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Method and apparatus for producing positive electrode active material for secondary battery

A positive electrode active material and secondary battery technology, applied in chemical instruments and methods, chemical/physical/physicochemical processes, nickel compounds, etc., can solve the problem of uneven particle size and composition, reduced productivity, retention time and reaction time. Changes and other issues, to achieve the effect of easy particle size control, uniform particle size, and improved productivity

Active Publication Date: 2020-10-16
LG CHEM LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0009] Generally, the advantage of the CSTR method is that it is easy to control the metal composition ratio, but the limitation of the CSTR method is that since the raw material input and the product discharge are performed simultaneously and continuously, the retention time and the reaction time of the positive electrode active material formed in the reactor may vary. Varies, and the resulting particles may be non-uniform in size and composition
[0010] Thus, there is a tendency to adopt a batch method that can facilitate particle size control and prepare a positive electrode active material precursor with a uniform particle size, but it is difficult to prepare a positive electrode active material with a uniform particle size distribution even with a batch reactor precursors, and the productivity may be significantly lower compared to the CSTR method

Method used

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  • Method and apparatus for producing positive electrode active material for secondary battery
  • Method and apparatus for producing positive electrode active material for secondary battery
  • Method and apparatus for producing positive electrode active material for secondary battery

Examples

Experimental program
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Effect test

Embodiment 1

[0120] NiSO 4 、CoSO 4 and MnSO 4 The nickel:cobalt:manganese molar ratio was mixed in water in an amount of 80:10:10 to prepare a transition metal-containing solution with a concentration of 2M. The reactor containing the transition metal-containing solution was connected to a 20 L batch reactor set at 60°C. Additionally, prepare 25 wt% aqueous NaOH and 15 wt% NH 4 OH aqueous solution and connect them to batch reactors respectively.

[0121] 4 L of deionized water was put into the batch reactor, and then the reactor was purged with nitrogen gas at a rate of 2 L / min to remove dissolved oxygen in the water and create a non-oxidizing atmosphere in the reactor. Afterwards, 25 ml of 50 wt% aqueous NaOH and 500 ml of 15 wt% NH 4 OH aqueous solution, and then stirred at a speed of 500 rpm and a temperature of 55° C. to maintain a pH of 12.2.

[0122] Afterwards, the transition metal-containing solution, NaOH aqueous solution and NH 4 OH aqueous solution, and reacted for 30 min...

Embodiment 2

[0125] As a solution containing transition metals, NiSO 4 、CoSO 4 and MnSO 4 Mix in water in such an amount that the molar ratio of nickel:cobalt:manganese is 95:2.5:2.5 to prepare a first transition metal-containing solution with a concentration of 2M, and NiSO 4 、CoSO 4 and MnSO 4Nickel:cobalt:manganese was mixed in water in such an amount that the molar ratio of nickel:cobalt:manganese was 50:25:25 to prepare a second transition metal-containing solution having a concentration of 2M. A first transition metal-containing solution reactor and a second transition metal-containing solution reactor containing the first transition metal-containing solution and a second transition metal-containing solution, respectively, are connected to the static mixer, respectively, and the divided A batch reactor (20 L) was connected to the outlet side of the static mixer. Additionally, prepare 25 wt% aqueous NaOH and 15 wt% NH 4 OH aqueous solution and connect them to the reactor respect...

Embodiment 3

[0129] When the batch reactor (20 L) was full, the addition of the transition metal-containing solution, aqueous NaOH and NH 4 OH aqueous solution, the reaction slurry in the batch reactor is conveyed to the hydrocyclone through the transfer line by the pump, and the concentrated The reaction slurry was then introduced into the batch reactor. Except after the concentrated reaction slurry was reintroduced into the batch reactor until the reactants in the batch reactor reached 4L, by adding the transition Metal solutions, NaOH aqueous solution and NH 4 OH aqueous solution to initiate the reaction, prepare Ni in the same manner as in Example 1 0.8 co 0.1 mn 0.1 (OH) 2 precursor.

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Abstract

The present invention provides a method for producing a positive electrode active material for a secondary battery, the method comprising the steps of: 1) forming positive electrode active material precursor particles while feeding a reaction solution into a batch type reactor, the reaction solution comprising: a transition metal-containing solution containing transition metal positive ions; an aqueous basic solution; and an ammonium ion-containing solution; 2) discharging a portion of the reaction slurry inside the reactor when the reactor is full, and feeding the discharged reaction slurry into a hydrocyclone; 3) centrifugally separating the reaction slurry, fed into the hydrocyclone, into a supernatant and a concentrated reaction slurry containing the positive electrode active materialprecursor particles; and 4) discharging the supernatant to the outside, and re-feeding the concentrated reaction slurry into the reactor to regrow the positive electrode active material precursor particles.

Description

technical field [0001] Cross References to Related Applications [0002] This application claims the benefit of Korean Patent Application No. 10-2018-0024859 filed in the Korean Intellectual Property Office on February 28, 2018, the disclosure of which is incorporated herein by reference in its entirety. technical field [0003] The invention relates to a method and equipment for preparing positive electrode active materials for secondary batteries. Background technique [0004] With the technological development and increase in demand for mobile devices, the demand for secondary batteries as energy sources has significantly increased. Among these secondary batteries, lithium secondary batteries having high energy density, high voltage, long cycle life, and low self-discharge rate have been commercialized and widely used. [0005] Lithium transition metal oxides have been used as positive electrode active materials for lithium secondary batteries, and among these oxide...

Claims

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Application Information

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IPC IPC(8): C01G53/00B01J19/00
CPCB01J19/00C01G53/00C01G53/006B01J19/0066B01J2219/00164B01J2219/00029
Inventor 郑元植崔相洵孙山铢郑志勋
Owner LG CHEM LTD
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