CN114105115B - Production method and application of ferric phosphate and lithium iron phosphate - Google Patents
Production method and application of ferric phosphate and lithium iron phosphate Download PDFInfo
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- CN114105115B CN114105115B CN202111387889.XA CN202111387889A CN114105115B CN 114105115 B CN114105115 B CN 114105115B CN 202111387889 A CN202111387889 A CN 202111387889A CN 114105115 B CN114105115 B CN 114105115B
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B25/00—Phosphorus; Compounds thereof
- C01B25/16—Oxyacids of phosphorus; Salts thereof
- C01B25/26—Phosphates
- C01B25/37—Phosphates of heavy metals
- C01B25/375—Phosphates of heavy metals of iron
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B25/00—Phosphorus; Compounds thereof
- C01B25/16—Oxyacids of phosphorus; Salts thereof
- C01B25/26—Phosphates
- C01B25/45—Phosphates containing plural metal, or metal and ammonium
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/05—Accumulators with non-aqueous electrolyte
- H01M10/052—Li-accumulators
- H01M10/0525—Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/58—Selection 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
- H01M4/5825—Oxygenated metallic salts or polyanionic structures, e.g. borates, phosphates, silicates, olivines
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2004/00—Particle morphology
- C01P2004/01—Particle morphology depicted by an image
- C01P2004/03—Particle morphology depicted by an image obtained by SEM
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M2004/026—Electrodes composed of, or comprising, active material characterised by the polarity
- H01M2004/028—Positive electrodes
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
Abstract
The invention discloses a production method and application of ferric phosphate and lithium iron phosphate; the production method of the ferric phosphate comprises the following steps: (1) Mixing ferrous chloride, hydrogen peroxide and hydrochloric acid in water for reaction to obtain ferric chloride solution; (2) Mixing ferric chloride solution with phytic acid and phosphate in water for reaction to obtain ferric phosphate precursor liquid; (3) And filtering, drying and calcining the ferric phosphate precursor liquid to obtain ferric phosphate. According to the invention, the low-temperature performance of the prepared lithium iron phosphate is obviously improved through the matched use of the phytic acid and the phosphate. Meanwhile, the method directly prepares the ferric chloride solution and directly uses the ferric chloride solution for producing ferric phosphate, so that compared with the traditional method using ferric chloride powder raw materials, the method saves the processes of drying ferric chloride and preparing slurry, and greatly saves the production cost.
Description
Technical Field
The invention relates to the technical field of batteries, in particular to a production method and application of ferric phosphate and lithium iron phosphate.
Background
With the continuous decrease of petroleum resources and the increasing pollution of automobile exhaust to the environment worldwide, hybrid Electric Vehicles (HEV) and Electric Vehicles (EV) have become attractive as alternatives to fuel-driven automobiles in the future, and mobile power systems are one of the key components of electric automobiles. Therefore, high performance (i.e., high specific energy, long life, safety), low cost, and environmentally friendly batteries will be an important and hot spot for the development of the mobile power industry. Lithium ion batteries are a new generation of green high-energy rechargeable batteries developed to meet this demand. It has the outstanding advantages of high voltage, small volume, light weight, high specific energy, no memory effect, no pollution, small self-discharge, long service life, etc.
The Padhi et al report that the lithium iron phosphate material with the olivine structure can be used as the positive electrode material of the lithium ion battery in 1997, and the lithium iron phosphate material is one of the positive electrode materials with the highest potential at present because of the advantages of low price, environmental protection, no pollution, no moisture absorption, good thermal stability and the like, and is concerned by vast scientific research institutions and commercial institutions. In recent years, a lot of research, development and improvement are carried out on the material by many scientific researchers, and the material is gradually commercialized and applied to the markets of high-capacity, high-power and long-service-life lithium ion batteries. Lithium iron phosphate represents a future development of positive electrode materials for power cells.
At present, a solid-phase synthesis method is a main method for preparing commercial lithium iron phosphate, but the defects of high cost of ferrous iron source, difficult preservation, large particle size of synthesized lithium iron phosphate, poor uniformity and the like are difficult to meet the requirements of a power type lithium ion battery. Therefore, ferric iron with low cost and stable performance is adopted to replace ferrous iron as an iron source, and synthetic ferric phosphate is adopted as a precursor to prepare the lithium iron phosphate. The synthesis method of the synthesized ferric phosphate generally comprises the steps of reacting ferric trichloride or ferric nitrate solution with phosphoric acid, and then decomposing and volatilizing hydrogen chloride or nitric acid at high temperature to obtain the ferric phosphate.
However, lithium iron phosphate has low electron conductivity and ion diffusion rate at room temperature of 10 due to its inherent characteristics (respectively -8 -10 -10 S/cm and 10 -12 -10 -14 cm 2 S) results in a significant degradation of the charge and discharge properties of the lithium iron phosphate as a positive electrode material at low temperatures.
Disclosure of Invention
The invention aims to provide a production method and application of ferric phosphate and lithium iron phosphate, which can obviously improve the low-temperature performance of the ferric phosphate and the lithium iron phosphate.
In order to achieve the above purpose, the present invention adopts the technical scheme that:
the invention discloses a production method of ferric phosphate, which comprises the following steps:
(1) Mixing ferrous chloride, hydrogen peroxide and hydrochloric acid in water for reaction to obtain ferric chloride solution;
(2) Mixing the ferric chloride solution obtained in the step (1) with phytic acid and phosphate in water for reaction to obtain ferric phosphate precursor liquid;
(3) And (3) filtering, drying and calcining the ferric phosphate precursor liquid obtained in the step (2) to obtain ferric phosphate.
As a preferred embodiment, in the step (2), the phosphate includes, but is not limited to, H 3 PO 4 、(NH 4 ) 3 PO 4 、(NH 4 ) 2 HPO 4 、(NH 4 )H 2 PO 4 One or more of the following.
As a preferable technical scheme, in the step (2), the molar ratio of the phytic acid to the phosphate is 1:999-999:1.
In the step (2), alkali liquor is added into the reaction system to control the pH value to be less than 7.
As a preferred technical scheme, the alkali liquor comprises one or a mixture of more than one of ammonia water, sodium hydroxide solution, sodium acetate solution and ammonium acetate solution.
In the preferred embodiment, in the step (2), the reaction is a normal temperature reaction.
In the step (3), alkali liquor is added for dilution before the filtration of the ferric phosphate precursor liquid or alkali liquor is added for washing during the filtration of the ferric phosphate precursor liquid.
In the step (3), the calcination temperature is 100-800 ℃.
The invention also discloses the ferric phosphate produced by the production method.
The invention also discloses a production method of the lithium iron phosphate, which comprises the steps of mixing the iron phosphate with lithium salt and a carbon source in water, and then drying and calcining to obtain the lithium iron phosphate.
The invention also discloses application of the lithium iron phosphate produced by the production method in a positive electrode material of a lithium ion battery.
The invention has the beneficial effects that:
the invention utilizes phytic acid and phosphate to form phosphate groups as a phosphorus source, synthesizes ferric phosphate with ferric chloride, and then prepares lithium iron phosphate by taking the ferric phosphate as a precursor. According to the invention, through the matching use of the phytic acid and the phosphate, the low-temperature performance of the prepared lithium iron phosphate is obviously improved.
Meanwhile, the method directly prepares the ferric chloride solution and directly uses the ferric chloride solution for producing ferric phosphate, so that compared with the traditional method using ferric chloride powder raw materials, the method saves the processes of drying ferric chloride and preparing slurry, and greatly saves the production cost.
Drawings
FIG. 1 is a process flow diagram for preparing iron phosphate from ferrous chloride;
FIG. 2 is a block diagram of an apparatus for producing ferric chloride from ferrous chloride;
FIG. 3 is a block diagram of an apparatus for producing ferric phosphate from ferric chloride;
FIG. 4 is a process flow diagram of the preparation of lithium iron phosphate from iron phosphate;
FIG. 5 is a block diagram of an apparatus for preparing lithium iron phosphate from ferric phosphate;
FIG. 6 is an SEM image of lithium iron phosphate of example 1;
FIG. 7 is a graph of specific 0.2C discharge capacity at-20℃for a button cell made of lithium iron phosphate of example 1;
FIG. 8 is a graph of specific 0.2C discharge capacity at-20℃for a button cell made of lithium iron phosphate of example 2;
fig. 9 is a graph showing the specific discharge capacity of the lithium iron phosphate of comparative example 1 at-20C at 0.2C.
Detailed Description
The present invention will be further described with reference to the accompanying drawings, in order to make the objects, technical solutions and advantages of the present invention more apparent.
Example 1
As shown in fig. 1 to 5, lithium iron phosphate was prepared by the following steps:
(1) Adding ferrous chloride, hydrogen peroxide and hydrochloric acid into an iron chloride reaction kettle, mixing, stirring and reacting, pumping the obtained iron chloride solution into an iron chloride tank for temporary storage.
(2) The ferric chloride solution obtained in the step (1) is treated with phytic acid and (NH) 4 )H 2 PO 4 Adding ammonia water into the reaction kettle, and controlling phytic acid and (NH) 4 )H 2 PO 4 The molar ratio of (2) is 1:99, controlling the addition amount of ammonia water to adjust the pH value of the system to about 2, and then mixing and stirring the mixture in a reaction kettle at normal temperature for reaction for 1 hour; and pumping the reaction slurry into an aging kettle for aging for 1 hour, and pumping the obtained ferric phosphate precursor liquid into a finished product tank for temporary storage.
(3) Adding ammonia water into the ferric phosphate precursor liquid obtained in the step (2) for dilution, then pumping the diluted ferric phosphate precursor liquid into a plate-frame filter for filtering, and washing the diluted ferric phosphate precursor liquid to be neutral; and then the wet material is added into a flash dryer for flash drying, and then is added into a rotary kiln for calcination at 400 ℃ to obtain the ferric phosphate.
(4) Adding the ferric phosphate, lithium carbonate and glucose obtained in the step (3) into a dispersion kettle filled with water for full dispersion, adding the slurry into a grinding tank for grinding, and then performing spray drying by spray drying equipment, sintering by a sintering furnace and crushing by an air flow crusher to obtain the lithium iron phosphate.
Example 2
As shown in fig. 1 to 5, lithium iron phosphate was prepared by the following steps:
(1) Adding ferrous chloride, hydrogen peroxide and hydrochloric acid into an iron chloride reaction kettle, mixing, stirring and reacting, pumping the obtained iron chloride solution into an iron chloride tank for temporary storage.
(2) Mixing ferric chloride solution obtained in the step (1), phytic acid and H 3 PO 4 Adding ammonia water into the reaction kettle, and controlling phytic acid and H 3 PO 4 The molar ratio of (2) is 1:99, controlling the addition amount of ammonia water to adjust the pH value of the system to about 2, and then mixing and stirring the mixture in a reaction kettle at normal temperature for reaction for 1 hour; and pumping the reaction slurry into an aging kettle for aging for 1 hour, and pumping the obtained ferric phosphate precursor liquid into a finished product tank for temporary storage.
(3) Adding ammonia water into the ferric phosphate precursor liquid obtained in the step (2) for dilution, then pumping the diluted ferric phosphate precursor liquid into a plate-frame filter for filtering, and washing the diluted ferric phosphate precursor liquid to be neutral; and then the wet material is added into a flash dryer for flash drying, and then is added into a rotary kiln for calcination at 400 ℃ to obtain the ferric phosphate.
(4) Adding the ferric phosphate, lithium carbonate and glucose obtained in the step (3) into a dispersion kettle filled with water for full dispersion, adding the slurry into a grinding tank for grinding, and then performing spray drying by spray drying equipment, sintering by a sintering furnace and crushing by an air flow crusher to obtain the lithium iron phosphate.
Comparative example 1
The lithium iron phosphate is prepared by the following steps:
(1) Adding ferrous chloride, hydrogen peroxide and hydrochloric acid into an iron chloride reaction kettle, mixing, stirring and reacting, pumping the obtained iron chloride solution into an iron chloride tank for temporary storage.
(2) Ferric chloride solution H obtained in the step (1) 3 PO 4 Adding ammonia water into a reaction kettle, controlling the adding amount of the ammonia water to adjust the pH value of the system to about 2, and then mixing and stirring the ammonia water in the reaction kettle at normal temperature for reaction for 1 hour; and pumping the reaction slurry into an aging kettle for aging for 1 hour, and pumping the obtained ferric phosphate precursor liquid into a finished product tank for temporary storage.
(3) Adding ammonia water into the ferric phosphate precursor liquid obtained in the step (2) for dilution, then pumping the diluted ferric phosphate precursor liquid into a plate-frame filter for filtering, and washing the diluted ferric phosphate precursor liquid to be neutral; and then the wet material is added into a flash dryer for flash drying, and then is added into a rotary kiln for calcination at 400 ℃ to obtain the ferric phosphate.
(4) Adding the ferric phosphate, lithium carbonate and glucose obtained in the step (3) into a dispersion kettle filled with water for full dispersion, adding the slurry into a grinding tank for grinding, and then performing spray drying by spray drying equipment, sintering by a sintering furnace and crushing by an air flow crusher to obtain the lithium iron phosphate.
Fig. 6 is an SEM image of the lithium iron phosphate prepared in example 1, and it can be seen from the figure that the lithium iron phosphate prepared in example 1 has a uniform particle size.
The lithium iron phosphate prepared in example 1, example 2 and comparative example 1 were used as positive electrode materials, respectively, and positive electrode sheets were prepared first: and (3) carrying out positive electrode material proportioning on the positive electrode material, the binder and the conductive agent to obtain uniform positive electrode slurry, and uniformly coating the prepared positive electrode slurry on a positive electrode current collector aluminum foil to obtain a positive electrode plate. And winding the positive plate, the negative plate and the diaphragm to prepare a lithium ion battery core, and injecting electrolyte to prepare the button cell.
FIG. 7 is a graph showing that the specific discharge capacity of the button cell made of the lithium iron phosphate of example 1 at-20 ℃ is 0.2C, and the specific discharge capacity of the button cell at-20 ℃ can reach 80mAh/g.
FIG. 8 is a graph showing the specific discharge capacity of the button cell made of the lithium iron phosphate of example 2 at-20 ℃ of 0.2C, wherein the specific discharge capacity of the button cell at-20 ℃ can reach 83mAh/g.
FIG. 9 is a graph showing the specific discharge capacity of the lithium iron phosphate of comparative example 1 at-20℃of 0.2C, which can reach 54mAh/g.
As can be seen from the comparison, compared with the comparison example using only phosphoric acid, the low-temperature performance of the prepared lithium iron phosphate is obviously improved through the matched use of the phytic acid and the phosphate.
The foregoing has shown and described the basic principles, principal features and advantages of the invention. It will be understood by those skilled in the art that the present invention is not limited to the embodiments described above, and that the above embodiments and descriptions are merely illustrative of the principles of the present invention, and various changes and modifications may be made without departing from the spirit and scope of the invention, which is defined in the appended claims. The scope of the invention is defined by the appended claims and equivalents thereof.
Claims (10)
1. A production method of ferric phosphate is characterized in that: the method comprises the following steps:
(1) Mixing ferrous chloride, hydrogen peroxide and hydrochloric acid in water for reaction to obtain ferric chloride solution;
(2) Mixing the ferric chloride solution obtained in the step (1) with phytic acid and phosphate in water for reaction to obtain ferric phosphate precursor liquid;
(3) Filtering, drying and calcining the ferric phosphate precursor liquid obtained in the step (2) to obtain ferric phosphate;
in the step (2), the molar ratio of the phytic acid to the phosphate is 1:999-1:99.
2. The method for producing iron phosphate according to claim 1, wherein: in step (2), the phosphate includes, but is not limited to, H 3 PO 4 、(NH 4 ) 3 PO 4 、(NH 4 ) 2 HPO 4 、(NH 4 )H 2 PO 4 One or more of the following.
3. The method for producing iron phosphate according to claim 1, wherein: in the step (2), alkali liquor is added into the reaction system, and the pH value is controlled to be less than 7.
4. A method for producing iron phosphate according to claim 3, wherein: the alkali liquor comprises one or a mixture of several of ammonia water, sodium hydroxide solution, sodium acetate solution and ammonium acetate solution.
5. The method for producing iron phosphate according to claim 1, wherein: in the step (2), the reaction is a normal temperature reaction.
6. The method for producing iron phosphate according to claim 1, wherein: in the step (3), alkali liquor is added for dilution before the filtration of the ferric phosphate precursor liquid or alkali liquor is added for washing during the filtration of the ferric phosphate precursor liquid.
7. The method for producing iron phosphate according to claim 1, wherein: in the step (3), the calcining temperature is 100-800 ℃.
8. Iron phosphate produced by the production method according to any one of claims 1 to 7.
9. A production method of lithium iron phosphate is characterized in that: mixing the iron phosphate according to claim 8 with lithium salt and carbon source in water, drying and calcining to obtain lithium iron phosphate.
10. The use of lithium iron phosphate produced by the production method of claim 9 in a positive electrode material of a lithium ion battery.
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| CN114506832A (en) * | 2022-03-08 | 2022-05-17 | 青岛九环新越新能源科技股份有限公司 | Zero-emission recycling production method of iron phosphate and lithium iron phosphate |
| CN114590788A (en) * | 2022-03-08 | 2022-06-07 | 青岛九环新越新能源科技股份有限公司 | Zero-emission recycling production method of lithium iron phosphate |
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