spray dryer It is 8S to stay the time, and the inert atmosphere is nitrogen, and the oxygen content in nitrogen is less than 5ppm, is passed through inert atmosphere and makes sintering furnace Interior furnace pressure is 1.09 atmospheric pressure, and charging thickness of the material in saggar is 8cm.
Temperature is 13 DEG C in constant temperature and humidity room in the step (3), relative humidity≤10%, and the grain size for being crushed to material is 1.2 microns, when screening, crosses 200 mesh sieve.
The purity of step (1) the mesoxalic acid ferrous iron is more than 99.5%, and granularity is 2.8 microns, BET 7.2m2/ g, mistake 150 mesh sieve, and tap density is more than 1.5g/mL, and impurity content is less than 100ppm.
The iron phosphorus ratio of ferric phosphate is 0.982 in the step (2), and granularity is 1.8 microns, tap density 0.68g/mL, Specific surface area is 9.5m2/g。
Finally obtained product index is as follows:
Embodiment 4
A kind of preparation method of high-pressure solid LiFePO4, is following steps:
(1) by ferrous oxalate and lithium phosphate according to molar ratio 1:1 mixing, by adding water for ball milling and sand milling, obtaining grain size is Material is spray-dried to obtain moisture less than 2%, grain size as 1.9 microns of dry powder, obtained dry powder by the material of 455nm Under an inert atmosphere through oversintering, primary sintered material is obtained, sintering total time is 14 hours, and sintering is divided into three sections, and first segment is Warming-up section, material are 4.5 hours in the warming-up section residence time, and second segment is soaking zone, and material is 7.5 in the soaking zone residence time Hour, the temperature of soaking zone is 748 DEG C, and third section is temperature descending section, and material is 2 hours in the temperature descending section residence time, is cooled to object 80 DEG C of dischargings of material temperature degree <;
(2) ferric phosphate and glucose, ferric phosphate and the step (1) of addition is added in the primary sintered material for obtaining step (1) The molar ratio of the lithium phosphate of addition is 2:1, then by adding water for ball milling and sand milling, the material that grain size is 315nm is obtained, by material It is spray-dried to obtain moisture less than the dry powder that 2%, grain size is 1.8 microns, obtained dry powder is under an inert atmosphere through burning Knot, obtained dry powder through oversintering, obtain double sintering material under an inert atmosphere, and sintering total time is 22.5 hours, sintering point It it is three sections, first segment is warming-up section, and material is 7.5 hours in the warming-up section residence time, and second segment is soaking zone, and material is being kept the temperature The section residence time is 11.5 hours, and the temperature of soaking zone is 769 DEG C, and third section is temperature descending section, and material is in the temperature descending section residence time It is 3.5 hours, is cooled to 50 DEG C of dischargings of temperature of charge <;
(3) the cooling material for obtaining step (2) is crushed in constant temperature and humidity room, is sieved, except after iron, being filled with nitrogen Then gas vacuumizes packaging again.
In the step (1) by ball milling and after being sanded, the solid content of material is 40.5%, the inlet air temperature of spray drying It it is 189 DEG C, residence time of the material in spray dryer is 9S, and the inert atmosphere is nitrogen, the oxygen content in nitrogen Less than 5ppm, it is passed through inert atmosphere and so that the furnace pressure in sintering furnace is 1.085 atmospheric pressure, charging thickness of the material in saggar For 12cm.
The weight for the glucose being added in the step (2) is the 14.1% of ferric phosphate weight, passes through ball milling in step (2) After sand milling, the solid content of material is 33%, and the inlet air temperature of spray drying is 189 DEG C, and material stops in spray dryer It is 9S to stay the time, and the inert atmosphere is nitrogen, and the oxygen content in nitrogen is less than 5ppm, is passed through inert atmosphere and makes sintering furnace Interior furnace pressure is 1.06 atmospheric pressure, and charging thickness of the material in saggar is 7.2cm.
Temperature is 14 DEG C in constant temperature and humidity room in the step (3), relative humidity≤10%, and the grain size for being crushed to material is 1.45 microns, when screening, crosses 200 mesh sieve.
The purity of step (1) the mesoxalic acid ferrous iron is more than 99.5%, and granularity is 2.8 microns, BET 7.8m2/ g, mistake 150 mesh sieve, and tap density is more than 1.5g/mL, and impurity content is less than 100ppm.
The iron phosphorus ratio of ferric phosphate is 0.983 in the step (2), and granularity is 2.5 microns, tap density 0.67g/mL, Specific surface area is 8.2m2/g。
Finally obtained product index is as follows:
Finally illustrate, the above examples are only used to illustrate the technical scheme of the present invention and are not limiting, although with reference to compared with Good embodiment describes the invention in detail, it will be understood by those of ordinary skill in the art that, it can be to the skill of the present invention Art scheme is modified or replaced equivalently, and without departing from the objective and range of technical solution of the present invention, should all be covered at this In the right of invention.

Claims (6)

1. a kind of preparation method of high-pressure solid LiFePO4, which is characterized in that be following steps:
(1) by ferrous oxalate and lithium phosphate according to molar ratio 1:1 mixing, by adding water for ball milling and sand milling, it is 450- to obtain grain size Material is spray-dried to obtain moisture less than 2%, grain size as 1-3 microns of dry powder, obtained dry powder by the material of 480nm Under an inert atmosphere through oversintering, primary sintered material is obtained, sintering total time is 12-15 hours, and sintering is divided into three sections, first segment For warming-up section, material is 3-5 hours in the warming-up section residence time, and second segment is soaking zone, and material is in the soaking zone residence time 5-8 hours, the temperature of soaking zone was 720-750 DEG C, and third section is temperature descending section, and material is 2-4 hours in the temperature descending section residence time, It is cooled to 80 DEG C of dischargings of temperature of charge <;
(2) ferric phosphate and glucose is added in the primary sintered material for obtaining step (1), and ferric phosphate and the step (1) of addition are added Lithium phosphate molar ratio be 2:1, then by adding water for ball milling and sand milling, the material that grain size is 300-320nm is obtained, by material It is spray-dried to obtain moisture less than the dry powder that 2%, grain size is 1-3 microns, obtained dry powder is under an inert atmosphere through burning Knot, obtained dry powder through oversintering, obtain double sintering material under an inert atmosphere, and sintering total time is 21-23 hours, sintering point It it is three sections, first segment is warming-up section, and material is 6-8 hours in the warming-up section residence time, and second segment is soaking zone, and material is being kept the temperature The section residence time is 10-12 hours, and the temperature of soaking zone is 760-770 DEG C, and third section is temperature descending section, and material is stopped in temperature descending section Time is 3-5 hours, is cooled to 50 DEG C of dischargings of temperature of charge <;
(3) the cooling material for obtaining step (2) is crushed in constant temperature and humidity room, is sieved, except after iron, being filled with nitrogen, so Vacuumize packaging again afterwards.
2. a kind of preparation method of high-pressure solid LiFePO4 according to claim 1, it is characterised in that:The step (1) Middle by ball milling and after being sanded, the solid content of material is 40-41%, and the inlet air temperature of spray drying is 180-200 DEG C, and material exists Residence time in spray dryer is 6-10S, and the inert atmosphere is nitrogen, and the oxygen content in nitrogen is less than 5ppm, leads to Enter inert atmosphere and so that the furnace pressure in sintering furnace is 1.05-1.1 atmospheric pressure, charging thickness of the material in saggar is 10- 12cm。
3. a kind of preparation method of high-pressure solid LiFePO4 according to claim 1, it is characterised in that:The step (2) The weight of the glucose of middle addition is the 14-15% of ferric phosphate weight, and in step (2) by ball milling and after being sanded, material is consolidated Content is 30-35%, and the inlet air temperature of spray drying is 180-200 DEG C, and residence time of the material in spray dryer is 6- 10S, the inert atmosphere are nitrogen, and the oxygen content in nitrogen is less than 5ppm, are passed through inert atmosphere and make stove in sintering furnace Pressure is 1.05-1.1 atmospheric pressure, and charging thickness of the material in saggar is 5-8cm.
4. a kind of preparation method of high-pressure solid LiFePO4 according to claim 1, it is characterised in that:The step (3) Temperature is 10-15 DEG C in middle constant temperature and humidity room, relative humidity≤10%, and the grain size for being crushed to material is 1-1.5 microns, when screening Cross 200 mesh sieve.
5. a kind of preparation method of high-pressure solid LiFePO4 according to claim 1, it is characterised in that:The step (1) The purity of mesoxalic acid ferrous iron is more than 99.5%, and granularity is 2-3 microns, BET 6-8m2/ g, crosses 150 mesh sieve, and tap density is big In 1.5g/mL, impurity content is less than 100ppm.
6. a kind of preparation method of high-pressure solid LiFePO4 according to claim 1, it is characterised in that:The step (2) The iron phosphorus ratio of middle ferric phosphate is 0.98-0.985, and granularity is 1-3 microns, tap density 0.6-0.7g/mL, specific surface area 7- 10m2/g。
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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109650366A (en) * 2018-11-22 2019-04-19 湖北融通高科先进材料有限公司 A kind of LiFePO4 and preparation method thereof
CN109921003A (en) * 2019-04-18 2019-06-21 王东升 A kind of preparation method of high-pressure solid LiFePO4
CN111392705A (en) * 2020-02-25 2020-07-10 东莞东阳光科研发有限公司 Preparation method of high-compaction lithium iron phosphate
CN113745503A (en) * 2021-08-04 2021-12-03 北京泰丰先行新能源科技有限公司 Preparation method of high-compaction lithium iron phosphate cathode material
CN114314547A (en) * 2021-12-23 2022-04-12 山东精工电子科技有限公司 High-compaction lithium iron phosphate material, sintering method and preparation method
CN117088352A (en) * 2023-10-20 2023-11-21 宁德时代新能源科技股份有限公司 Preparation method of lithium iron phosphate, positive electrode active material, positive electrode plate, battery and electricity utilization device

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101332987A (en) * 2008-07-31 2008-12-31 福建师范大学 Method for preparing positive electrode material of LiFePO4 by phosphorous acid or salt thereof
WO2010051749A1 (en) * 2008-11-05 2010-05-14 Byd Company Limited Method of preparing cathode active material and method of forming lithium secondary battery
JP2010530124A (en) * 2007-09-25 2010-09-02 ビーワイディー カンパニー リミテッド Method for preparing positive electrode material for lithium secondary battery
CN103441269A (en) * 2013-08-05 2013-12-11 北大先行科技产业有限公司 Lithium/carbon pyrophosphate coated lithium iron phosphate composite and preparation method thereof
CN103985862A (en) * 2014-04-14 2014-08-13 江苏中欧材料研究院有限公司 Synthetic method of high vibration compaction high specific capacity phosphatic positive pole material
CN104319380A (en) * 2014-11-13 2015-01-28 四川浩普瑞新能源材料有限公司 Composite LiFePO4/C cathode material for lithium ion battery and preparation method for composite LiFePO4/C cathode material
CN103730657B (en) * 2014-01-09 2016-05-18 北大先行科技产业有限公司 A kind of preparation method of lithium phosphate/carbon-coated lithium iron phosphate composite

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010530124A (en) * 2007-09-25 2010-09-02 ビーワイディー カンパニー リミテッド Method for preparing positive electrode material for lithium secondary battery
CN101332987A (en) * 2008-07-31 2008-12-31 福建师范大学 Method for preparing positive electrode material of LiFePO4 by phosphorous acid or salt thereof
WO2010051749A1 (en) * 2008-11-05 2010-05-14 Byd Company Limited Method of preparing cathode active material and method of forming lithium secondary battery
CN103441269A (en) * 2013-08-05 2013-12-11 北大先行科技产业有限公司 Lithium/carbon pyrophosphate coated lithium iron phosphate composite and preparation method thereof
CN103730657B (en) * 2014-01-09 2016-05-18 北大先行科技产业有限公司 A kind of preparation method of lithium phosphate/carbon-coated lithium iron phosphate composite
CN103985862A (en) * 2014-04-14 2014-08-13 江苏中欧材料研究院有限公司 Synthetic method of high vibration compaction high specific capacity phosphatic positive pole material
CN104319380A (en) * 2014-11-13 2015-01-28 四川浩普瑞新能源材料有限公司 Composite LiFePO4/C cathode material for lithium ion battery and preparation method for composite LiFePO4/C cathode material

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109650366A (en) * 2018-11-22 2019-04-19 湖北融通高科先进材料有限公司 A kind of LiFePO4 and preparation method thereof
CN109921003A (en) * 2019-04-18 2019-06-21 王东升 A kind of preparation method of high-pressure solid LiFePO4
CN111392705A (en) * 2020-02-25 2020-07-10 东莞东阳光科研发有限公司 Preparation method of high-compaction lithium iron phosphate
CN111392705B (en) * 2020-02-25 2021-11-12 东莞东阳光科研发有限公司 Preparation method of high-compaction lithium iron phosphate
CN113745503A (en) * 2021-08-04 2021-12-03 北京泰丰先行新能源科技有限公司 Preparation method of high-compaction lithium iron phosphate cathode material
CN114314547A (en) * 2021-12-23 2022-04-12 山东精工电子科技有限公司 High-compaction lithium iron phosphate material, sintering method and preparation method
CN117088352A (en) * 2023-10-20 2023-11-21 宁德时代新能源科技股份有限公司 Preparation method of lithium iron phosphate, positive electrode active material, positive electrode plate, battery and electricity utilization device

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