Cobalt-free precursor for lithium ion battery, positive electrode material and preparation methods of cobalt-free precursor and positive electrode material

A technology for lithium-ion batteries and positive electrode materials, applied in battery electrodes, positive electrodes, secondary batteries, etc., can solve problems such as large fluctuations in Co prices and shortage of Co resources, and achieve accelerated deintercalation, poor rate performance, and high The effect of specific capacity

Inactive Publication Date: 2020-09-11
GEM CO LTD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, in the ternary cathode material, the introduction of Co element greatly increases the manufacturing cost of the material, but because Co resources are very scarce and relatively concentrated, the price of Co fluctuates greatly. Therefore, it is nece

Method used

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  • Cobalt-free precursor for lithium ion battery, positive electrode material and preparation methods of cobalt-free precursor and positive electrode material
  • Cobalt-free precursor for lithium ion battery, positive electrode material and preparation methods of cobalt-free precursor and positive electrode material
  • Cobalt-free precursor for lithium ion battery, positive electrode material and preparation methods of cobalt-free precursor and positive electrode material

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Experimental program
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Effect test

Embodiment 1

[0024] Step 1: nickel sulfate and manganese sulfate are configured into A solution according to the molar ratio Ni:Mn=80:20, nickel sulfate and manganese sulfate are configured into B solution according to the molar ratio Ni:Mn=60:40, A solution, B solution The total concentration of nickel and manganese in the medium is 2.5mol / L.

[0025] Step 2: Add 300L of pure water, 3kg of liquid caustic soda and 40kg of ammonia water into the reaction kettle, the ammonia concentration of the bottom liquid is 5g / L, and the pH is 12.0. 1m into the reactor 3 / h of inert gas to prevent the oxidation of Mn in the reaction process, and then use a metering pump to add A solution to the reactor with a flow rate of 30kg / h. The flow rate is added to the reactor for stirring, and the stirring rate is 300rpm / min. Among them, the concentration of the added ammonia water is 7g / L, and the concentration of the added liquid caustic soda is 2.5mol / L. During the reaction process, the flow rate

Embodiment 2

[0030]Step 1: Nickel sulfate and manganese carbonate are configured into A solution according to the molar ratio Ni:Mn=85:15, nickel sulfate and manganese carbonate are configured into B solution according to the molar ratio Ni:Mn=70:30, A solution, B solution The total concentration of nickel and manganese in the medium is 3mol / L.

[0031] Step 2: Add 300L of pure water, 2.75kg of liquid caustic soda and 45kg of ammonia water into the reaction kettle, the ammonia concentration of the bottom liquid is 7g / L, and the pH is 11.8. 1m into the reactor 3 / h of inert gas to prevent the oxidation of Mn in the reaction process, and then use a metering pump to add solution A to the reactor at a flow rate of 60kg / h. Add reactor and stir, stirring rate is 250rpm / min, and wherein, the concentration of the ammoniacal liquor that adds is 9g / L, and the concentration of the liquid caustic soda that adds is 4mol / L, by controlling the flow rate of ammoniacal liquor and liquid caustic

Embodiment 3

[0036] Step 1: nickel carbonate and manganese carbonate are configured into A solution according to the molar ratio Ni:Mn=91:09, nickel carbonate and manganese carbonate are configured into B solution according to the molar ratio Ni:Mn=75:25, A solution, B solution The total concentration of nickel and manganese in the medium is 3.5mol / L.

[0037] Step 2: Add 300L of pure water, 2.5kg of liquid caustic soda and 47kg of ammonia water into the reactor to maintain the pH of the bottom liquid at 11.6 and the ammonia concentration at 8g / L. In order to pass 1m into the reactor 3 / h of inert gas to prevent the oxidation of Mn in the reaction process, and then use a metering pump to add solution A to the reactor at a flow rate of 50kg / h. Add the reaction kettle to stir, the stirring rate is 200rpm / min, wherein, the concentration of the added ammonia water is 14g / L, the concentration of the added liquid caustic soda is 4.5mol / L, adjust the system by controlling the flow of

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Abstract

The invention discloses a cobalt-free precursor for a lithium ion battery, the chemical formula of the precursor is NixMn1-x (OH) 2, 0.75 < = x < = 0.85, the particle size is 12-18 [mu] m, and the cross-sectional morphology of the particles is divergent from the center of a circle to the circumference. The invention also discloses a preparation method of the cobalt free precursor for lithium ion battery and a positive electrode material. According to the preparation method disclosed by the invention, the core-shell cobalt-free precursor with a divergent structure can be obtained, the nickel content of the inner core is higher than that of the outer shell, and the manganese content of the inner core is lower than that of the outer shell, so that a structure of which the inner core is high-nickel and low-manganese and the outer shell is high-manganese and low-nickel is formed; the high nickel of the inner core can improve the specific capacity of the material, the high manganese of the outer shell can provide smooth transition of Li < + >, and the divergent structure of the inner core particles provides a Li < + > transmission channel to accelerate de-intercalation of Li < + > and improve the rate capability of the material, so that the problem of poor rate capability caused by Co deficiency is solved; higher specific capacity, cycling stability and thermal stability can be obtained by using the precursor to prepare the positive electrode material.

Description

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Claims

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Application Information

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Owner GEM CO LTD
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