WO2018129883A1 - Lithium iron phosphate/carbon composite material and preparation method therefor - Google Patents

Lithium iron phosphate/carbon composite material and preparation method therefor Download PDF

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WO2018129883A1
WO2018129883A1 PCT/CN2017/092314 CN2017092314W WO2018129883A1 WO 2018129883 A1 WO2018129883 A1 WO 2018129883A1 CN 2017092314 W CN2017092314 W CN 2017092314W WO 2018129883 A1 WO2018129883 A1 WO 2018129883A1
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iron phosphate
lithium
carbon composite
lithium iron
composite material
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PCT/CN2017/092314
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French (fr)
Chinese (zh)
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陈立鹏
汪龙
柳娜
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宁德时代新能源科技股份有限公司
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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/362Composites
    • 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
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B32/00Carbon; Compounds thereof
    • C01B32/05Preparation or purification of carbon not covered by groups C01B32/15, C01B32/20, C01B32/25, C01B32/30
    • 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
    • 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
    • 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
    • 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
    • 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
    • C01P2002/00Crystal-structural characteristics
    • C01P2002/70Crystal-structural characteristics defined by measured X-ray, neutron or electron diffraction data
    • C01P2002/72Crystal-structural characteristics defined by measured X-ray, neutron or electron diffraction data by d-values or two theta-values, e.g. as X-ray diagram
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2004/00Particle morphology
    • C01P2004/01Particle morphology depicted by an image
    • C01P2004/03Particle morphology depicted by an image obtained by SEM
    • 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 field of lithium ion batteries, and more particularly to a lithium iron phosphate/carbon composite material and a preparation method thereof.
  • lithium iron phosphate material As a positive electrode material for lithium ion batteries, lithium iron phosphate material has the advantages of abundant raw material source, low price, green environmental protection, high theoretical specific capacity (about 170 mAh/g), long life, good safety and thermal stability, and is currently commercialized.
  • the preparation of lithium iron phosphate material mainly uses high energy wet grinding equipment to grind and pulverize iron orthophosphate and lithium salt to realize nanocrystallization of lithium iron phosphate material.
  • the production cost of this preparation method is high, which limits its development.
  • the specific performances are as follows: 1) raw materials belong to specific fields of fine processing products, non-chemical application fields are bulk products, and raw material costs are high; 2) existing wet grinding
  • the preparation of lithium iron phosphate material has higher energy consumption, but the production capacity is relatively low. 3)
  • the equipment and auxiliary materials of the existing wet grinding process belong to wearing parts and consumables, and the production investment is large.
  • the object of the present invention is to overcome the deficiencies of the prior art and provide a lithium iron phosphate/carbon composite material which is low in cost, ideal in performance, and suitable for industrial production, and a preparation method thereof.
  • the present invention provides a method for preparing a lithium iron phosphate/carbon composite material, which comprises the following steps:
  • the iron fine powder has a particle size of 5 to 30 ⁇ m
  • the phosphoric acid is a concentrated phosphoric acid having a concentration of 70 to 85%.
  • the molar ratio of the Fe fine powder to the Fe and P elements in the concentrated phosphoric acid is 1:1.
  • the acidification additive is at least one of oxalic acid, citric acid, tartaric acid and oxalic acid, and the content thereof is iron fine powder. 5 to 15% of the mass.
  • step 1) a doping metal compound is further added, and the molar ratio of the doping metal element M to the P element in the doped metal compound is 0.005 ⁇ 0.03:1.
  • the doping metal compound is a manganese-containing compound, a titanium-containing compound, a cobalt-containing compound, an iron-containing compound, a magnesium-containing compound, an aluminum-containing compound, and the like.
  • a chromium compound and a cerium-containing compound the doping metal compound is one or more of an oxide, a hydroxide, a nitrate, and an organic acid salt containing a doping element, and the organic acid salt is preferably vinegar. Acid salt, oxalate.
  • the acidification temperature is 50 to 150 ° C, and the acidification time is 4 to 8 hours.
  • the molar ratio of the Li to the P element is 1.02:1.
  • the lithium-containing compound comprises lithium carbonate, lithium hydroxide monohydrate, lithium acetate, lithium nitrate, lithium citrate, preferably one. Lithium hydroxide in water.
  • the organic carbon source is one or more of maltose, glucose, sucrose, fructose, starch, phenolic resin, The amount added is 5 to 15% of the mass of the iron fine powder.
  • the sintering temperature is 650 to 750 ° C, and the sintering time is 4 to 8 hours.
  • the present invention also provides a lithium iron phosphate/carbon composite material which is produced according to the method for producing lithium iron phosphate/carbon composite material of the present invention.
  • the preparation method of the lithium iron phosphate/carbon composite material of the invention directly adopts the iron acid powder and phosphoric acid for acidification and reflux reaction, and then mixes the lithium salt and the carbon source, and is dried to obtain an organic carbon source composite lithium iron phosphate precursor.
  • the sintered lithium iron phosphate/carbon composite material has the following advantages: 1) a wide range of raw materials and low cost, the raw materials involved are low-cost bulk chemical products; 2) the product has good crystal structure and less impurities.
  • Fig. 1 is an XRD chart of a lithium iron phosphate/carbon composite material obtained in Example 1 of the present invention.
  • Example 2 is an SEM image of a lithium iron phosphate/carbon composite material obtained in Example 1 of the present invention.
  • Fig. 3 is a graph showing the first discharge specific capacity of the lithium iron phosphate/carbon composite material obtained in Example 1 and Comparative Example 1 of the present invention.
  • the three-necked bottle was placed in an oil bath, heated to 50 ° C, and acidified and refluxed at this temperature for 4 hours;
  • the collected precursors were sintered at 650 ° C for 4 hours, and pulverized and sieved to obtain a low-cost lithium iron phosphate/carbon composite material.
  • Example 1 is an X-ray diffraction (XRD) pattern of a lithium iron phosphate/carbon composite material according to Example 1 of the present invention, and the XRD pattern shows that the lithium iron phosphate/carbon composite material obtained in Example 1 has good crystallinity and high purity, and is not There is an impurity peak.
  • 2 is an SEM image of a lithium iron phosphate/carbon composite material according to Embodiment 1 of the present invention. As can be seen from FIG. 2, the lithium iron phosphate/carbon composite material prepared in Example 1 of the present invention is a nano particle, and the particle size thereof. evenly distributed.
  • the lithium iron phosphate/carbon composite material prepared in Example 1 was mixed with a conductive agent carbon black (Super P) and a binder PVDF at a mass ratio of 90:5:5 to form a slurry, uniformly coated on an aluminum foil current collector.
  • the positive electrode membrane is made up, the lithium metal sheet is used as the negative electrode, the polypropylene microporous membrane is used as the separator, and the lithium hexafluorophosphate is used as the electrolyte.
  • the half-cell is assembled in the argon-protected glove box, and the prepared half-cell is subjected to charge and discharge test. .
  • Example 3 is a graph of the first discharge specific capacity of the lithium iron phosphate/carbon composite material obtained in Example 1 of the present invention, As can be seen from Fig. 3, the half-cell 0.1C first discharge specific capacity is 150 mAh/g, and the 1C first discharge specific capacity is 140 mAh/g.
  • the steps of the examples 2 to 5 are basically the same as those of the first embodiment, wherein the quality of the iron fine powder and lithium hydroxide monohydrate is the same as that of the first embodiment, and the use amount and preparation process parameters of the respective materials different from the first embodiment are different. See Tables 1-3 for the results of the first discharge specific capacity test of each of the examples.
  • Figure 3 is a broken line diagram of the first discharge specific capacity of the lithium iron phosphate/carbon composite prepared in Comparative Example 1. As can be seen from Figure 3, Comparative Example 1 0.1C and 1C of lithium iron phosphate/carbon composite. The first discharge specific capacity was 137 mAh/g and 118 mAh/g, respectively.
  • Example 1 and Comparative Example 1 According to the first discharge specific capacity results of Example 1 and Comparative Example 1, it can be seen that although the raw materials involved in the two methods are the same, the final results are different because different processes are employed.
  • the acidizing reflow technique employed in the first to fifth embodiments of the present invention is superior to the comparative example 1 in the high energy wet ball milling technique, and the first discharge specific capacities of 0.1C and 1C of Examples 1 to 5 are higher than that of Comparative Example 1, which is better.
  • the conductivity is also low during the preparation process using the acidified reflux technology of Examples 1 to 5.
  • the acid reflow technology is not only simple in process, but also has better performance of the prepared lithium iron phosphate/carbon composite material, and has a good market application prospect.
  • the preparation method of the lithium iron phosphate/carbon composite material of the present invention is to directly carry out an acid reflux reaction using iron fine powder and phosphoric acid, and then mix the lithium salt and The carbon source, the organic iron source composite lithium iron phosphate precursor is dried, and finally the lithium iron phosphate/carbon composite material is sintered, which has the following advantages: 1) the raw material source is wide, the cost is low, and the raw materials involved are low-cost.
  • the product has good crystal structure, less impurities, uniform particle size and excellent electrochemical performance; 3)
  • the preparation process is simple and practical, and the acid precipitation reaction process is used to react the iron powder with phosphoric acid to prepare nanoparticles. It replaces the traditional high-energy wet grinding and pulverization nano-fabrication process; 4)
  • the equipment has low operating cost, and only needs to support the atmospheric pressure reflux reaction device, avoiding the use of high-value, difficult-to-maintain wet-grinding equipment and auxiliary materials, and easy to realize large-scale industrial production. .
  • the acidified refluxed slurry is not a complete single substance solution form, but a nanoparticle emulsion of the mixture.
  • the acidification reaction does not require all the reactions, and only the large particle iron powder is partially acidified, so that the large particle skeleton structure is loose and pulverized into small particles, that is, the ferrous iron and the acid in the iron powder react with each other to make the large particle powder.
  • the components of the small particles are ferrous oxide, Fe 3 O 4 , ferrous phosphate, iron phosphate and the like.
  • the acidifying additive is only exemplified by oxalic acid, citric acid or oxalic acid, according to other embodiments of the present invention, the acidifying additive may also be tartaric acid or A combination of the foregoing acidifying additives.
  • the organic carbon source has been described by taking only maltose, glucose, sucrose, and fructose as an example in the embodiment of the present invention, the organic carbon source may be starch, phenol resin or the like according to other embodiments of the present invention. A combination of organic carbon sources.
  • the compound doped with the metal element M is described by way of example only in the examples of the present invention, manganese dioxide, magnesium oxide, titanium dioxide, and cobalt trioxide, the doping metal according to other embodiments of the present invention.
  • the compound may also be an iron-containing compound, an aluminum-containing compound, a chromium-containing compound, a cerium-containing compound or a combination of the foregoing doped metal compounds;
  • the doping metal compound is an oxide containing a doping element, hydrogen Oxide, nitrate, organic acid salt or a combination thereof.
  • the lithium-containing compound is exemplified by lithium hydroxide monohydrate as an example in the embodiment of the present invention
  • the lithium-containing compound may also be lithium carbonate, lithium acetate or lithium nitrate. , lithium citrate or a combination of the foregoing lithium-containing compounds.

Abstract

A preparation method for a lithium iron phosphate/carbon composite material, comprising the following steps: 1) weighing iron powder, phosphoric acid, and an acidifying additive, and dispersing the same in deionized water; 2) heating to perform an acidification reflux reaction; 3) after the acidification reflux reaction ends, adding a lithium-containing compound and an organic carbon source to perform mixing and dispersion; 4) stirring and evaporation drying the mixture to obtain a lithium iron phosphate precursor which is composited by the organic carbon source; and 5) sintering the collected precursor, pulverizing and screening, and then obtaining the lithium iron phosphate/carbon composite material. Relative to the existing technology, said preparation method for the lithium iron phosphate/carbon composite material has the following advantages: 1) the raw materials have wide sources and are low cost; 2) the product has a good crystalline structure, few impurities, and even granularity, and has ideal electrochemical properties; 3) the preparation process is simple and practical, equipment running costs are low, and large scale industrial production is easily achieved.

Description

磷酸铁锂/碳复合材料及其制备方法Lithium iron phosphate/carbon composite material and preparation method thereof 技术领域Technical field
本发明属于锂离子电池领域,更具体地说,本发明涉及一种磷酸铁锂/碳复合材料及其制备方法。The invention belongs to the field of lithium ion batteries, and more particularly to a lithium iron phosphate/carbon composite material and a preparation method thereof.
背景技术Background technique
作为锂离子电池的正极材料,磷酸铁锂材料具有原料来源丰富、价格低廉、绿色环保、理论比容量高(约170mAh/g)、寿命长、安全和热稳定性好等优点,是目前商业化汽车动力电池的首选正极材料。As a positive electrode material for lithium ion batteries, lithium iron phosphate material has the advantages of abundant raw material source, low price, green environmental protection, high theoretical specific capacity (about 170 mAh/g), long life, good safety and thermal stability, and is currently commercialized. The preferred cathode material for automotive power batteries.
目前,磷酸铁锂材料的制备主要采用高能湿法研磨设备对正磷酸铁和锂盐进行研磨粉碎,实现磷酸铁锂材料的纳米化。但是,这种制备方法生产成本较高,限制了其发展,具体表现在:1)原料属于特定领域精细加工产品,非化工应用领域大宗化产品,原料成本较高;2)现有湿法研磨制备磷酸铁锂材料能耗较高,但产能又比较低;3)现有湿法研磨工艺所配套的设备和辅材属于易损件和消耗品,生产投入大。At present, the preparation of lithium iron phosphate material mainly uses high energy wet grinding equipment to grind and pulverize iron orthophosphate and lithium salt to realize nanocrystallization of lithium iron phosphate material. However, the production cost of this preparation method is high, which limits its development. The specific performances are as follows: 1) raw materials belong to specific fields of fine processing products, non-chemical application fields are bulk products, and raw material costs are high; 2) existing wet grinding The preparation of lithium iron phosphate material has higher energy consumption, but the production capacity is relatively low. 3) The equipment and auxiliary materials of the existing wet grinding process belong to wearing parts and consumables, and the production investment is large.
有鉴于此,确有必要提供一种成本低廉、性能理想、适合工业化生产的磷酸铁锂/碳复合材料及其制备方法。In view of this, it is indeed necessary to provide a lithium iron phosphate/carbon composite material which is low in cost, ideal in performance, and suitable for industrial production, and a preparation method thereof.
发明内容Summary of the invention
本发明的目的在于:克服现有技术的不足,提供一种成本低廉、性能理想、适合工业化生产的磷酸铁锂/碳复合材料及其制备方法。The object of the present invention is to overcome the deficiencies of the prior art and provide a lithium iron phosphate/carbon composite material which is low in cost, ideal in performance, and suitable for industrial production, and a preparation method thereof.
为了实现上述发明目的,本发明提供了一种磷酸铁锂/碳复合材料的制备方法,其包括以下步骤:In order to achieve the above object, the present invention provides a method for preparing a lithium iron phosphate/carbon composite material, which comprises the following steps:
1)称取铁精粉、磷酸和酸化添加剂,分散于去离子水中; 1) Weigh iron powder, phosphoric acid and acidification additives, and disperse in deionized water;
2)加热进行酸化回流反应;2) heating to carry out an acid reflux reaction;
3)酸化回流反应结束后,加入含锂化合物和有机碳源进行混合分散;3) after the acidification reflux reaction is completed, the lithium-containing compound and the organic carbon source are added for mixing and dispersion;
4)将混料进行搅拌蒸干得有机碳源复合的磷酸铁锂前躯物;以及4) stirring and evaporating the mixture to obtain an organic carbon source composite lithium iron phosphate precursor;
5)将收集到的前躯物进行烧结,粉碎过筛后获得磷酸铁锂/碳复合材料。5) The collected precursors are sintered, pulverized and sieved to obtain lithium iron phosphate/carbon composite material.
作为本发明磷酸铁锂/碳复合材料的制备方法的一种改进,步骤1)中,所述铁精粉的粒径尺寸为5~30μm,所述磷酸为浓度为70~85%的浓磷酸,所述铁精粉与浓磷酸中Fe与P元素的摩尔比为1:1。As an improvement of the preparation method of the lithium iron phosphate/carbon composite material of the present invention, in the step 1), the iron fine powder has a particle size of 5 to 30 μm, and the phosphoric acid is a concentrated phosphoric acid having a concentration of 70 to 85%. The molar ratio of the Fe fine powder to the Fe and P elements in the concentrated phosphoric acid is 1:1.
作为本发明磷酸铁锂/碳复合材料的制备方法的一种改进,步骤1)中,所述酸化添加剂为草酸、柠檬酸、酒石酸、乙二酸中的至少一种,其含量为铁精粉质量的5~15%。As an improvement of the preparation method of the lithium iron phosphate/carbon composite material of the present invention, in the step 1), the acidification additive is at least one of oxalic acid, citric acid, tartaric acid and oxalic acid, and the content thereof is iron fine powder. 5 to 15% of the mass.
作为本发明磷酸铁锂/碳复合材料的制备方法的一种改进,步骤1)中,还加入掺杂金属化合物,掺杂金属化合物中的掺杂金属元素M与P元素的摩尔比为0.005~0.03:1。As an improvement of the preparation method of the lithium iron phosphate/carbon composite material of the present invention, in step 1), a doping metal compound is further added, and the molar ratio of the doping metal element M to the P element in the doped metal compound is 0.005~ 0.03:1.
作为本发明磷酸铁锂/碳复合材料的制备方法的一种改进,所述掺杂金属化合物为含锰化合物、含钛化合物、含钴化合物、含铁化合物、含镁化合物、含铝化合物、含铬化合物、含铌化合物中的一种或多种,掺杂金属化合物为含掺杂元素的氧化物、氢氧化物、硝酸盐、有机酸盐中的一种或多种,有机酸盐优选醋酸盐、草酸盐。As an improvement of the preparation method of the lithium iron phosphate/carbon composite material of the present invention, the doping metal compound is a manganese-containing compound, a titanium-containing compound, a cobalt-containing compound, an iron-containing compound, a magnesium-containing compound, an aluminum-containing compound, and the like. One or more of a chromium compound and a cerium-containing compound, the doping metal compound is one or more of an oxide, a hydroxide, a nitrate, and an organic acid salt containing a doping element, and the organic acid salt is preferably vinegar. Acid salt, oxalate.
作为本发明磷酸铁锂/碳复合材料的制备方法的一种改进,步骤2)中,所述酸化温度为50~150℃,酸化时间为4~8小时。As an improvement of the preparation method of the lithium iron phosphate/carbon composite material of the present invention, in the step 2), the acidification temperature is 50 to 150 ° C, and the acidification time is 4 to 8 hours.
作为本发明磷酸铁锂/碳复合材料的制备方法的一种改进,步骤3)中,所述Li与P元素的摩尔比为1.02:1。As an improvement of the preparation method of the lithium iron phosphate/carbon composite material of the present invention, in the step 3), the molar ratio of the Li to the P element is 1.02:1.
作为本发明磷酸铁锂/碳复合材料的制备方法的一种改进,步骤3)中,所述含锂化合物包括碳酸锂、一水氢氧化锂、醋酸锂、硝酸锂、柠檬酸锂,优选一 水氢氧化锂。As an improvement of the preparation method of the lithium iron phosphate/carbon composite material of the present invention, in the step 3), the lithium-containing compound comprises lithium carbonate, lithium hydroxide monohydrate, lithium acetate, lithium nitrate, lithium citrate, preferably one. Lithium hydroxide in water.
作为本发明磷酸铁锂/碳复合材料的制备方法的一种改进,步骤3)中,所述有机碳源为麦芽糖、葡萄糖、蔗糖、果糖、淀粉、酚醛树脂中的一种或多种,其添加量为铁精粉质量的5~15%。As an improvement of the preparation method of the lithium iron phosphate/carbon composite material of the present invention, in the step 3), the organic carbon source is one or more of maltose, glucose, sucrose, fructose, starch, phenolic resin, The amount added is 5 to 15% of the mass of the iron fine powder.
作为本发明磷酸铁锂/碳复合材料的制备方法的一种改进,步骤5)中,所述烧结温度为650~750℃,烧结时间为4~8小时。As an improvement of the preparation method of the lithium iron phosphate/carbon composite material of the present invention, in the step 5), the sintering temperature is 650 to 750 ° C, and the sintering time is 4 to 8 hours.
为了实现上述发明目的,本发明还提供了一种磷酸铁锂/碳复合材料,其根据本发明磷酸铁锂/碳复合材料的制备方法制得。In order to achieve the above object, the present invention also provides a lithium iron phosphate/carbon composite material which is produced according to the method for producing lithium iron phosphate/carbon composite material of the present invention.
相对于现有技术,本发明磷酸铁锂/碳复合材料的制备方法直接采用铁精粉和磷酸进行酸化回流反应,然后混合锂盐和碳源,干燥得有机碳源复合的磷酸铁锂前躯物,最后烧结得磷酸铁锂/碳复合材料,具有以下优点:1)原料来源广泛、成本低廉,所涉及的原料均为低成本的大宗化工产品;2)产品晶体结构好、杂质较少、粒度均匀,具有优异的电化学性能;3)制备工艺简单实用,采用酸化回流反应工艺,使铁精粉和磷酸反应制得纳米颗粒,取代传统的高能湿法研磨粉碎纳米化工艺;4)设备运行成本低,只需配套常压回流反应装置,避免使用高价值,难维护的湿法研磨设备和辅材,易于实现大规模工业化生产。Compared with the prior art, the preparation method of the lithium iron phosphate/carbon composite material of the invention directly adopts the iron acid powder and phosphoric acid for acidification and reflux reaction, and then mixes the lithium salt and the carbon source, and is dried to obtain an organic carbon source composite lithium iron phosphate precursor. Finally, the sintered lithium iron phosphate/carbon composite material has the following advantages: 1) a wide range of raw materials and low cost, the raw materials involved are low-cost bulk chemical products; 2) the product has good crystal structure and less impurities. Uniform particle size, excellent electrochemical performance; 3) Simple and practical preparation process, using acid reflux reaction process to make iron powder and phosphoric acid react to produce nanoparticles, replacing traditional high-energy wet grinding and pulverization nano-processing; 4) Equipment Low operating cost, only need to support the atmospheric pressure reflux reaction device, avoid the use of high-value, difficult to maintain wet grinding equipment and auxiliary materials, easy to achieve large-scale industrial production.
附图说明DRAWINGS
下面结合说明书附图和具体实施方式,对本发明磷酸铁锂/碳复合材料及其制备方法进行详细说明,其中:The lithium iron phosphate/carbon composite material of the present invention and a preparation method thereof are described in detail below with reference to the accompanying drawings and specific embodiments, wherein:
图1为本发明实施例1所制得的磷酸铁锂/碳复合材料的XRD谱图。BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is an XRD chart of a lithium iron phosphate/carbon composite material obtained in Example 1 of the present invention.
图2为本发明实施例1所制得的磷酸铁锂/碳复合材料的SEM图。2 is an SEM image of a lithium iron phosphate/carbon composite material obtained in Example 1 of the present invention.
图3为本发明实施例1和对比例1所制得的磷酸铁锂/碳复合材料的首次放电比容量曲线图。 Fig. 3 is a graph showing the first discharge specific capacity of the lithium iron phosphate/carbon composite material obtained in Example 1 and Comparative Example 1 of the present invention.
具体实施方式detailed description
为了使本发明的发明目的、技术方案及其有益技术效果更加清晰,以下结合附图和具体实施方式,对本发明进行进一步详细说明。应当理解的是,本说明书中描述的具体实施方式仅仅是为了解释本发明,并非为了限定本发明。The present invention will be further described in detail below in conjunction with the drawings and specific embodiments. The specific embodiments described in the specification are to be construed as illustrative only and not limiting.
实施例1Example 1
将D50为10μm的77.18g铁精粉,1.3g二氧化锰,115.29g浓磷酸(85%),3.86g草酸和57.65g去离子水依次加入三口瓶中,以400rpm速度分散,得到悬浮液;77.18 g of iron fine powder having a D50 of 10 μm, 1.3 g of manganese dioxide, 115.29 g of concentrated phosphoric acid (85%), 3.86 g of oxalic acid and 57.65 g of deionized water were sequentially added to a three-necked flask, and dispersed at a speed of 400 rpm to obtain a suspension;
将三口瓶置于油浴锅中,加热到50℃,在此温度下酸化回流反应4小时;The three-necked bottle was placed in an oil bath, heated to 50 ° C, and acidified and refluxed at this temperature for 4 hours;
向三口瓶中加入42.78g一水氢氧化锂和3.86g麦芽糖,以1500rpm速度分散1小时,待反应结束后,关闭冷却回流;42.78 g of lithium hydroxide monohydrate and 3.86 g of maltose were added to the three-necked flask, and dispersed at 1500 rpm for 1 hour. After the reaction was completed, the cooling and reflux were closed;
将混料搅拌蒸干,得到有机碳源复合的磷酸铁锂前躯物;The mixture is stirred and evaporated to obtain an organic iron source composite lithium iron phosphate precursor;
将所收集到的前躯物在650℃下烧结4小时,粉碎过筛后得低成本的磷酸铁锂/碳复合材料。The collected precursors were sintered at 650 ° C for 4 hours, and pulverized and sieved to obtain a low-cost lithium iron phosphate/carbon composite material.
图1为本发明实施例1中磷酸铁锂/碳复合材料的X射线衍射(XRD)图,XRD图谱表明,实施例1所得到的磷酸铁锂/碳复合材料结晶度好,纯度高,不存在杂质峰。图2为本发明实施例1中磷酸铁锂/碳复合材料的SEM图,从图2中可以看出,本发明实施例1所制备的磷酸铁锂/碳复合材料为纳米颗粒,其颗粒尺寸分布均匀。1 is an X-ray diffraction (XRD) pattern of a lithium iron phosphate/carbon composite material according to Example 1 of the present invention, and the XRD pattern shows that the lithium iron phosphate/carbon composite material obtained in Example 1 has good crystallinity and high purity, and is not There is an impurity peak. 2 is an SEM image of a lithium iron phosphate/carbon composite material according to Embodiment 1 of the present invention. As can be seen from FIG. 2, the lithium iron phosphate/carbon composite material prepared in Example 1 of the present invention is a nano particle, and the particle size thereof. evenly distributed.
将实施例1所制备得到的磷酸铁锂/碳复合材料与导电剂炭黑(Super P)和粘结剂PVDF按质量比90:5:5混合配成浆料,均匀涂敷在铝箔集流体上制成正极膜片,以金属锂片为负极,聚丙烯微孔膜为隔膜,六氟磷酸锂为电解液,在氩气保护的手套箱内组装成半电池,将制成的半电池进行充放电测试。图3实线a为本发明实施例1所制得的磷酸铁锂/碳复合材料的首次放电比容量曲线图, 从图3中可以看出,半电池0.1C首次放电比容量为150mAh/g,1C首次放电比容量为140mAh/g。The lithium iron phosphate/carbon composite material prepared in Example 1 was mixed with a conductive agent carbon black (Super P) and a binder PVDF at a mass ratio of 90:5:5 to form a slurry, uniformly coated on an aluminum foil current collector. The positive electrode membrane is made up, the lithium metal sheet is used as the negative electrode, the polypropylene microporous membrane is used as the separator, and the lithium hexafluorophosphate is used as the electrolyte. The half-cell is assembled in the argon-protected glove box, and the prepared half-cell is subjected to charge and discharge test. . 3 is a graph of the first discharge specific capacity of the lithium iron phosphate/carbon composite material obtained in Example 1 of the present invention, As can be seen from Fig. 3, the half-cell 0.1C first discharge specific capacity is 150 mAh/g, and the 1C first discharge specific capacity is 140 mAh/g.
实施例2~5的步骤与实施例1基本相同,其中,铁精粉、一水氢氧化锂的质量与实施例1相同,各实施例与实施例1不同的相关物质使用量、制备工艺参数和各实施例的首次放电比容量测试结果参见表1~3。The steps of the examples 2 to 5 are basically the same as those of the first embodiment, wherein the quality of the iron fine powder and lithium hydroxide monohydrate is the same as that of the first embodiment, and the use amount and preparation process parameters of the respective materials different from the first embodiment are different. See Tables 1-3 for the results of the first discharge specific capacity test of each of the examples.
对比例1Comparative example 1
分别称取D50为10μm的77.18g铁精粉,1.3g二氧化锰,115.29g浓磷酸(85%),42.78g一水氢氧化锂,3.86g草酸,3.86g麦芽糖和57.65g去离子水;将上述原料以1400rpm研磨速度进行高能湿法球磨4小时;进行喷雾干燥得磷酸铁锂前躯体;将前躯体在650℃下烧结4小时,粉碎过筛后得磷酸铁锂/碳复合材料。77.18g iron fine powder, 1.3g manganese dioxide, 115.29g concentrated phosphoric acid (85%), 42.78g lithium hydroxide monohydrate, 3.86g oxalic acid, 3.86g maltose and 57.65g deionized water with D50 of 10μm were weighed respectively. The above raw materials were subjected to high-energy wet ball milling at a polishing rate of 1400 rpm for 4 hours; spray drying was carried out to obtain a lithium iron phosphate precursor; the precursor was sintered at 650 ° C for 4 hours, and pulverized and sieved to obtain a lithium iron phosphate/carbon composite material.
图3虚线b为对比例1所制得的磷酸铁锂/碳复合材料的首次放电比容量曲线图,从图3中可以看出,对比例1磷酸铁锂/碳复合材料的0.1C和1C首次放电比容量分别为137mAh/g、118mAh/g。Figure 3 is a broken line diagram of the first discharge specific capacity of the lithium iron phosphate/carbon composite prepared in Comparative Example 1. As can be seen from Figure 3, Comparative Example 1 0.1C and 1C of lithium iron phosphate/carbon composite. The first discharge specific capacity was 137 mAh/g and 118 mAh/g, respectively.
表1、实施例1~5与对比例1的相关物质使用量Table 1, Examples 1 to 5 and Comparative Example 1 use of related substances
Figure PCTCN2017092314-appb-000001
Figure PCTCN2017092314-appb-000001
表2、实施例1~5与对比例1的制备工艺参数Table 2, Preparation Process Parameters of Examples 1 to 5 and Comparative Example 1
Figure PCTCN2017092314-appb-000002
Figure PCTCN2017092314-appb-000002
表3、实施例1~5与对比例1的首次放电比容量测试结果Table 3, first discharge specific capacity test results of Examples 1 to 5 and Comparative Example 1
Figure PCTCN2017092314-appb-000003
Figure PCTCN2017092314-appb-000003
根据实施例1和对比例1首次放电比容量结果可以看出,虽然两种方法所涉及到的原料相同,但因为采用了不同的工艺,最终的结果也不相同。本发明实施例1至5采用的酸化回流技术与对比例1采用高能湿法球磨技术相比,实施例1至5的0.1C和1C首次放电比容量都要高于对比例1,具有更好的导电性,而且在制备过程中,使用实施例1至5的酸化回流技术运行成本更低。通过对比分析可知,酸化回流技术不仅工艺简单,而且制得的磷酸铁锂/碳复合材料的性能更理想,具有很好的市场应用前景。 According to the first discharge specific capacity results of Example 1 and Comparative Example 1, it can be seen that although the raw materials involved in the two methods are the same, the final results are different because different processes are employed. The acidizing reflow technique employed in the first to fifth embodiments of the present invention is superior to the comparative example 1 in the high energy wet ball milling technique, and the first discharge specific capacities of 0.1C and 1C of Examples 1 to 5 are higher than that of Comparative Example 1, which is better. The conductivity is also low during the preparation process using the acidified reflux technology of Examples 1 to 5. Through comparative analysis, it can be seen that the acid reflow technology is not only simple in process, but also has better performance of the prepared lithium iron phosphate/carbon composite material, and has a good market application prospect.
结合以上对本发明实施例和对比例的详细描述可知,相对于现有技术,本发明磷酸铁锂/碳复合材料的制备方法是直接采用铁精粉和磷酸进行酸化回流反应,然后混合锂盐和碳源,干燥得有机碳源复合的磷酸铁锂前躯物,最后烧结得磷酸铁锂/碳复合材料,具有以下优点:1)原料来源广泛、成本低廉,所涉及的原料均为低成本的大宗化工产品;2)产品晶体结构好、杂质较少、粒度均匀,具有优异的电化学性能;3)制备工艺简单实用,采用酸化回流反应工艺,使铁精粉和磷酸反应制得纳米颗粒,取代传统的高能湿法研磨粉碎纳米化工艺;4)设备运行成本低,只需配套常压回流反应装置,避免使用高价值,难维护的湿法研磨设备和辅材,易于实现大规模工业化生产。In combination with the above detailed description of the examples and comparative examples of the present invention, it can be seen that, compared with the prior art, the preparation method of the lithium iron phosphate/carbon composite material of the present invention is to directly carry out an acid reflux reaction using iron fine powder and phosphoric acid, and then mix the lithium salt and The carbon source, the organic iron source composite lithium iron phosphate precursor is dried, and finally the lithium iron phosphate/carbon composite material is sintered, which has the following advantages: 1) the raw material source is wide, the cost is low, and the raw materials involved are low-cost. Bulk chemical products; 2) The product has good crystal structure, less impurities, uniform particle size and excellent electrochemical performance; 3) The preparation process is simple and practical, and the acid precipitation reaction process is used to react the iron powder with phosphoric acid to prepare nanoparticles. It replaces the traditional high-energy wet grinding and pulverization nano-fabrication process; 4) The equipment has low operating cost, and only needs to support the atmospheric pressure reflux reaction device, avoiding the use of high-value, difficult-to-maintain wet-grinding equipment and auxiliary materials, and easy to realize large-scale industrial production. .
需要说明的是,在酸化回流反应的过程中,酸化回流后的浆料并不是完全的单一物质溶液形态,而是混合物的纳米颗粒乳液。酸化反应并不需要全部反应,只需将大颗粒铁精粉通过部分酸化反应,使得大颗粒骨架结构疏松,粉化成小颗粒,即将铁精粉中的二价铁和酸反应,使得大颗粒粉化,来实现大颗粒变为小颗粒的纳米化过程,其中,小颗粒的成份为氧化亚铁、Fe3O4、磷酸亚铁、磷酸铁等。It should be noted that during the acidification reflux reaction, the acidified refluxed slurry is not a complete single substance solution form, but a nanoparticle emulsion of the mixture. The acidification reaction does not require all the reactions, and only the large particle iron powder is partially acidified, so that the large particle skeleton structure is loose and pulverized into small particles, that is, the ferrous iron and the acid in the iron powder react with each other to make the large particle powder. In order to realize the nanometerization process of large particles into small particles, the components of the small particles are ferrous oxide, Fe 3 O 4 , ferrous phosphate, iron phosphate and the like.
需要进一步说明的是,虽然在本说明书的实施例中仅以草酸、柠檬酸、乙二酸为例对酸化添加剂进行了说明,但是,根据本发明的其他实施例,酸化添加剂也可以是酒石酸或前述酸化添加剂的组合。此外,虽然本发明的实施例中仅以麦芽糖、葡萄糖、蔗糖、果糖为例对有机碳源进行了说明,但是,根据本发明的其他实施例,有机碳源也可以是淀粉、酚醛树脂或前述有机碳源的组合。再者,虽然本发明的实施例中仅以二氧化锰、氧化镁、二氧化钛、四氧化三钴为例对掺杂有金属元素M的化合物进行了说明,但是,根据本发明的其他实施例,掺杂金属化合物也可以是含铁化合物、含铝化合物、含铬化合物、含铌化合物或前述掺杂金属化合的组合;掺杂金属化合物为含掺杂元素的氧化物、氢 氧化物、硝酸盐、有机酸盐或其组合。最后,虽然本发明的实施例中仅以一水氢氧化锂为例对含锂化合物进行了说明,但是,根据本发明的其他实施例,含锂化合物也可以是碳酸锂、醋酸锂、硝酸锂、柠檬酸锂或前述含锂化合物的组合。It should be further noted that although in the examples of the present specification, the acidifying additive is only exemplified by oxalic acid, citric acid or oxalic acid, according to other embodiments of the present invention, the acidifying additive may also be tartaric acid or A combination of the foregoing acidifying additives. Further, although the organic carbon source has been described by taking only maltose, glucose, sucrose, and fructose as an example in the embodiment of the present invention, the organic carbon source may be starch, phenol resin or the like according to other embodiments of the present invention. A combination of organic carbon sources. Furthermore, although the compound doped with the metal element M is described by way of example only in the examples of the present invention, manganese dioxide, magnesium oxide, titanium dioxide, and cobalt trioxide, the doping metal according to other embodiments of the present invention. The compound may also be an iron-containing compound, an aluminum-containing compound, a chromium-containing compound, a cerium-containing compound or a combination of the foregoing doped metal compounds; the doping metal compound is an oxide containing a doping element, hydrogen Oxide, nitrate, organic acid salt or a combination thereof. Finally, although the lithium-containing compound is exemplified by lithium hydroxide monohydrate as an example in the embodiment of the present invention, according to other embodiments of the present invention, the lithium-containing compound may also be lithium carbonate, lithium acetate or lithium nitrate. , lithium citrate or a combination of the foregoing lithium-containing compounds.
根据上述说明书的揭示和指导,本发明所属技术领域的技术人员还可以对上述实施方式进行适当的变更和修改。因此,本发明并不局限于上面揭示和描述的具体实施方式,对本发明的一些修改和变更也应当落入本发明的权利要求的保护范围内。此外,尽管本说明书中使用了一些特定的术语,但这些术语只是为了方便说明,并不对本发明构成任何限制。 The above embodiments may be modified and modified as appropriate by those skilled in the art in light of the above disclosure. Therefore, the invention is not limited to the specific embodiments disclosed and described herein, and the modifications and variations of the invention are intended to fall within the scope of the appended claims. In addition, although specific terms are used in the specification, these terms are merely for convenience of description and do not limit the invention.

Claims (11)

  1. 一种磷酸铁锂/碳复合材料的制备方法,其特征在于,包括以下步骤:A method for preparing a lithium iron phosphate/carbon composite material, comprising the steps of:
    1)称取铁精粉、磷酸和酸化添加剂,分散于去离子水中;1) Weigh iron powder, phosphoric acid and acidification additives, and disperse in deionized water;
    2)加热进行酸化回流反应;2) heating to carry out an acid reflux reaction;
    3)酸化回流反应结束后,加入含锂化合物和有机碳源进行混合分散;3) after the acidification reflux reaction is completed, the lithium-containing compound and the organic carbon source are added for mixing and dispersion;
    4)将混料进行搅拌蒸干得有机碳源复合的磷酸铁锂前躯物;以及4) stirring and evaporating the mixture to obtain an organic carbon source composite lithium iron phosphate precursor;
    5)将收集到的前躯物进行烧结,粉碎过筛后获得磷酸铁锂/碳复合材料。5) The collected precursors are sintered, pulverized and sieved to obtain lithium iron phosphate/carbon composite material.
  2. 根据权利要求1所述的磷酸铁锂/碳复合材料的制备方法,其特征在于,步骤1)中,所述铁精粉的粒径尺寸为5~30μm,所述磷酸为浓度为70~85%的浓磷酸,所述铁精粉与浓磷酸中Fe与P元素的摩尔比为1:1。The method for preparing a lithium iron phosphate/carbon composite according to claim 1, wherein in the step 1), the iron fine powder has a particle size of 5 to 30 μm, and the phosphoric acid has a concentration of 70 to 85. % of concentrated phosphoric acid, the molar ratio of Fe to P in the iron fine powder and concentrated phosphoric acid is 1:1.
  3. 根据权利要求1所述的磷酸铁锂/碳复合材料的制备方法,其特征在于,步骤1)中,所述酸化添加剂为草酸、柠檬酸、酒石酸、乙二酸中的至少一种,其含量为铁精粉质量的5~15%。The method for preparing a lithium iron phosphate/carbon composite material according to claim 1, wherein in the step 1), the acidifying additive is at least one of oxalic acid, citric acid, tartaric acid and oxalic acid. It is 5 to 15% of the quality of iron fine powder.
  4. 根据权利要求1所述的磷酸铁锂/碳复合材料的制备方法,其特征在于,步骤1)中,还加入掺杂金属化合物,掺杂金属化合物中的掺杂金属元素M与P元素的摩尔比为0.005~0.03:1。The method for preparing a lithium iron phosphate/carbon composite material according to claim 1, wherein in step 1), a doping metal compound is added, and a molar ratio of the doping metal element M and the P element in the doping metal compound is further added. The ratio is 0.005 to 0.03:1.
  5. 根据权利要求4所述的磷酸铁锂/碳复合材料的制备方法,其特征在于,所述掺杂金属化合物为含锰化合物、含钛化合物、含钴化合物、含铁化合物、含镁化合物、含铝化合物、含铬化合物、含铌化合物中的一种或多种,掺杂金属化合物为含掺杂元素的氧化物、氢氧化物、硝酸盐、有机酸盐中的一种或多种。The method for preparing a lithium iron phosphate/carbon composite according to claim 4, wherein the dopant metal compound is a manganese-containing compound, a titanium-containing compound, a cobalt-containing compound, an iron-containing compound, a magnesium-containing compound, and a One or more of an aluminum compound, a chromium-containing compound, and a cerium-containing compound, and the doping metal compound is one or more of an oxide, a hydroxide, a nitrate, and an organic acid salt containing a doping element.
  6. 根据权利要求1所述的磷酸铁锂/碳复合材料的制备方法,其特征在于,步骤2)中,所述酸化温度为50~150℃,酸化时间为4~8小时。The method for preparing a lithium iron phosphate/carbon composite according to claim 1, wherein in the step 2), the acidification temperature is 50 to 150 ° C, and the acidification time is 4 to 8 hours.
  7. 根据权利要求1所述的磷酸铁锂/碳复合材料的制备方法,其特征在于, 步骤3)中,所述Li与P元素摩尔比为1.02:1。The method for preparing a lithium iron phosphate/carbon composite according to claim 1, wherein In the step 3), the molar ratio of the Li to the P element is 1.02:1.
  8. 根据权利要求1所述的磷酸铁锂/碳复合材料的制备方法,其特征在于,步骤3)中,所述含锂化合物包括碳酸锂、一水氢氧化锂、醋酸锂、硝酸锂、柠檬酸锂,优选一水氢氧化锂。The method for preparing a lithium iron phosphate/carbon composite according to claim 1, wherein in the step 3), the lithium-containing compound comprises lithium carbonate, lithium hydroxide monohydrate, lithium acetate, lithium nitrate, and citric acid. Lithium, preferably lithium hydroxide monohydrate.
  9. 根据权利要求1所述的磷酸铁锂/碳复合材料的制备方法,其特征在于,步骤3)中,所述有机碳源为麦芽糖、葡萄糖、蔗糖、果糖、淀粉、酚醛树脂或其组合,其添加量为铁精粉质量的5~15%。The method for preparing a lithium iron phosphate/carbon composite according to claim 1, wherein in the step 3), the organic carbon source is maltose, glucose, sucrose, fructose, starch, phenolic resin or a combination thereof. The amount added is 5 to 15% of the mass of the iron fine powder.
  10. 根据权利要求1所述的磷酸铁锂/碳复合材料的制备方法,其特征在于,步骤5)中,所述烧结温度为650~750℃,烧结时间为4~8小时。The method for producing a lithium iron phosphate/carbon composite according to claim 1, wherein in the step 5), the sintering temperature is 650 to 750 ° C, and the sintering time is 4 to 8 hours.
  11. 一种磷酸铁锂/碳复合材料,其特征在于,所述磷酸铁锂/碳复合材料根据权利要求1~10中任意一项所述的制备方法制得。 A lithium iron phosphate/carbon composite material, characterized in that the lithium iron phosphate/carbon composite material is produced according to the production method according to any one of claims 1 to 10.
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