Cathode Precursor Co-Precipitation for Smaller Primary Particles

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Solution Overview

Problem

The existing methods for preparing positive electrode active material precursors for secondary batteries using batch-type reactors face limitations in reducing primary particle size and surface density, leading to non-uniformity and reduced reactivity during sintering.

Innovation Solution

A method involving a co-precipitation reaction in a batch-type reactor, where a transition metal-containing solution, a basic solution, and an ammonium solution are added, maintaining a molar ratio of ammonium ions to transition metal cations at 0.5 or less and a pH of 11.2 or less, to produce a positive electrode active material precursor with reduced primary particle size and surface density.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Ease of manufacture

If a batch-type reactor is used to prepare positive electrode active material precursor, then the control of metal composition ratio is easy, but the primary particle size increases and surface density increases as particles grow

Engineering Contradiction:
Improvecontrol of metal composition ratioVSAvoidprimary particle size
Core Design Contradiction:
Ease of manufactureVSVolume of moving object

Solution Approach 1:

The batch-type reactor process is segmented into multiple controlled stages: initial rapid nucleation phase, intermediate growth phase, and final maturation phase. Each stage uses different addition rates of raw materials and different stirring speeds to control particle development independently, preventing excessive particle growth while maintaining composition control.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The process dynamically adjusts operating parameters during reaction: stirring speed varies from high (rapid mixing during nucleation) to moderate (controlled growth), temperature is adjusted in stages, and raw material addition rates are modified over time. This dynamic control allows the system to maintain small primary particle size while achieving uniform metal composition ratio.

Inventive Principle:
Principle #15Dynamics

2Ease of manufacture

If a batch-type reactor is used to prepare positive electrode active material precursor, then the control of metal composition ratio is easy, but the density of particle surface increases as particles grow

Engineering Contradiction:
Improvecontrol of metal composition ratioVSAvoiddensity of particle surface
Core Design Contradiction:
Ease of manufactureVSQuantity of substance

Solution Approach 1:

The precipitation process is divided into distinct phases where surface density control is prioritized in early stages. Rapid nucleation creates numerous small particles with high surface area-to-volume ratio, preventing surface densification. Subsequent controlled growth maintains this surface characteristic while achieving target composition.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The process uses excessive nucleation (creating more nuclei than eventually needed) to ensure a large number of small particles form initially. This excessive nucleation action prevents surface density increase by distributing material across many particles rather than allowing a few particles to grow large and dense at the surface.

Inventive Principle:
Principle #16Partial or excessive action

3Stability of the object's composition

If the primary particle size of the precursor particle increases, then the surface energy decreases, but the reactivity with lithium source and doping source decreases during sintering

Engineering Contradiction:
Improvesurface energyVSAvoidreactivity with lithium source and doping source
Core Design Contradiction:
Stability of the object's compositionVSReliability

Solution Approach 1:

The process optimizes multiple parameters simultaneously to maintain small primary particle size: controls supersaturation level, adjusts stirring speed, modifies temperature profile, and regulates pH change rate. These parameter changes prevent particle growth that would reduce surface energy and reactivity.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The process performs preliminary nucleation under controlled conditions to create a large population of small particles before any significant growth occurs. This preliminary action establishes a particle size distribution that maintains high surface energy and reactivity throughout the subsequent sintering process with lithium and doping sources.

Inventive Principle:
Principle #10Preliminary action

Applied Scientific Principles

This section explains which scientific principles are used to turn an abstract innovation direction into a practical engineering solution.

Function Achieved in This Case

The method effectively reduces the primary particle size and surface density of the positive electrode active material precursor, improving capacity, rate capability, cycle characteristics, and resistance increase characteristics when used in lithium batteries.

Implementation Method 1

preparing a positive electrode active material precursor by a co-precipitation reaction while adding a transition metal-containing solution containing transition metal cations, a basic solution, and an ammonium solution to a batch-type reactor

Methodology Applied
Scientific EffectCo-precipitation: Coprecipitation

Data Source

PatentUS20250062336A1Positive Electrode Active Material Precursor for Secondary Battery, Preparation Method Thereof and Method of Preparing Positive Electrode Active Material
Publication Date: 2025.02.20 LG CHEM LTD
  • US20250062336A1 patent drawing
  • US20250062336A1 patent drawing
  • US20250062336A1 patent drawing

AI summary

A method of preparing a positive electrode active material precursor for a secondary battery includes preparing a positive electrode active material precursor by a co-precipitation reaction while adding a transition metal-containing solution containing transition metal cations, a basic solution, and an ammonium solution to a batch-type reactor, wherein a molar ratio of ammonium ions contained in the ammonium solution to the transition metal cations contained in the transition metal-containing solution added to the batch-type reactor is 0.5 or less, and a pH in the batch-type reactor is maintained at 11.2 or less.