Silicon-Infiltrated Battery Particles With Controlled CVI Temperature Gradient

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Solution Overview

Problem

Existing chemical vapor infiltration (CVI) methods for producing electroactive materials in porous particles suffer from uncontrolled silicon deposition on reactor surfaces, leading to flaking and product inhomogeneity, which is exacerbated by high reactor surface area-to-particle mass ratios and temperature differentials, hindering large-scale production.

Innovation Solution

A process and system that control the temperature differential (ΔT) between reactor surfaces and porous particles to ≤+90°C, using preheating and mechanical agitation to ensure silicon deposition primarily occurs within the pores of the particles, reducing flaking and improving homogeneity.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Ease of manufacture

If low concentrations of silane (1.25 vol %) are used in CVI, then the deposition process is easier to control, but the production time becomes unacceptable for large-scale manufacture

Engineering Contradiction:
Improvecontrol of deposition processVSAvoidproduction time
Core Design Contradiction:
Ease of manufactureVSProductivity

Solution Approach 1:

The patent changes the concentration parameter of the silicon-containing precursor from low (1.25 vol %) to high (at least 25 vol %), which dramatically reduces production time while maintaining controlled deposition through the temperature differential mechanism

Inventive Principle:
Principle #35Parameter changes

2Productivity

If high concentrations of silicon-containing precursor are used, then production time is reduced, but uncontrolled soiling of the reaction zone occurs with large silicon flakes forming on internal surfaces

Engineering Contradiction:
Improveproduction timeVSAvoidhomogeneity of silicon deposition
Core Design Contradiction:
ProductivityVSManufacturing precision

Solution Approach 1:

The patent creates different temperature conditions in different locations: the porous particles are maintained at a lower temperature (ΔT ≤ +90°C relative to reactor surfaces) which promotes controlled silicon deposition, while the reactor internal surfaces are at higher temperature which prevents flake formation. This local temperature differentiation enables high precursor concentration to be used without soiling

Inventive Principle:
Principle #3Local quality

Solution Approach 2:

The porous particles are preheated to a controlled temperature before exposure to the high concentration silicon-containing precursor gas. This preliminary temperature setting ensures that when the precursor contacts the particles, silicon deposits uniformly within the pores rather than forming flakes on reactor surfaces

Inventive Principle:
Principle #10Preliminary action

3Temperature

If a high ratio of reactor surface area to mass of porous particles is used, then sufficient heat transfer to particles is achieved, but the scale-up of the method is restricted

Engineering Contradiction:
Improveheat transfer to particlesVSAvoidscale-up capability
Core Design Contradiction:
TemperatureVSProductivity

Solution Approach 1:

The patent fundamentally changes the temperature parameter relationship between reactor surfaces and porous particles, maintaining ΔT ≤ +90°C. This allows scaling to larger reactor sizes without requiring proportionally larger surface areas, as the temperature control mechanism remains effective regardless of reactor scale

Inventive Principle:
Principle #35Parameter changes

4Temperature

If temperature differential between reactor surfaces and porous particles is high, then heat transfer is improved, but silicon flake formation on reactor surfaces increases

Engineering Contradiction:
Improveheat transfer efficiencyVSAvoidsilicon flake formation
Core Design Contradiction:
TemperatureVSObject-generated harmful factors

Solution Approach 1:

The patent applies preliminary anti-action by preheating the porous particles to a controlled temperature before exposing them to the silicon-containing precursor. This prevents the temperature differential from causing silicon flake formation on reactor surfaces while still allowing sufficient heat transfer for the deposition process

Inventive Principle:
Principle #9Preliminary anti-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

This approach minimizes reactor soiling and enhances product quality by ensuring uniform silicon deposition within the porous particles, enabling efficient large-scale production without interruptions.

Implementation Method 1

contacting the plurality of particles in the reaction zone with a gas comprising at least 25 vol % of a silicon-containing precursor at a temperature effective to cause deposition of silicon in the pores of the porous particles

Methodology Applied
Scientific EffectChemical Vapour Deposition: Chemical Vapour Deposition

Implementation Method 2

using preheating and mechanical agitation to ensure silicon deposition primarily occurs within the pores of the particles

Methodology Applied
Scientific EffectThermal heating: Heating

Implementation Method 3

using preheating and mechanical agitation to ensure silicon deposition primarily occurs within the pores of the particles

Methodology Applied
Scientific EffectMechanical agitation: Stirring

Data Source

PatentUS12473203B2Process for preparing electroactive materials for metal-ion batteries
Publication Date: 2025.11.18 NEXEON LTD
  • US12473203B2 patent drawing
  • US12473203B2 patent drawing
  • US12473203B2 patent drawing

AI summary

The invention relates to a process for preparing composite particles, the process comprising contacting the plurality of particles in the reaction zone with a gas comprising at least 25 vol % of a silicon-containing precursor at a temperature effective to cause deposition of silicon in the pores of the porous particles. A controlled temperature differential between the maximum temperature of the internal surfaces of the reaction zone and the simultaneous minimum temperature within the plurality of porous particles is maintained during the contacting step.