WO2012062111A1 - Processing method of lithium iron phosphate used as positive electrode material of lithium ion battery - Google Patents

Processing method of lithium iron phosphate used as positive electrode material of lithium ion battery Download PDF

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WO2012062111A1
WO2012062111A1 PCT/CN2011/075934 CN2011075934W WO2012062111A1 WO 2012062111 A1 WO2012062111 A1 WO 2012062111A1 CN 2011075934 W CN2011075934 W CN 2011075934W WO 2012062111 A1 WO2012062111 A1 WO 2012062111A1
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iron phosphate
lithium iron
lithium
ion battery
treating
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PCT/CN2011/075934
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Chinese (zh)
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朱杰
杜振山
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河北力滔电池材料有限公司
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    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01GCOMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
    • C01G49/00Compounds of iron
    • C01G49/009Compounds containing, besides iron, two or more other elements, with the exception of oxygen or hydrogen
    • 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
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/13Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • H01M4/139Processes of manufacture
    • H01M4/1397Processes of manufacture of electrodes based on inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFy
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/362Composites
    • H01M4/366Composites as layered products
    • 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
    • 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
    • H01M4/62Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • H01M4/624Electric conductive fillers
    • H01M4/625Carbon or graphite
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2006/00Physical properties of inorganic compounds
    • C01P2006/40Electric properties
    • 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

Definitions

  • the invention belongs to the technical field of lithium ion batteries, and in particular relates to a method for treating a lithium iron phosphate cathode material. Background technique
  • the lithium iron phosphate material for lithium ion batteries has unparalleled safety, long cycle life, good high temperature performance and stable discharge platform. It is used in electric vehicles, energy storage batteries and large power tool batteries. The only candidate for the positive electrode material. Lithium iron phosphate materials produced by different processes have considerable performance differences. Among them, the self-discharge problem of lithium iron phosphate material is one of the more serious problems. For example, many solid phase lithium iron phosphate materials have a monthly self-discharge of more than 3%. The carbon coating is good, and the hydrothermal method for producing lithium iron phosphate material has a monthly self-discharge of less than 1%. Materials with high self-discharge generally have high temperature cycling and storage performance.
  • Typical data are: 55°C cycle 300 times attenuation capacity over 20%. According to the literature, this is because Fe203 or other highly active iron compounds remaining in lithium iron phosphate, during the cycle, iron ions continue to electrochemically or chemically dissolve, iron ions migrate to the negative electrode, blocking the lithium ion diffusion channel, thereby Causes a rapid decline in cycle life. After dissecting the battery with poor performance, the separator and the negative electrode will also be brown or yellow, and ion probe chromatography will show a large amount of iron ions. Therefore, the dissolution and migration of iron ions are eliminated, and the self-discharge performance and high-temperature performance of the battery can be effectively improved. Summary of the invention
  • the present invention provides a method for treating a lithium iron battery positive electrode material lithium iron phosphate in order to solve the problems existing in the prior art.
  • the object of the present invention is to provide a lithium ion battery cathode material lithium iron phosphate which has the advantages of simple process, convenient operation, excellent material performance, and can effectively improve the shelf life and high temperature performance of the battery, stable product quality, and greatly improved battery performance.
  • Approach. The iron ion elution is prevented from migrating to the negative electrode, and the lithium ion diffusion channel of the negative electrode is prevented from being clogged, thereby improving the self-discharge and high-temperature performance of the lithium iron phosphate material.
  • the technical principle of the present invention is: First, the wettability of the lithium iron phosphate material is improved, and then the high activity iron ions on the surface of the lithium iron phosphate are leached with an acid solution.
  • the acidity of the solution is such that the high-activity iron ions are dissolved without dissolving the lithium iron phosphate, and the pH of the solution is controlled to be between 1. 5 and 2.5.
  • the lithium iron phosphate material is washed and dried to obtain a desired lithium iron phosphate material.
  • the method for treating the lithium iron phosphate cathode material of the present invention adopts the following technical scheme:
  • a lithium ion battery cathode material lithium iron phosphate treatment method characterized in that: lithium ion battery cathode material lithium iron phosphate treatment process includes:
  • the method for treating the lithium iron phosphate cathode material of the present invention can also adopt the following technical measures:
  • the lithium ion battery cathode material lithium iron phosphate treatment method is characterized in that the wetting agent is ethanol, methanol, acetone or butyl. Ketone organic solvent. It can wet the surface of lithium iron phosphate material, and it can be dissolved infinitely with water. At the same time, it will evaporate during the drying process without affecting the performance of the system.
  • the lithium ion battery cathode material lithium iron phosphate treatment method is characterized in that: when the wetting agent treats the lithium iron phosphate material, the weight ratio of the lithium iron phosphate material to the wetting solution is 1: 1-10.
  • the method for treating a lithium iron battery positive electrode material lithium iron phosphate is characterized in that: the acid in the acid solution is nitric acid and oxalic acid. Both acids can reach a pH of 0-1, and the trace acid remaining after washing can be evaporated or sublimated during the subsequent drying process without affecting the performance of the system.
  • the method for treating a lithium iron battery positive electrode material lithium iron phosphate is characterized in that: the protective gas is nitrogen, argon, helium or a mixed gas of one or more of them.
  • the lithium ion battery cathode material lithium iron phosphate treatment method is characterized in that: the filtered lithium iron phosphate is washed twice with steamed water or pure water of 10-20 times weight of lithium iron phosphate material, and the operation control temperature is 10-25 ° C.
  • the method for treating a lithium iron battery positive electrode material lithium iron phosphate is characterized in that: the drying temperature is 180-250 ° C under vacuum conditions or a protective gas atmosphere.
  • Lithium ion battery cathode material lithium iron phosphate treatment method due to the use of the novel technical solution of the invention, compared with the prior art, the invention produces lithium iron phosphate cathode material, after acid washing, the surface of high activity iron ions The magnitude is reduced. After being assembled into a lithium iron phosphate battery, the iron dissolution of the positive electrode is greatly reduced, and the battery life and high temperature performance are effectively improved.
  • the lithium iron phosphate battery treated by the invention has a monthly self-discharge reduction of 0.8%, and the 55 °C high temperature 1C/300 cycle decay rate is reduced from the original 20% to 11.6%, and the battery performance is greatly improved.
  • the invention has the advantages of simple process, convenient operation, excellent material performance, effective improvement of the shelf life and high temperature performance of the battery, stable product quality, and greatly improved battery performance. detailed description
  • Lithium ion battery cathode material lithium iron phosphate treatment method firstly prepared 100 kg 0.1% concentration of ethanol water solution. After mixing, slowly add 10 kg of lithium iron phosphate powder material to stir into a uniform suspension. Then, 50 kg of a nitric acid solution having a pH of 0 was prepared, and the nitric acid solution was slowly added to the lithium iron phosphate suspension under stirring, and the pH of the final solution was 2.5%. After reaching the set pH value, the mixture was stirred for 1 hour, and then the solution was filtered to filter out the lithium iron phosphate material therein. Wash twice with 150 kg of distilled water. All of the above operating ambient temperatures and solution temperatures are 25 °C. The washed lithium iron phosphate material. Dry at 200 ° C under vacuum to constant weight (completely dried) to obtain the final product.
  • lithium iron phosphate as a positive electrode material for lithium ion batteries
  • 1000 kg of a 3% concentration of butanone aqueous solution is prepared.
  • 4000 kg of a nitric acid solution having a pH of 1 was prepared, and the nitric acid solution was slowly added to the lithium iron phosphate suspension under stirring, and the pH of the final solution was 1.5.
  • the mixture was stirred for 3 hours, and then the solution was filtered, and the lithium iron phosphate material was filtered off. Wash twice with 20,000 kg of steamed water. All of the above operating ambient and solution temperatures are 15 °C.
  • lithium iron phosphate For the treatment of lithium iron phosphate cathode material lithium iron phosphate, first prepare 500 kg of 1% methanol aqueous solution. After the preparation, slowly add 100 kg of lithium iron phosphate powder material to stir into a uniform suspension. Prepare 600 kg of oxalic acid solution with a pH of 0.5, and slowly add the oxalic acid solution to the lithium iron phosphate suspension under stirring, with the pH of the final solution reaching 2. 0. After reaching the set pH value, the mixture was stirred for 2 hours, and then the solution was filtered to filter out the lithium iron phosphate material therein. Wash twice with 1500 kg of distilled water. All of the above operating ambient temperatures and solution temperatures are 25 °C. The washed lithium iron phosphate material. Dry at 200 ° C under vacuum to constant weight (completely dried) to obtain the final product.
  • the lithium iron phosphate cathode material prepared by the invention has been subjected to acid washing, and the surface active iron ions are greatly reduced. After being assembled into a lithium iron phosphate battery, the iron dissolution of the positive electrode is greatly reduced, and the battery life and high temperature performance are effectively improved.

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

Abstract

A processing method of lithium iron phosphate used as the positive electrode material of a lithium ion battery comprises: 1) wet-treating the lithium iron phosphate material, i.e. processing the lithium iron phosphate material with a wetting agent of 0.1-3% wt. in concentration, to obtain a homogeneous aqueous suspension of lithium iron phosphate material; 2) leaching high active iron ions on the surface of the lithium iron phosphate material with acid solution, i.e. adding an acid solution with pH value of 0-1 into the suspension of lithium iron phosphate under agitation, to keep the pH value of the obtained solution at the range between 1.5-2.5, while rendering a complete reaction by agitating; 3) filtering and drying, i.e. filtering the solution, washing the filtered lithium iron phosphate with distilled water or pure water, and drying the washed lithium iron phosphate material under vacuum condition or protective gas atmosphere to obtain the finished lithium iron phosphate material. The lithium iron phosphate material is carbon coated. The shelf life and high temperature property of the battery can be improved by the method.

Description

一种锂离子电池正极材料磷酸铁锂的处理方法 技术领域  Method for processing lithium iron phosphate cathode material lithium iron phosphate
本发明属于锂离子电池技术领域,特别是涉及一种锂离子电池正极材料磷酸铁锂的 处理方法。 背景技术  The invention belongs to the technical field of lithium ion batteries, and in particular relates to a method for treating a lithium iron phosphate cathode material. Background technique
目前, 锂离子电池用的磷酸铁锂材料具有无与伦比的安全性, 超长的循环寿命、 良 好的高温性能和稳定的放电平台, 是用于电动交通工具、 储能电池和大倍率电动工具电 池的唯一侯选正极材料。 不同工艺制造的磷酸铁锂材料具有相当大的性能差异。 其中, 磷酸铁锂材料的自放电问题是较为严重的问题之一。 例如, 很多固相法合成的磷酸铁锂 材料月自放电达到 3%以上。 而碳包覆良好、 水热法制造磷酸铁锂材料月自放电小于 1%。 自放电高的材料一般高温循环和储存性能也比较差, 典型数据是: 55°C循环 300次衰减 容量超过 20%。有文献认为,这是因为磷酸铁锂中残存的 Fe203或其他高活性铁化合物, 在循环过程中, 铁离子不断发生电化学或化学溶解, 铁离子迁移到负极, 堵塞了锂离子 扩散通道, 从而造成循环寿命的迅速下降。 解剖循环后性能较差的电池, 也会发现隔膜 和负极变成棕色或黄色, 离子探针色谱证明出现大量的铁离子。 因此, 消除了铁离子的 溶解和迁移, 就可以有效地改善电池的自放电性能和高温性能。 发明内容  At present, the lithium iron phosphate material for lithium ion batteries has unparalleled safety, long cycle life, good high temperature performance and stable discharge platform. It is used in electric vehicles, energy storage batteries and large power tool batteries. The only candidate for the positive electrode material. Lithium iron phosphate materials produced by different processes have considerable performance differences. Among them, the self-discharge problem of lithium iron phosphate material is one of the more serious problems. For example, many solid phase lithium iron phosphate materials have a monthly self-discharge of more than 3%. The carbon coating is good, and the hydrothermal method for producing lithium iron phosphate material has a monthly self-discharge of less than 1%. Materials with high self-discharge generally have high temperature cycling and storage performance. Typical data are: 55°C cycle 300 times attenuation capacity over 20%. According to the literature, this is because Fe203 or other highly active iron compounds remaining in lithium iron phosphate, during the cycle, iron ions continue to electrochemically or chemically dissolve, iron ions migrate to the negative electrode, blocking the lithium ion diffusion channel, thereby Causes a rapid decline in cycle life. After dissecting the battery with poor performance, the separator and the negative electrode will also be brown or yellow, and ion probe chromatography will show a large amount of iron ions. Therefore, the dissolution and migration of iron ions are eliminated, and the self-discharge performance and high-temperature performance of the battery can be effectively improved. Summary of the invention
本发明为解决现有技术存在的问题,提供了一种锂离子电池正极材料磷酸铁锂的处 理方法。  The present invention provides a method for treating a lithium iron battery positive electrode material lithium iron phosphate in order to solve the problems existing in the prior art.
本发明目的是提供一种具有工工艺简单, 操作方便, 材料性能优良, 能有效提高电 池的搁置寿命和高温性能, 产品质量稳定, 电池性能大幅改善等优点的锂离子电池正极 材料磷酸铁锂的处理方法。 防止铁离子溶出向负极迁移, 避免负极的锂离子扩散通道被 堵塞, 从而改善磷酸铁锂材料的自放电和高温性能。  The object of the present invention is to provide a lithium ion battery cathode material lithium iron phosphate which has the advantages of simple process, convenient operation, excellent material performance, and can effectively improve the shelf life and high temperature performance of the battery, stable product quality, and greatly improved battery performance. Approach. The iron ion elution is prevented from migrating to the negative electrode, and the lithium ion diffusion channel of the negative electrode is prevented from being clogged, thereby improving the self-discharge and high-temperature performance of the lithium iron phosphate material.
本发明的技术原理是: 首先改善磷酸铁锂材料的润湿性, 然后用酸溶液浸出磷酸铁 锂表面的高活性铁离子。 溶液的酸度恰好使高活性铁离子溶解而不会溶解磷酸铁锂, 这 需要将溶液 PH值控制在 1. 5-2. 5之间。浸出高活性铁离子后将磷酸铁锂材料洗涤烘干, 得到所需要的磷酸铁锂材料。  The technical principle of the present invention is: First, the wettability of the lithium iron phosphate material is improved, and then the high activity iron ions on the surface of the lithium iron phosphate are leached with an acid solution. The acidity of the solution is such that the high-activity iron ions are dissolved without dissolving the lithium iron phosphate, and the pH of the solution is controlled to be between 1. 5 and 2.5. After leaching high-activity iron ions, the lithium iron phosphate material is washed and dried to obtain a desired lithium iron phosphate material.
本发明锂离子电池正极材料磷酸铁锂的处理方法采用如下技术方案:  The method for treating the lithium iron phosphate cathode material of the present invention adopts the following technical scheme:
一种锂离子电池正极材料磷酸铁锂的处理方法, 其特点是: 锂离子电池正极材料磷 酸铁锂的处理过程包括:  A lithium ion battery cathode material lithium iron phosphate treatment method, characterized in that: lithium ion battery cathode material lithium iron phosphate treatment process includes:
1 ) 磷酸铁锂材料的润湿处理: 首先用 0. 1-3%重量百分比浓度的润湿剂处理磷 酸铁锂材料, 使包覆碳的磷酸铁锂材料形成均匀的水性悬浊液; 1) Wetting treatment of lithium iron phosphate material: firstly treating phosphorus with a wetting agent of 0.1 to 3% by weight a lithium iron phosphate material, forming a carbon-coated lithium iron phosphate material to form a uniform aqueous suspension;
2 ) 用酸溶液浸出磷酸铁锂表面的高活性铁离子: 将 pH值为 0-1的酸溶液在搅 拌状态下加入到磷酸铁锂悬浊液中, 使最终溶液的 PH值保持在 1. 5-2. 5之间, 搅拌使 体系充分反应;  2) Leaching the high-activity iron ions on the surface of the lithium iron phosphate with an acid solution: Adding the acid solution having a pH of 0-1 to the lithium iron phosphate suspension under stirring to maintain the pH of the final solution at 1. 5-2. 5, stirring to make the system fully react;
3 ) 过滤烘干: 溶液过滤, 滤出的磷酸铁锂用蒸熘水或纯净水洗涤; 洗涤后的磷 酸铁锂材料, 真空条件或保护性气体气氛下烘干, 得到最终的磷酸铁锂材料。  3) Filtration and drying: The solution is filtered, and the filtered lithium iron phosphate is washed with distilled water or purified water; the washed lithium iron phosphate material is dried under vacuum or a protective gas atmosphere to obtain a final lithium iron phosphate material. .
本发明锂离子电池正极材料磷酸铁锂的处理方法还可以采用如下技术措施: 所述的锂离子电池正极材料磷酸铁锂的处理方法,其特点是:润湿剂为乙醇、 甲醇、 丙酮或丁酮有机溶剂。 可以润湿磷酸铁锂材料表面, 又与水无限固溶, 同时在烘干过程 中蒸发掉, 不影响体系性能。  The method for treating the lithium iron phosphate cathode material of the present invention can also adopt the following technical measures: The lithium ion battery cathode material lithium iron phosphate treatment method is characterized in that the wetting agent is ethanol, methanol, acetone or butyl. Ketone organic solvent. It can wet the surface of lithium iron phosphate material, and it can be dissolved infinitely with water. At the same time, it will evaporate during the drying process without affecting the performance of the system.
所述的锂离子电池正极材料磷酸铁锂的处理方法, 其特点是: 润湿剂处理磷酸铁锂 材料时, 磷酸铁锂材料与润湿溶液的重量比为 1 : 1-10。  The lithium ion battery cathode material lithium iron phosphate treatment method is characterized in that: when the wetting agent treats the lithium iron phosphate material, the weight ratio of the lithium iron phosphate material to the wetting solution is 1: 1-10.
所述的锂离子电池正极材料磷酸铁锂的处理方法, 其特点是: 酸溶液中的酸为硝酸 和草酸。 两种酸都可以达到 0-1的 pH值, 且洗涤后残留的微量酸在随后的烘干过程中 可以蒸发或升华掉, 不影响体系性能。  The method for treating a lithium iron battery positive electrode material lithium iron phosphate is characterized in that: the acid in the acid solution is nitric acid and oxalic acid. Both acids can reach a pH of 0-1, and the trace acid remaining after washing can be evaporated or sublimated during the subsequent drying process without affecting the performance of the system.
所述的锂离子电池正极材料磷酸铁锂的处理方法, 其特点是: 酸溶液和磷酸铁锂悬 浊液的重量比为 1 : 0. 5-2, 最终溶液的 pH值保持在 1. 5-2. 5之间时搅拌 1_3小时。  5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 5 Stir between 1 and 3 hours between -2.5.
所述的锂离子电池正极材料磷酸铁锂的处理方法, 其特点是: 保护性气体为氮气、 氩气、 氦气或它们中的一种或几种的混合气体。  The method for treating a lithium iron battery positive electrode material lithium iron phosphate is characterized in that: the protective gas is nitrogen, argon, helium or a mixed gas of one or more of them.
所述的锂离子电池正极材料磷酸铁锂的处理方法, 其特点是: 滤出的磷酸铁锂用磷 酸铁锂材料重量 10-20倍的蒸熘水或纯净水洗涤 2遍, 操作控制温度为 10-25°C。  The lithium ion battery cathode material lithium iron phosphate treatment method is characterized in that: the filtered lithium iron phosphate is washed twice with steamed water or pure water of 10-20 times weight of lithium iron phosphate material, and the operation control temperature is 10-25 ° C.
所述的锂离子电池正极材料磷酸铁锂的处理方法, 其特点是: 真空条件或保护性气 体气氛下烘干温度为 180— 250°C。  The method for treating a lithium iron battery positive electrode material lithium iron phosphate is characterized in that: the drying temperature is 180-250 ° C under vacuum conditions or a protective gas atmosphere.
本发明具有的优点和积极效果:  The invention has the advantages and positive effects:
锂离子电池正极材料磷酸铁锂的处理方法, 由于采用了本发明全新的技术方案, 与 现有技术相比, 发明制得的磷酸铁锂正极材料, 经过了酸洗涤, 表面高活性铁离子大幅 度减少。 在组装成磷酸铁锂电池后, 正极的铁溶出大幅度减少, 有效提高了电池的搁置 寿命和高温性能。 经过本发明处理的磷酸铁锂电池月自放电降低到 0. 8%, 55 °C高温 1C/300次循环衰减率由原来的 20%降低到 11. 6%, 电池性能得到大幅度改善。  Lithium ion battery cathode material lithium iron phosphate treatment method, due to the use of the novel technical solution of the invention, compared with the prior art, the invention produces lithium iron phosphate cathode material, after acid washing, the surface of high activity iron ions The magnitude is reduced. After being assembled into a lithium iron phosphate battery, the iron dissolution of the positive electrode is greatly reduced, and the battery life and high temperature performance are effectively improved. The lithium iron phosphate battery treated by the invention has a monthly self-discharge reduction of 0.8%, and the 55 °C high temperature 1C/300 cycle decay rate is reduced from the original 20% to 11.6%, and the battery performance is greatly improved.
本发明具有工艺简单, 操作方便, 材料性能优良, 能有效提高电池的搁置寿命和高 温性能, 产品质量稳定, 电池性能大幅改善等优点。 具体实施方式  The invention has the advantages of simple process, convenient operation, excellent material performance, effective improvement of the shelf life and high temperature performance of the battery, stable product quality, and greatly improved battery performance. detailed description
为能进一步了解本发明的技术内容、 特点及功效, 兹列举以下实例, 并详细说明如 下: In order to further understand the technical content, features and effects of the present invention, the following examples are listed, and Next:
实施例 1  Example 1
锂离子电池正极材料磷酸铁锂的处理方法,首先配制 100公斤 0. 1%浓度的乙醇水溶 液。 配好后, 缓慢加入 10公斤磷酸铁锂粉体材料搅拌成均匀的悬浊液。 然后配制 50公 斤 pH值为 0的硝酸溶液, 将硝酸溶液在搅拌状态下缓慢加入到磷酸铁锂悬浊液中, 以 最终溶液的 pH值达到 2. 5为准。 到达设定的 pH值后, 搅拌 1小时, 然后将溶液过滤, 滤出其中的磷酸铁锂材料。 再用 150公斤蒸熘水洗涤 2遍。 以上所有的操作环境温度和 溶液温度为 25°C。洗涤后的磷酸铁锂材料。在 200°C真空条件烘干到恒重(完全干燥), 得到最终产品。  Lithium ion battery cathode material lithium iron phosphate treatment method, firstly prepared 100 kg 0.1% concentration of ethanol water solution. After mixing, slowly add 10 kg of lithium iron phosphate powder material to stir into a uniform suspension. Then, 50 kg of a nitric acid solution having a pH of 0 was prepared, and the nitric acid solution was slowly added to the lithium iron phosphate suspension under stirring, and the pH of the final solution was 2.5%. After reaching the set pH value, the mixture was stirred for 1 hour, and then the solution was filtered to filter out the lithium iron phosphate material therein. Wash twice with 150 kg of distilled water. All of the above operating ambient temperatures and solution temperatures are 25 °C. The washed lithium iron phosphate material. Dry at 200 ° C under vacuum to constant weight (completely dried) to obtain the final product.
实施例 2  Example 2
锂离子电池正极材料磷酸铁锂的处理方法, 首先配制 1000公斤 3%浓度的丁酮水溶 液。配好后,缓慢加入 1000公斤磷酸铁锂粉体材料搅拌成均匀的悬浊液。然后配制 4000 公斤 pH值为 1的硝酸溶液, 将硝酸溶液在搅拌状态下缓慢加入到磷酸铁锂悬浊液中, 以最终溶液的 PH值达到 1. 5为准。 到达设定的 pH值后, 搅拌 3小时, 然后将溶液过 滤, 滤出其中的磷酸铁锂材料。 再用 20000公斤蒸熘水分次洗涤 2遍。 以上所有的操作 环境温度和溶液温度为 15°C。 洗涤后的磷酸铁锂材料。 在 200°C氩气气体气氛下烘干到 恒重 (完全干燥) , 得到最终产品。  For the treatment of lithium iron phosphate as a positive electrode material for lithium ion batteries, firstly, 1000 kg of a 3% concentration of butanone aqueous solution is prepared. After the preparation, slowly add 1000 kg of lithium iron phosphate powder material to stir into a uniform suspension. Then, 4000 kg of a nitric acid solution having a pH of 1 was prepared, and the nitric acid solution was slowly added to the lithium iron phosphate suspension under stirring, and the pH of the final solution was 1.5. After reaching the set pH value, the mixture was stirred for 3 hours, and then the solution was filtered, and the lithium iron phosphate material was filtered off. Wash twice with 20,000 kg of steamed water. All of the above operating ambient and solution temperatures are 15 °C. The washed lithium iron phosphate material. Dry to 200 ° C under an argon atmosphere to constant weight (completely dried) to obtain the final product.
实施例 3  Example 3
锂离子电池正极材料磷酸铁锂的处理方法, 首先配制 500 公斤 1%浓度的甲醇水溶 液。 配好后, 缓慢加入 100公斤磷酸铁锂粉体材料搅拌成均匀的悬浊液。 配制 600公斤 pH值为 0. 5的草酸溶液,将草酸溶液在搅拌状态下缓慢加入到磷酸铁锂悬浊液中, 以最 终溶液的 pH值达到 2. 0为准。 到达设定的 pH值后, 搅拌 2小时, 然后将溶液过滤, 滤出其中的磷酸铁锂材料。 再用 1500公斤蒸熘水洗涤 2遍。 以上所有的操作环境温度 和溶液温度为 25°C。洗涤后的磷酸铁锂材料。在 200°C真空条件烘干到恒重(完全干燥), 得到最终产品。  For the treatment of lithium iron phosphate cathode material lithium iron phosphate, first prepare 500 kg of 1% methanol aqueous solution. After the preparation, slowly add 100 kg of lithium iron phosphate powder material to stir into a uniform suspension. Prepare 600 kg of oxalic acid solution with a pH of 0.5, and slowly add the oxalic acid solution to the lithium iron phosphate suspension under stirring, with the pH of the final solution reaching 2. 0. After reaching the set pH value, the mixture was stirred for 2 hours, and then the solution was filtered to filter out the lithium iron phosphate material therein. Wash twice with 1500 kg of distilled water. All of the above operating ambient temperatures and solution temperatures are 25 °C. The washed lithium iron phosphate material. Dry at 200 ° C under vacuum to constant weight (completely dried) to obtain the final product.
本发明制得的磷酸铁锂正极材料, 经过了酸洗涤, 表面高活性铁离子大幅度减少。 在组装成磷酸铁锂电池后, 正极的铁溶出大幅度减少, 有效提高了电池的搁置寿命和高 温性能。  The lithium iron phosphate cathode material prepared by the invention has been subjected to acid washing, and the surface active iron ions are greatly reduced. After being assembled into a lithium iron phosphate battery, the iron dissolution of the positive electrode is greatly reduced, and the battery life and high temperature performance are effectively improved.

Claims

权利要求书 Claim
1. 一种锂离子电池正极材料磷酸铁锂的处理方法, 其特征是: 锂离子电池正极材 料磷酸铁锂的处理过程包括: A lithium ion battery cathode material lithium iron phosphate treatment method, characterized in that: lithium ion battery cathode material lithium iron phosphate processing process includes:
1 ) 、 磷酸铁锂材料的润湿处理: 首先用 0.1-3%重量百分比浓度的润湿剂处理磷酸 铁锂材料, 使包覆碳的磷酸铁锂材料形成均匀的水性悬浊液;  1), the wetting treatment of the lithium iron phosphate material: firstly treating the lithium iron phosphate material with a wetting agent of 0.1-3% by weight, so that the carbon-coated lithium iron phosphate material forms a uniform aqueous suspension;
2) 、 用酸溶液浸出磷酸铁锂表面的高活性铁离子: 将 pH值为 0-1的酸溶液在搅拌 状态下加入到磷酸铁锂悬浊液中, 使最终溶液的 pH值保持在 1.5-2.5之间, 搅拌使体系 充分反应;  2), leaching high-activity iron ions on the surface of lithium iron phosphate with an acid solution: adding an acid solution having a pH of 0-1 to a suspension of lithium iron phosphate under stirring to maintain the pH of the final solution at 1.5 Between -2.5, stirring to fully react the system;
3 ) 、 过滤烘干: 溶液过滤, 滤出的磷酸铁锂用蒸熘水或纯净水洗涤; 洗涤后的磷 酸铁锂材料, 真空条件或保护性气体气氛下烘干, 得到最终的磷酸铁锂材料。  3), filter drying: solution filtration, filtered lithium iron phosphate washed with distilled water or purified water; washed lithium iron phosphate material, vacuum or protective gas atmosphere to dry, to obtain the final lithium iron phosphate material.
2. 按照权利要求 1所述的锂离子电池正极材料磷酸铁锂的处理方法, 其特征是: 润湿剂为乙醇、 甲醇、 丙酮或丁酮有机溶剂。  2. The method for treating a lithium ion battery cathode material lithium iron phosphate according to claim 1, wherein the wetting agent is an organic solvent of ethanol, methanol, acetone or methyl ethyl ketone.
3. 按照权利要求 1或 2所述的锂离子电池正极材料磷酸铁锂的处理方法, 其特征 是: 润湿剂处理磷酸铁锂材料时, 磷酸铁锂材料与润湿溶液的重量比为 1 : 1-10。  The method for treating a lithium iron battery positive electrode material lithium iron phosphate according to claim 1 or 2, wherein: the weight ratio of the lithium iron phosphate material to the wetting solution is 1 when the wetting agent treats the lithium iron phosphate material. : 1-10.
4. 按照权利要求 1所述的锂离子电池正极材料磷酸铁锂的处理方法, 其特征是: 酸溶液中的酸为硝酸和草酸。  4. The method for treating a lithium ion battery cathode material lithium iron phosphate according to claim 1, wherein the acid in the acid solution is nitric acid and oxalic acid.
5. 按照权利要求 4或 5所述的锂离子电池正极材料磷酸铁锂的处理方法, 其特征 是: 酸溶液和磷酸铁锂悬浊液的重量比为 1 : 0.5-2, 最终溶液的 pH值保持在 1.5-2.5之 间时搅拌 1-3小时。  The method for treating a lithium ion battery cathode material lithium iron phosphate according to claim 4 or 5, wherein the weight ratio of the acid solution to the lithium iron phosphate suspension is 1: 0.5-2, and the pH of the final solution Stir for 1-3 hours while maintaining the value between 1.5 and 2.5.
6. 按照权利要求 1所述的锂离子电池正极材料磷酸铁锂的处理方法, 其特征是: 保护性气体为氮气、 氩气、 氦气或它们中的一种或几种的混合气体。  6. The method for treating a lithium iron battery positive electrode material lithium iron phosphate according to claim 1, wherein the protective gas is nitrogen gas, argon gas, helium gas or a mixed gas of one or more of them.
7. 按照权利要求 1所述的锂离子电池正极材料磷酸铁锂的处理方法, 其特征是: 滤出的磷酸铁锂用磷酸铁锂材料重量 10-20倍的蒸熘水或纯净水洗涤 2遍, 操作控制温 度为 10-25 °C。  7. The method for treating a lithium ion battery cathode material lithium iron phosphate according to claim 1, wherein the filtered lithium iron phosphate is washed with distilled iron or purified water having a weight of 10-20 times of lithium iron phosphate material. The operating control temperature is 10-25 °C.
8. 按照权利要求 1所述的锂离子电池正极材料磷酸铁锂的处理方法, 其特征是: 真空条件或保护性气体气氛下烘干温度为 180— 250°C。  8. The method for treating a lithium ion battery cathode material lithium iron phosphate according to claim 1, wherein the drying temperature is 180 to 250 ° C under vacuum or a protective gas atmosphere.
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