[go: up one dir, main page]

CN107863530B - A method for preparing high-density lithium iron phosphate by using siderite - Google Patents

A method for preparing high-density lithium iron phosphate by using siderite Download PDF

Info

Publication number
CN107863530B
CN107863530B CN201711070611.3A CN201711070611A CN107863530B CN 107863530 B CN107863530 B CN 107863530B CN 201711070611 A CN201711070611 A CN 201711070611A CN 107863530 B CN107863530 B CN 107863530B
Authority
CN
China
Prior art keywords
iron
siderite
iron phosphate
lithium
solution
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.)
Active
Application number
CN201711070611.3A
Other languages
Chinese (zh)
Other versions
CN107863530A (en
Inventor
谷亦杰
秦文娟
陈蕴博
刘成全
王海峰
刘洪权
陈林
王萌
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shandong University of Science and Technology
Original Assignee
Shandong University of Science and Technology
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Shandong University of Science and Technology filed Critical Shandong University of Science and Technology
Priority to CN201711070611.3A priority Critical patent/CN107863530B/en
Publication of CN107863530A publication Critical patent/CN107863530A/en
Application granted granted Critical
Publication of CN107863530B publication Critical patent/CN107863530B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • 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
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B25/00Phosphorus; Compounds thereof
    • C01B25/16Oxyacids of phosphorus; Salts thereof
    • C01B25/26Phosphates
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B25/00Phosphorus; Compounds thereof
    • C01B25/16Oxyacids of phosphorus; Salts thereof
    • C01B25/26Phosphates
    • C01B25/37Phosphates of heavy metals
    • C01B25/375Phosphates of heavy metals of iron
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B25/00Phosphorus; Compounds thereof
    • C01B25/16Oxyacids of phosphorus; Salts thereof
    • C01B25/26Phosphates
    • C01B25/45Phosphates containing plural metal, or metal and ammonium
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/052Li-accumulators
    • H01M10/0525Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Materials Engineering (AREA)
  • Manufacturing & Machinery (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Battery Electrode And Active Subsutance (AREA)

Abstract

本发明公开了一种利用菱铁矿制备高密度磷酸铁锂的方法,它首先在菱铁矿中直接加入磷酸得到铁的溶液,铁的溶液与高分子共聚物P(DMDAAC‑AM)混合,在混合溶液中加入双氧水充分反应得磷酸铁锂前驱体二水磷酸铁,二水磷酸铁再与碳酸锂和葡萄糖混合烧结后得到磷酸铁锂。本发明利用的原料是菱铁矿,菱铁矿是一种分布比较广泛的矿物,可以作为铁矿石来提炼铁,用菱铁矿直接合成前驱体二水磷酸铁,不但省去了铁矿石提炼铁的耗能步骤,实现了锂离子电池正极材料从自然界直接获得的目的,而且菱铁矿相对于铁粉来说更容易与磷酸反应,提高了反应的可行性。

Figure 201711070611

The invention discloses a method for preparing high-density lithium iron phosphate by using siderite. First, phosphoric acid is directly added to siderite to obtain an iron solution, and the iron solution is mixed with polymer copolymer P (DMDAAC-AM), Hydrogen peroxide is added to the mixed solution to fully react to obtain iron phosphate dihydrate, a precursor of lithium iron phosphate, and the iron phosphate dihydrate is mixed with lithium carbonate and glucose to obtain lithium iron phosphate after sintering. The raw material used in the invention is siderite, which is a widely distributed mineral and can be used as iron ore to extract iron, and the precursor iron phosphate dihydrate is directly synthesized with siderite, which not only saves iron ore The energy-consuming step of extracting iron from stone realizes the purpose that the cathode material of lithium ion battery is directly obtained from nature, and siderite is easier to react with phosphoric acid than iron powder, which improves the feasibility of the reaction.

Figure 201711070611

Description

Method for preparing high-density lithium iron phosphate by adopting siderite
Technical Field
The invention belongs to the field of electrochemistry, and particularly relates to a method for preparing a lithium ion battery anode material by utilizing siderite.
Background
The lithium ion battery is a new generation of green high-energy battery with excellent performance, and has become one of the key points of the development of high and new technologies, and the synthesis method of lithium iron phosphate as the anode material of the lithium ion battery is the central importance in the development. The method for synthesizing the lithium iron phosphate battery by utilizing the siderite at present comprises the steps of dissolving the siderite by sulfuric acid, hydrochloric acid or nitric acid, adding an oxidant and phosphoric acid or phosphate to react to generate precursor iron phosphate of a lithium ion battery positive electrode material, and sintering the iron phosphate with lithium carbonate and C to synthesize the lithium iron phosphate. Such as:
chinese patent application No. 201210591476.8 discloses a preparation method of a lithium iron phosphate precursor of a lithium ion battery anode material, which comprises the steps of leaching siderite by sulfuric acid or hydrochloric acid, adjusting the concentration of the solution, adding hydrogen peroxide or an ozone oxidant and a precipitator, selectively precipitating elements in the siderite which are beneficial to the electrochemical performance of lithium iron phosphate by controlling the synthesis conditions, and drying to obtain the lithium iron phosphate precursor.
Chinese patent application No. 200810031119.3 discloses a method for preparing a lithium iron phosphate precursor by comprehensively utilizing ilmenite: leaching titanic iron ore with acid, filtering to obtain filtrate, and dissolving a certain amount of other iron sources in the filtrate to ensure that the concentration of Fe in the mixed solution is 0.01-3mol/L and the molar ratio of Ti to Fe is 0.0005-0.5; adding a proper amount of oxidant into the mixed solution, adjusting the pH value of the system to be 1.5-6.0 by using an aqueous solution of alkali to ensure that part of iron and certain impurity ions are coprecipitated, and filtering to obtain filtrate; adding a precipitator (0.01-6mol/L) into the filtrate, adjusting the pH value of the system to be 4.0-14.0 by using an aqueous solution of alkali, reacting in a stirring reactor at 10-90 ℃ for 10min-24h, filtering, washing, drying the precipitate at 50-150 ℃, and calcining in the air at 300-800 ℃ for 1-24h to obtain the ferric oxide of the doped metal element, which is the precursor of the lithium iron phosphate of the lithium ion battery anode material.
The lithium iron phosphate prepared by the methods described in the two documents has good electrochemical performance, but has the following defects that firstly, the process is long and the synthesis efficiency is low because acid is required to be added to leach iron in siderite; secondly, because of adding sulfuric acid, hydrochloric acid or nitric acid, impurity element SO which influences the performance of the battery is introduced4 2-、CL-And NO3 -And the like.
At present, ferric phosphate lithium is synthesized by directly using ferric salt, lithium salt and phosphoric acid under hydrothermal conditions without adding sulfuric acid, hydrochloric acid or nitric acid, such as Chinese patent applicationNo. 201110045252.2 discloses a method for greatly improving the performance of LiFePO which is a cathode material of a lithium ion battery prepared by low-temperature hydrothermal synthesis4A method with excellent electrochemical performance comprises the steps of preparing a slurry precursor in water through lithium salt, ferric salt and phosphoric acid according to a certain adding sequence and proportion, then adding a certain amount of organic solvent, and preparing nano LiFePO with excellent electrochemical performance under hydrothermal conditions4And (3) a positive electrode material. The raw material of the patent uses soluble ferric salt, and the preparation of the soluble ferric salt consumes a large amount of energy and increases reaction steps.
In addition, the capacity of the storage battery is an important index for measuring the performance of the storage battery, and lithium iron phosphate has some performance defects, and the energy density of the lithium iron phosphate battery is low due to the fact that the tap density and the compaction density are low due to the fact that the existing synthesized lithium iron phosphate particles are small.
Chinese patent publication No. CN104817059A discloses a method for preparing battery-grade iron phosphate by reacting iron powder with phosphoric acid, which comprises mixing iron powder with diluted phosphoric acid, and reacting to generate Fe (H)2PO4)2Then adding an oxidant to oxidize to generate iron phosphate precipitate, and filtering and drying to obtain high-purity battery-grade iron phosphate, namely dihydrate iron phosphate; ferric phosphate dihydrate is a nano-flaky crystal of a quasi-red iron phosphate ore (phosphosiderite) crystal form. The disclosed technology has the following defects: firstly, because the main raw material is iron powder, the common knowledge that the iron powder does not naturally exist in the nature, is a regenerated substance and needs to be made by steel making, the steel making is a more complicated process and consumes a large amount of electric energy, and if the regenerated substance is used for synthesizing the anode material of the lithium ion battery, the method is certainly not a good method which is worth recommending; secondly, hydrogen is generated in the reaction process, the hydrogen is flammable and explosive, and when the hydrogen reaches a certain proportion in the air, the hydrogen can explode when exposed to fire, which not only brings harmfulness to the whole process, but also requires that an operator has high operation skill. Therefore, the technology disclosed in the document cannot be popularized and industrialized in a large scale, and does not meet the current policy of energy conservation and environmental protection.
Disclosure of Invention
The invention provides a method for preparing a lithium ion battery anode material by siderite, aiming at overcoming the technical defects of long process, low synthesis efficiency, high danger coefficient, difficult operation and impurity element content in the existing lithium iron phosphate preparation technology and improving the density of lithium iron phosphate so as to improve the capacity of a lithium ion battery.
In order to achieve the purpose, the invention adopts the technical scheme that:
a method for preparing a high-density lithium ion battery anode material by siderite, which is characterized in that,
the first step is as follows: dissolving siderite
Directly adding phosphoric acid into siderite, wherein the concentration of the phosphoric acid is required to be 0.2-0.3mol/L, the molar ratio of iron to pure phosphoric acid is required to be 2 (4-8), the reaction temperature is 0-100 ℃, the reaction time is 1-5h, after full reaction, filtering to obtain an iron solution, and the chemical reaction formula is as follows:
FeCO3+2H3PO4=Fe2++2(H2PO4)-+H2O+CO2
in the second step, the solution of iron is mixed with the high molecular copolymer P (DMDAAC-AM)
Adding the iron solution obtained in the first step into a P (DMDAAC-AM) solution, and fully stirring to uniformly mix the solution and the solution, wherein the mass ratio of the P (DMDAAC-AM) to siderite is required to be 1: 10-1: 50;
thirdly, reacting the mixed solution of iron and P (DMDAAC-AM) with hydrogen peroxide
Adding hydrogen peroxide into the mixed solution in the second step, wherein the concentration of the hydrogen peroxide is 5-30wt%, the molar ratio of iron to pure hydrogen peroxide is required to be 2 (1-1.5), the reaction temperature is 50-100 ℃, the reaction time is 1-5h, after full reaction, filtering, washing with deionized water, and drying to obtain the ferric phosphate dihydrate as the precursor of the lithium iron phosphate, and the chemical reaction formula is as follows:
2Fe2++4(H2PO4)-+H2O2+2H2O=2FePO4·2H2O↓+2H3PO4
the fourth step: and (3) mixing and sintering the ferric phosphate dihydrate prepared in the third step with lithium carbonate and glucose to obtain lithium iron phosphate, wherein the mixing molar ratio of lithium phosphate to lithium carbonate to glucose (calculated by carbon) is 2 (1-1.1): 0.5-0.8), the reaction is carried out in a protective atmosphere, the reaction temperature is 600-800 ℃, and the reaction time is 5-15 hours.
The chemical reaction formula is as follows:
2FePO4·2H2O↓+Li2CO3+0.5C=2LiFePO4+1.5CO2+2H2O。
the lithium iron phosphate material prepared by the process is used as the anode, and the graphite is used as the cathode to manufacture the lithium ion battery.
The advantages of the present invention are illustrated below based on the reaction mechanism:
1. the invention directly adds phosphoric acid into siderite, leaches iron in siderite to obtain iron solution by controlling the concentration of phosphoric acid and the reaction temperature and time, then adds high molecular copolymer P (DMDAAC-AM) into the iron solution, because P (DMDAAC-AM) is the copolymer of dimethyl diallyl ammonium chloride and acrylamide, it is a glassy solid, easy to absorb water, it is an important water-soluble polymer, and it has flocculation and thickening properties, when adding hydrogen peroxide into the mixed solution of iron and P (DMDAAC-AM), because of the delayed precipitation of P (DMDAAC-AM), the particle size of iron phosphate after reaction is large, and finally the sintered lithium iron phosphate particles are controlled to about 10um, and the tap density reaches 1.5-2 g/cm3Thereby improving the energy density of the lithium iron phosphate battery.
2. The invention directly reacts to obtain the ferric phosphate dihydrate of the precursor of the lithium iron phosphate by controlling the concentration of the phosphoric acid and the reaction temperature and time, the reacted ferric phosphate dihydrate exists in the phosphoric acid in a precipitation form, and the pure precursor ferric phosphate dihydrate is obtained by direct filtration, thereby not only omitting the process of leaching iron in siderite by hydrochloric acid or sulfuric acid in advance, reducing the cost, but also not introducing other impurities which are not beneficial to the performance of the battery, and improving the conductivity of the battery.
3. The siderite is a mineral with wide distribution and can be used as iron ore to refine iron, and the siderite is directly used for synthesizing the precursor ferric phosphate dihydrate, so that the energy consumption step of extracting iron from the iron ore is omitted, the aim of directly obtaining the anode material of the lithium ion battery from the nature is fulfilled, and the siderite is easier to react with phosphoric acid compared with iron powder, and the feasibility of the reaction is improved.
4. The gas generated in the reaction process is colorless, tasteless and odorless CO at normal temperature2Gas, CO2The gas has no harm to human body, no flammability, easy operation, and generated CO2Plays a role of stirring the solution, increases the activity of the siderite and further improves the feasibility of the reaction
In a word, the invention is a method for preparing the lithium ion battery anode material, which has low energy consumption and high safety factor and is convenient to popularize.
Drawings
Fig. 1 is a Scanning Electron Microscope (SEM) image of lithium iron phosphate prepared in example 1 of the present invention.
Fig. 2 is an X-ray powder diffraction (XRD) pattern of lithium iron phosphate prepared in example 1 of the present invention.
Fig. 3 is a Scanning Electron Microscope (SEM) image of lithium iron phosphate prepared in example 2 of the present invention.
Fig. 4 is an X-ray powder diffraction (XRD) pattern of lithium iron phosphate prepared in example 2 of the present invention.
The technical scheme of the invention is further illustrated by combining the specific examples.
In the first embodiment, taking siderite containing 1mol of iron carbonate as an example, the concentration of phosphoric acid is 0.2mol/L, and the concentration of hydrogen peroxide is 10 wt%, and the specific preparation method comprises the following steps:
the first step is as follows: dissolving siderite
According to the mol ratio of iron to pure phosphoric acid of 2:7, H is directly added into siderite3PO is 3.5mol of phosphoric acid, the reaction temperature is 40 ℃, the reaction time is 5 hours, and after full reaction, an iron solution is obtained;
in the second step, the solution of iron is mixed with P (DMDAAC-AM)
Adding the iron solution obtained in the first step into a P (DMDAAC-AM) solution, and fully stirring to uniformly mix the solution and the solution, wherein the mass ratio of siderite to P (DMDAAC-AM) is 10: 1;
thirdly, reacting the iron solution with hydrogen peroxide
Adding H into the iron solution according to the molar ratio of iron to pure hydrogen peroxide of 2:12O20.5mol of hydrogen peroxide, wherein the concentration of the hydrogen peroxide is 10 wt%, the reaction temperature is 70 ℃, the reaction time is 3 hours, and after full reaction, the mixture is filtered, washed by deionized water and dried to obtain a precursor ferric phosphate dihydrate;
the fourth step: and mixing and sintering the ferric phosphate dihydrate prepared in the first step, lithium carbonate and glucose to obtain lithium iron phosphate, wherein the mixing molar ratio of the ferric phosphate, the lithium carbonate and the glucose (calculated by carbon) is 2:1:0.6, and the reaction is carried out in a protective atmosphere, wherein the reaction temperature is 700 ℃ and the reaction time is 10 hours. The scanning electron microscope image and the X-ray powder diffraction image of the prepared lithium iron phosphate are respectively shown in the figures 1-2.
Example one lithium iron phosphate particle tap density of 1.7g/cm3
By using the lithium iron phosphate prepared in the first embodiment as a positive electrode and graphite as a negative electrode, a lithium ion battery with a battery voltage of 3V and a 18650 battery capacity of 1300mAh can be prepared.
Example two
In the second embodiment, 1mol of siderite (calculated by iron carbonate) is taken as an example, the concentration of phosphoric acid is 0.3mol/L, and the concentration of hydrogen peroxide is 20 wt%, and the specific preparation method comprises the following steps:
the first step is as follows: dissolving siderite.
According to the mol ratio of iron to pure phosphoric acid of 2:4, H is directly added into siderite3PO is 2mol of phosphoric acid, the concentration of the phosphoric acid is 0.3mol/L, the reaction temperature is 70 ℃, the reaction time is 3 hours, and after full reaction, an iron solution is obtained;
in the second step, the solution of iron is mixed with P (DMDAAC-AM)
Adding the iron solution obtained in the first step into the P (DMDAAC-AM) solution, and fully stirring to uniformly mix the iron solution and the P (DMDAAC-AM) solution, wherein the mass ratio of the siderite to the P (DMDAAC-AM) is required to be 20: 1.
And thirdly, reacting the iron solution with hydrogen peroxide.
Adding H into the iron solution according to the molar ratio of iron to pure hydrogen peroxide of 2:1.52O20.75mol of hydrogen peroxide, wherein the reaction temperature is 90 ℃, the reaction time is 1h, and after full reaction, filtering, washing with deionized water and drying to obtain a precursor ferric phosphate dihydrate;
the fourth step: mixing and sintering the ferric phosphate dihydrate prepared in the first step, lithium carbonate and glucose to obtain lithium iron phosphate, wherein the mixing molar ratio of the ferric phosphate to the lithium carbonate to the glucose (calculated by carbon) is 2:1.1: 0.6; the reaction was carried out in a protective atmosphere at a reaction temperature of 650 ℃ for a reaction time of 12 h. The scanning electron microscope image and the X-ray powder diffraction pattern of the prepared lithium iron phosphate are respectively shown in fig. 3-4.
The tap density of the lithium iron phosphate particles prepared in the second embodiment reaches 1.75g/cm3
The lithium iron phosphate prepared in the second embodiment is used as a positive electrode, graphite is used as a negative electrode, and the battery voltage is 3V, and the 18650 battery capacity is 1300 mAh.

Claims (1)

1.一种利用菱铁矿制备高密度磷酸铁锂的方法,其特征在于,1. a method utilizing siderite to prepare high-density lithium iron phosphate, is characterized in that, 第一步:溶解菱铁矿Step 1: Dissolving siderite 在菱铁矿中直接加入磷酸,要求磷酸的浓度为0.2-0.3mol/L,要求铁与纯磷酸的摩尔比为2:(4-8),反应温度为0-100℃,反应时间为1-5h,待充分反应后,过滤得到铁的溶液,化学反应式为:Add phosphoric acid directly to siderite, the concentration of phosphoric acid is required to be 0.2-0.3mol/L, the molar ratio of iron to pure phosphoric acid is required to be 2:(4-8), the reaction temperature is 0-100℃, and the reaction time is 1 -5h, after fully reacted, the iron solution was obtained by filtration. The chemical reaction formula is: FeCO3+2H3PO4=Fe2++2(H2PO4)-+H2O+CO2 FeCO 3 +2H 3 PO 4 =Fe 2+ +2(H 2 PO 4 ) - +H 2 O+CO 2 第二步: 铁的溶液与高分子共聚物P( DMDAAC-AM)混合 Step 2: The iron solution is mixed with the polymer copolymer P (DMDAAC-AM) 把第一步得到的铁的溶液加入到P( DMDAAC-AM)溶液当中充分搅拌,使二者混合均匀,要求P( DMDAAC -AM)与菱铁矿的质量之比为1:10~1:50;Add the iron solution obtained in the first step into the P(DMDAAC-AM) solution and stir well to make the two evenly mixed. The mass ratio of P(DMDAAC-AM) to siderite is required to be 1:10~1: 50; 第三步: 铁与P( DMDAAC-AM)的混合溶液与双氧水反应 Step 3: The mixed solution of iron and P (DMDAAC-AM) reacts with hydrogen peroxide 在第二步的混合溶液中加入双氧水,双氧水的浓度为5-30wt%,要求铁与纯双氧水的摩尔比为2:(1-1.5),反应温度为50-100℃,反应时间为1-5h,待充分反应后,过滤,用去离子水洗涤、干燥得磷酸铁锂前驱体二水磷酸铁,化学反应式为: In the mixed solution of the second step, add hydrogen peroxide, the concentration of hydrogen peroxide is 5-30wt%, the molar ratio of iron and pure hydrogen peroxide is required to be 2:(1-1.5), the reaction temperature is 50-100 ℃, and the reaction time is 1- 5h, after fully reacting, filtering, washing with deionized water, and drying to obtain iron phosphate dihydrate, the precursor of lithium iron phosphate. The chemical reaction formula is: 2Fe2++4(H2PO4)-+H2O2+2H2O =2FePO4·2H2O↓+2H3PO4 2Fe 2+ +4(H 2 PO 4 ) - +H 2 O 2 +2H 2 O =2FePO 4 ·2H 2 O↓+2H 3 PO 4 第四步:将第三步制备的二水磷酸铁与碳酸锂和葡萄糖混合烧结后得到振实密度达到1.5—2g/cm3的磷酸铁锂,二水磷酸铁与碳酸锂和以碳计葡萄糖混合摩尔比为2:(1-1.1):(0.5-0.8),反应在保护气氛中进行,反应温度为600-800℃,反应时间为5-15h;The fourth step: the iron phosphate dihydrate prepared in the third step is mixed and sintered with lithium carbonate and glucose to obtain lithium iron phosphate with a tap density of 1.5-2g/ cm3 , iron phosphate dihydrate and lithium carbonate and glucose in terms of carbon. The mixing molar ratio is 2:(1-1.1):(0.5-0.8), the reaction is carried out in a protective atmosphere, the reaction temperature is 600-800°C, and the reaction time is 5-15h; 化学反应式为:The chemical reaction formula is: 2FePO4·2H2O↓+Li2CO3+0.5C=2LiFePO4+1.5CO2 + 2H2O。2FePO 4 ·2H 2 O↓+Li 2 CO 3 +0.5C=2LiFePO 4 +1.5CO 2 + 2H 2 O.
CN201711070611.3A 2017-11-03 2017-11-03 A method for preparing high-density lithium iron phosphate by using siderite Active CN107863530B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201711070611.3A CN107863530B (en) 2017-11-03 2017-11-03 A method for preparing high-density lithium iron phosphate by using siderite

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201711070611.3A CN107863530B (en) 2017-11-03 2017-11-03 A method for preparing high-density lithium iron phosphate by using siderite

Publications (2)

Publication Number Publication Date
CN107863530A CN107863530A (en) 2018-03-30
CN107863530B true CN107863530B (en) 2020-04-28

Family

ID=61700623

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201711070611.3A Active CN107863530B (en) 2017-11-03 2017-11-03 A method for preparing high-density lithium iron phosphate by using siderite

Country Status (1)

Country Link
CN (1) CN107863530B (en)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11552290B2 (en) 2018-07-27 2023-01-10 Form Energy, Inc. Negative electrodes for electrochemical cells
CN108987749A (en) * 2018-08-28 2018-12-11 深圳市德方纳米科技股份有限公司 The method of ferric phosphate, the preparation method of iron manganese phosphate for lithium and lithium iron phosphate positive material are prepared by phosphorus ore
US12294086B2 (en) 2019-07-26 2025-05-06 Form Energy, Inc. Low cost metal electrodes
CN114613965B (en) * 2022-03-22 2025-01-10 宜昌邦普循环科技有限公司 Preparation method and application of lithium iron phosphate/carbon composite material
CN114835101A (en) * 2022-05-25 2022-08-02 雅安天蓝新材料科技有限公司 Composition for preparing lithium iron phosphate, preparation method of lithium iron phosphate and battery anode material
CN115477292A (en) * 2022-10-10 2022-12-16 唐山亨坤新能源材料有限公司 A kind of method that iron ore powder prepares iron phosphate
CN117023542A (en) * 2023-07-19 2023-11-10 合肥国轩高科动力能源有限公司 Low-temperature high-magnification lithium iron manganese phosphate material and preparation method and application thereof
CN117797764B (en) * 2024-02-28 2024-06-07 广东顺控自华科技有限公司 Calcium-based siderite and preparation method and application thereof

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100567144C (en) * 2008-04-15 2009-12-09 中南大学 A method for comprehensively utilizing ilmenite to prepare lithium iron phosphate precursor
US9682861B2 (en) * 2009-05-04 2017-06-20 Meecotech, Inc. Electrode active composite materials and methods of making thereof
CN101948379B (en) * 2010-09-01 2013-04-10 中国科学院宁波材料技术与工程研究所 Method for preparing battery-level ferrous oxalate
CN102126713B (en) * 2011-03-01 2012-10-03 四川大学 High-purity iron phosphate used for producing lithium ion battery positive-pole material and preparation method thereof
WO2014056143A1 (en) * 2012-10-09 2014-04-17 上海交通大学 Lithium iron phosphate material and preparation thereof
EP2778127A1 (en) * 2013-03-15 2014-09-17 Clariant International Ltd. Lithium transition metal phosphate secondary agglomerates and process for its manufacture
CN104817059B (en) * 2015-04-29 2017-07-18 江西东华科技园有限责任公司 A kind of method that battery-grade iron phosphate is prepared by iron powder and phosphatase reaction

Also Published As

Publication number Publication date
CN107863530A (en) 2018-03-30

Similar Documents

Publication Publication Date Title
CN107863530B (en) A method for preparing high-density lithium iron phosphate by using siderite
WO2022116702A1 (en) Method for preparing iron phosphate and use thereof
WO2022116692A1 (en) Method for preparing iron phosphate from lithium extraction slag of waste lithium iron phosphate positive electrode powder and application
CN107863531B (en) A method for preparing lithium ion battery positive electrode material by using siderite
CN101264876B (en) Method for preparing ferric lithium phosphate precursor by comprehensive utilization of ilmenite
CN101508431A (en) Process for producing homodisperse spherical iron lithium phosphate
CN113460987A (en) Doped iron phosphate and preparation method and application thereof
CN101121509A (en) Preparation method of hydrothermal synthesis of lithium iron phosphate cathode material for lithium ion battery
JP2012155916A (en) Lithium secondary battery cathode active material and its manufacturing method, and precursor of the same and its manufacturing method
CN104743537A (en) Preparation method for lithium iron phosphate/carbon composite positive material with high multiplying power
CN113348150A (en) Titanium oxide, method for producing titanium oxide, and lithium secondary battery using titanium oxide-containing electrode active material
CN103165877A (en) A kind of preparation method and application of lithium battery negative electrode material
CN104835956A (en) Method of preparing lithium ion battery anode material from two or more metal salts/solutions of nickel, cobalt, manganese, aluminum and the like
CN107732236B (en) Utilize the method for siderite hydrothermal synthesis anode material for lithium-ion batteries
CN115148483A (en) Method for preparing LiFe5O8 magnetic material by using waste lithium iron phosphate battery
CN114899392A (en) Preparation method of lithium iron phosphate or lithium ferromanganese anode material of lithium ion battery
CN107720719B (en) Method for preparing lithium iron manganese phosphate by using siderite and rhodochrosite
US20240034626A1 (en) Method for preparing high performance lithium iron phosphate nanopowder
JP5196486B2 (en) Method for producing composite titanium oxide
JPH0896809A (en) Manufacture of tricobalt tetroxide for lithium secondary battery positive electrode material
US20050142058A1 (en) Low temperature process for preparing tricobalt tetraoxide
CN112938926B (en) Lithium iron phosphate and preparation method thereof
CN112010278B (en) Method for preparing battery-grade vanadyl fluorophosphate sodium anode material from industrial waste vanadium and prepared anode material
CN103456950A (en) Green synthesis method for lithium-nickel phosphate/carbon composite material for lithium-ion battery
CN118702165B (en) Sodium ion battery precursor, positive electrode material and preparation method thereof, and sodium ion battery

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant