Preparation method of Ni-Co-Al ternary precursor with continuous concentration gradient

A concentration gradient, nickel-cobalt-aluminum technology, applied in chemical instruments and methods, electrical components, nickel compounds, etc., can solve the problems of complex process, poor battery cycle performance, low battery energy density, etc., and achieve simple process and good cycle performance Good, good product stability

Active Publication Date: 2019-04-02
SINOSTEEL ANHUI TIANYUAN TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

For example, Chinese patent CN103715424B discloses a core-shell structure positive electrode material and its preparation method. It first precipitates nickel and cobalt, and then deposits a layer of aluminum hydroxide on the surface. However, the aluminum layer on the surface is in the electrochemical reaction. Does not participate in the reaction, and reduces the electronic conductivity and ion diffusivity of the material, so that the capacity cannot be effectively exerted, and the energy density of the battery is low
Another example is the Chinese patent CN106207140A which discloses a method for preparing nickel-cobalt-aluminum composites with mu

Method used

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  • Preparation method of Ni-Co-Al ternary precursor with continuous concentration gradient

Examples

Experimental program
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Example Embodiment

[0028] Example 1

[0029] Prepare solution

[0030] Use deionized water to prepare a 1.5M nickel sulfate solution, a 0.5M cobalt sulfate solution, a 0.2M sodium metaaluminate solution, and a mixed solution of ammonia and sodium hydroxide. The ammonia concentration is 2M and the sodium hydroxide concentration is 4M.

[0031] reaction

[0032] Add 10L of dilute ammonia solution into the 100L reactor, and add the above solutions to the reactor in parallel flow. Adjust the concentration of nickel solution and cobalt solution at the moment the raw materials are added to the reactor: add deionized water to the nickel solution at a flow rate of 0.5L / h, and add cobalt with a concentration of 1.2M to the cobalt solution at a flow rate of 0.5L / h Solution. When the concentration of the nickel solution is 0.1M or the cobalt solution is 1M, stop adding raw materials to the reaction kettle and age for 10 hours. During the whole process, the pH of the system was 11, and the reaction temperature ...

Example Embodiment

[0036] Example 2

[0037] Prepare solution

[0038] Use deionized water to prepare 2M nickel sulfate solution, 1M cobalt sulfate solution, 0.5M sodium metaaluminate solution, and a mixed solution of ammonia and sodium hydroxide, where the concentration of ammonia is 3M and the concentration of sodium hydroxide is 6M.

[0039] reaction

[0040] 15L of dilute ammonia solution was added to the 100L reactor, and the above solutions were added to the reactor in parallel flow. Adjust the concentration of nickel solution and cobalt solution at the moment the raw materials are added to the reactor: add deionized water to the nickel solution at a flow rate of 1L / h, and add a 1M cobalt solution to the cobalt solution at a flow rate of 1L / h. When the concentration of the nickel solution is 0.1M or the cobalt solution is 1M, stop adding raw materials to the reaction kettle and age for 12h. In the whole process, the pH of the system was 11.5 and the reaction temperature was 65°C.

[0041] Post-pr...

Example Embodiment

[0044] Example 3

[0045] Prepare solution

[0046] Use deionized water to prepare 1M nickel sulfate solution, 0.3M cobalt sulfate solution, 0.3M sodium metaaluminate solution, and a mixed solution of ammonia and sodium hydroxide, where the concentration of ammonia is 1M and the concentration of sodium hydroxide is 3M .

[0047] reaction

[0048] Add 20L of dilute ammonia solution into the 100L reactor, and add the above solutions to the reactor in parallel flow. Adjust the concentration of nickel solution and cobalt solution at the moment the raw materials are added to the reactor: add deionized water to the nickel solution at a flow rate of 0.1L / h, and add cobalt with a concentration of 1.5M to the cobalt solution at a flow rate of 0.5L / h Solution. When the concentration of the nickel solution is 0.1M or the cobalt solution is 1M, stop adding raw materials to the reaction kettle and age for 24h. In the whole process, the pH of the system was 12 and the reaction temperature was 5...

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Abstract

The invention relates to the field of preparation of a lithium ion battery positive electrode material, in particular to a preparation method of a Ni-Co-Al ternary precursor with continuous concentration gradient. The preparation method is characterized by comprising the steps of (1) combining and adding a mixed solution of a nickel solution, a cobalt solution, an aluminum solution, a complexing agent and a precipitant into a reaction kettle; (2) adding deionized water into the nickel solution during the material addition process, adding a high-concentration cobalt solution into the cobalt solution until the concentration of the nickel solution is 0.1M or the concentration cobalt solution is 1M, stopping adding a raw material, constantly stirring to ensure uniform solution during the wholeprocess, controlling a pH value of a reaction system to 10.5-12 and temperature to 55-65 DEG C, and continuing to age for 6-24 hours after material addition is stopped; and (3) taking out the material for solid-liquid separation, washing and drying to obtain the Ni-Co-Al ternary precursor with continuous concentration gradient after aging.

Description

technical field [0001] The invention relates to the field of preparation of cathode materials for lithium ion batteries, in particular to a method for preparing a nickel-cobalt-aluminum ternary precursor with a continuous concentration gradient. Background technique [0002] Lithium-ion batteries have a series of advantages such as high energy density and long cycle life, and have been widely used in digital, energy storage and electric vehicles. At present, the energy density of lithium batteries is mostly 140wh / kg, and the corresponding cruising range of electric vehicles is about 300 kilometers, which is far from meeting people's requirements for long cruising range of cars. [0003] In order to develop a lithium-ion battery with higher energy density, researchers focus their work on the positive electrode material of the battery, because the performance of the positive electrode material largely determines the performance of the battery. The nickel-cobalt-aluminum terna...

Claims

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Application Information

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IPC IPC(8): H01M4/485H01M4/525H01M10/0525C01G53/00
CPCC01G53/006H01M4/485H01M4/525H01M10/0525Y02E60/10
Inventor 李涛裴晓东骆艳华钱有军佘世杰刘晨王凡陈静
Owner SINOSTEEL ANHUI TIANYUAN TECH
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