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Preparation method of rate type lithium iron phosphate

A technology of lithium iron phosphate and rate, which is applied in the field of preparation of rate-type lithium iron phosphate, can solve the problems of incapable of large-scale industrialization, high energy consumption, and high degree of automation, and achieve the goal of increasing mileage, low energy consumption, and environment optimization Effect

Active Publication Date: 2020-08-18
HEFEI GUOXUAN HIGH TECH POWER ENERGY CO LTD CO LTD
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0004] In view of this, it is necessary for the present invention to provide a method for preparing a rate-type lithium iron phosphate. By improving the traditional process, especially the optimization of the particle size and sintering curve, the preparation method can prepare a rate-type iron phosphate Lithium, and the preparation method has a high degree of automation, can be compatible with energy-type lithium iron phosphate equipment, does not require equipment modification, is very suitable for large-scale industrialization, and solves the problems of high energy consumption and inability in the existing rate-type lithium iron phosphate production process. Technical problems of large-scale industrialization

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  • Preparation method of rate type lithium iron phosphate

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preparation example Construction

[0033] The invention discloses a preparation method of rate type lithium iron phosphate, comprising the following steps:

[0034] Adding carbon source and phosphorus iron source into deionized water for mixed reaction to obtain slurry A;

[0035] Add lithium source and additives to the slurry A, and use mechanical stirring and self-circulation system to run together for 3-5 hours to form slurry B. During the operation, the reaction temperature is controlled at 25-41 ° C. The viscosity of the slurry B The control range does not exceed 180mPa·S, preferably 50-180mPa·S;

[0036] Grinding the slurry B to a nano-sized slurry C by a sand mill system;

[0037] Removing the moisture of the slurry C by dynamic drying to obtain the material D;

[0038] The material D is crystallized by six-stage sintering in a protective atmosphere to obtain a sintered material. The protective atmosphere is nitrogen or an inert gas. It can be understood that the inert gas here is conventionally used i...

Embodiment 1

[0053] Glucose and ferric phosphate are added to deionized water according to the mass fraction of carbon source: phosphorus and iron source being 10%, and mixed to prepare slurry A;

[0054] Add lithium carbonate and tetrabutyl titanate (1000ppm) into the slurry A according to the molar ratio Li / Fe=1.035, mechanically stir and run the self-circulation system together for 3 hours to form a uniformly mixed slurry B. The temperature of the reaction process is controlled at 25-41 °C, the viscosity control range of slurry B does not exceed 180mPa·s;

[0055] Grind slurry B to D50 = 0.35 μm slurry C through a sand mill system;

[0056] After the slurry C is spray-dried, the water content of the material is removed to reach the particle size range of D50=8μm;

[0057] The six heating times of the dried material are: 230°C for the first stage, 250°C for the second stage, 450°C for the third stage, 580°C for the fourth stage, 580°C for the fifth stage, and 680°C for the sixth stage. ...

Embodiment 2

[0062] Glucose and ferric phosphate are added to deionized water according to the mass fraction of carbon source: phosphorus and iron source being 11%, and mixed to prepare slurry A;

[0063] According to the molar ratio Li / Fe=1.035, add lithium carbonate + lithium hydroxide composite lithium salt and titanium dioxide (5000ppm) into the slurry A for mechanical stirring and self-circulation system to run together for 3 hours to form a uniformly mixed slurry B, and the temperature of the reaction process is controlled At 25-41°C, the viscosity control range of slurry B does not exceed 180mPa·s;

[0064] Grind slurry B to D50 = 0.3 μm slurry C through a sand milling system;

[0065] After the slurry C is spray-dried, the water content of the material is removed to reach the particle size range of D50=7.5 μm;

[0066] The six heating times of the dried material are: 230°C for the first stage, 250°C for the second stage, 450°C for the third stage, 580°C for the fourth stage, 580°C...

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Abstract

A preparation method of rate type lithium iron phosphate comprises the following steps of adding a carbon source and a phosphorus iron source into deionized water, mixing and reacting to obtain slurryA; adding the lithium source and the additive into the slurry A, and meanwhile adopting mechanical stirring and a self-circulation system for jointly operating for 3-5 h to form slurry B; grinding the slurry B into nano-sized slurry C through a sanding system; removing the moisture of the slurry C through dynamic drying to obtain a material D; carrying out the crystallization reaction on the material D in a protective atmosphere by adopting six-stage sintering to obtain a sintered material; and crushing the sintered material to obtain the rate type lithium iron phosphate. The preparation method can be used for preparing the rate type lithium iron phosphate, is high in automation degree, can be compatible with the energy type lithium iron phosphate device, does not need the device transformation, and is very suitable for large-scale industrialization.

Description

technical field [0001] The invention belongs to the field of lithium ion batteries, and in particular relates to a preparation method of rate-type lithium iron phosphate. Background technique [0002] The rapid development of new energy vehicles has put forward higher and higher requirements for the power battery technology of key core components. The power battery requires not only maintaining a certain capacity, but also maintaining a certain rate performance to meet people's travel convenience. requirements. Among them, lithium iron phosphate battery has always been the development direction of power battery because of its low price, long life and high safety. With the development of long-distance transportation, the demand for fast charging and discharging has become, and the development and industrialization of high-rate lithium iron phosphate to meet the expectation of cruising range has become a research direction. [0003] The conductivity of lithium iron phosphate...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): H01M4/58H01M4/62H01M10/0525
CPCH01M4/5825H01M4/625H01M10/0525Y02E60/10
Inventor 饶媛媛
Owner HEFEI GUOXUAN HIGH TECH POWER ENERGY CO LTD CO LTD