Methods of Preparing Positive Electrode Active Material Precursor For Lithium Secondary Battery And Positive Electrode Active Material

Patent metadata

Field	Value
Publication number	US-2019214628-A1
Application number	US-201816333378-A
Country	US
Kind code	A1
Filing date	Feb 6, 2018
Priority date	Feb 6, 2017
Publication date	Jul 11, 2019
Grant date	—

Abstract

A method of preparing a positive electrode active material precursor for a lithium secondary battery by using a batch-type reactor, which includes the steps of 1) forming positive electrode active material precursor particles while continuously adding a transition metal-containing solution including a transition metal cation, an aqueous alkaline solution, and an ammonium ion-containing solution to a batch-type reactor, 2) sedimenting the positive electrode active material precursor particles formed; 3) discharging a supernatant formed after the sedimentation of the positive electrode active material precursor particles to an outside; 4) adjusting a pH to 10 to 12 by adding the ammonium ion-containing solution; and 5) growing the positive electrode active material precursor particles while continuously again adding the transition metal-containing solution to the batch-type reactor, and a method of preparing a positive electrode active material using the same.

First claim

1 . A method of preparing a positive electrode active material precursor for a lithium secondary battery by using a batch-type reactor, the method comprising:
(1) forming positive electrode active material precursor particles while continuously adding a transition metal-containing solution including a transition metal cation, an aqueous alkaline solution, and an ammonium ion-containing solution to the batch-type reactor; (2) stopping the addition of the solutions when the batch-type reactor is full and sedimenting the positive electrode active material precursor particles formed; (3) discharging a supernatant formed after the sedimentation of the positive electrode active material precursor particles to an outside; (4) adjusting a pH, which has been reduced in the discharging of the supernatant, to 10 to 12 by adding the ammonium ion-containing solution; and (5) growing the positive electrode active material precursor particles while continuously again adding the transition metal-containing solution including a transition metal cation, the aqueous alkaline solution, and the ammonium ion-containing solution to the batch-type reactor.

2 . The method of claim 1 , wherein, in (3), when the positive electrode active material precursor particles are sedimented, stirring is performed at 5 rpm to 50 rpm.

3 . The method of claim 1 , wherein addition rates of the transition metal-containing solution, the aqueous alkaline solution, and the ammonium ion-containing solution in (1) satisfy Equation 1:
2( V−v )/ t≤υ 1 +υ 2 +υ 3 ≤30( V−v )/ t   [Equation 1]
wherein, in Equation 1, V is a volume (mL) of the batch-type reactor, v is a volume (mL) of the solution filled in the batch-type reactor before the continuous addition of the transition metal-containing solution, t is total reaction time (minutes), υ 1 is an addition rate (mL/min) of the transition metal-containing solution, υ 2 is an addition rate (mL/min) of the aqueous alkaline solution, and υ 3 is an addition rate (mL/min) of the ammonium ion-containing solution.

4 . The method of claim 1 , wherein the ammonium ion-containing solution comprises at least one selected from the group consisting of NH 4 OH, (NH 4 ) 2 SO 4 , NH 4 NO 3 , NH 4 Cl, CH 3 COONH 4 , and NH 4 CO 3 .

5 . The method of claim 1 , wherein the forming of the positive electrode active material precursor particles in (1) comprises:
(a) forming particle nucleus through a co-precipitation reaction at a pH of 11 to 13 by adjusting amounts of the aqueous alkaline solution and ammonium ion-containing solution added, and (b) after the forming of the nucleus, growing the particles through a co-precipitation reaction at a pH of 8 to 12 by adjusting amounts of the aqueous alkaline solution and ammonium ion-containing solution added.

6 . The method of claim 1 , wherein the transition metal-containing solution in (1) comprises a cation of at least one transition metal selected from the group consisting of nickel (Ni), manganese (Mn), and cobalt (Co).

7 . The method of claim 1 , wherein the transition metal-containing solution in (1) comprises a first transition metal-containing solution including cations of two or more transition metals and a second transition metal-containing solution including cations of two or more transition metals but having concentrations of the transition metal cations which are different from those of the first transition metal-containing solution.

8 . The method of claim 7 , wherein positive electrode active material precursor particles having a concentration gradient are formed by gradually decreasing an addition rate of the first transition metal-containing solution and gradually increasing an addition rate of the second transition metal-containing solution.

9 . The method of claim 8 , wherein, during the formation of the positive electrode active material precursor particles having a concentration gradient, a pH in the batch-type reactor satisfies Equation 2:
pH 0 −([ Ni ] 0 −[ Ni ] t1 )×0.05≤pH t1 ≤pH 0 −([ Ni ] 0 −[ Ni ] t1 )×0.005  [Equation 2]
wherein, in Formula 2, pH t1 is a pH in the reactor at time t1, pH 0 is an initial pH in the reactor, [Ni] 0 is a molar concentration of Ni in the transition metal-containing solution initially added, and [Ni] t1 is a molar concentration of Ni in the transition metal-containing solution added at time t1.

10 . The method of claim 9 , wherein the pH in the batch-type reactor is controlled by an addition flow of the aqueous alkaline solution, and the addition flow of the aqueous alkaline solution satisfies Equation 3:
υ 2,0 ×{1−(0.01×([ Ni ] 0 −[ Ni ] t2 ))}≤υ 2,t2 <υ 2,0   [Equation 3]
wherein, in Formula 3, υ 2,t2 is an addition flow of the aqueous alkaline solution at time t2, υ 2,0 is an initial addition flow of the aqueous alkaline solution, [Ni] 0 is a molar concentration of Ni in the transition metal-containing solution initially added, and [Ni] t2 is a molar concentration of Ni in the transition metal-containing solution added at time t2.

11 . The method of claim 1 , wherein the aqueous alkaline solution comprises at least one selected from the group consisting of a hydrate of an alkali metal, a hydroxide of an alkali metal, a hydrate of an alkaline earth metal, and a hydroxide of an alkaline earth metal.

12 . The method of claim 1 , wherein, after (5), (2) to (5) are repeatedly performed.

13 . The method of claim 1 , wherein yield of the method of preparing a positive electrode active material precursor is improved by 100% to 3,000% in comparison to when a positive electrode active material precursor is prepared by using the same-sized batch-type reactor without sedimenting the positive electrode active material precursor particles and removing the supernatant.

14 . The method of claim 1 , wherein the finally formed positive electrode active material precursor particles have a (D 90 −D 10 )/D 50 of 1.2 or less.

15 . A method of preparing a positive electrode active material for a lithium secondary battery, the method comprising sintering after mixing the positive electrode active material precursor prepared according to any one of claim 1 with a lithium-containing raw material.

Assignees

• Lg Chemical Ltd

Inventors

• Choi Sang Soon
• Park Hyun Ah
• Jung Won Sig

Classifications

• H01M4/525

  of mixed oxides or hydroxides containing iron, cobalt or nickel for inserting or intercalating light metals, e.g. LiNiO2, LiCoO2 or LiCoOxFy · CPC title

• H01M4/505

  of mixed oxides or hydroxides containing manganese for inserting or intercalating light metals, e.g. LiMn2O4 or LiMn2OxFy · CPC title

• C01P2004/51

  Particles with a specific particle size distribution · CPC title

• H01M4/0471 Primary

  involving thermal treatment, e.g. firing, sintering, backing particulate active material, thermal decomposition, pyrolysis · CPC title

• C01G53/50

  of the type (MnO2)n-, e.g. Li(NixMn1-x)O2 or Li(MyNixMn1-x-y)O2 · CPC title