Fumed Silica Aggregate Size Control via Post-Flame Segmentation

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Solution Overview

Problem

Conventional processes for producing fumed silica are limited in producing a wide range of aggregate sizes and coefficients of structure, which restricts the improvement of rheological and reinforcement properties, and dispersibility.

Innovation Solution

A process involving a stream of silica precursor and combustible gas, where fumed silica particles are formed by mixing and combusting these streams, allowing contact with dopants or controlling temperature-time profiles to achieve larger aggregate sizes and adjustable coefficients of structure.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Manufacturing precision

If conventional pyrogenic processes are used to produce fumed silica, then high purity is achieved, but aggregate size is limited to a narrow range

Engineering Contradiction:
Improveaggregate size controlVSAvoidrange of aggregate sizes
Core Design Contradiction:
Manufacturing precisionVSAdaptability or versatility

Solution Approach 1:

The invention divides the aggregate growth process into distinct stages: initial particle formation in the flame, followed by separate aggregation stages in the post-flame zone. This segmentation allows independent control of particle size and aggregate size, enabling a wider range of aggregate sizes while maintaining high purity.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The invention transitions from controlling only flame temperature to controlling both spatial dimension (flame zone vs. post-flame zone) and temporal dimension (formation stage vs. aggregation stage). This multi-dimensional control enables independent adjustment of aggregate size beyond what single-parameter flame temperature control allows.

Inventive Principle:
Principle #17Another dimension (Dimensionality change)

2Length of moving object

If flame temperature is increased to grow larger aggregates, then aggregate size increases, but surface area decreases due to particle coalescence

Engineering Contradiction:
Improveaggregate sizeVSAvoidsurface area
Core Design Contradiction:
Length of moving objectVSArea of stationary object

Solution Approach 1:

The invention performs preliminary particle formation at controlled flame temperatures to establish the primary particle size and surface area, then allows aggregation to occur in the cooler post-flame zone. This preliminary action prevents excessive coalescence during aggregation, enabling larger aggregates to form while preserving more surface area compared to conventional high-temperature processes.

Inventive Principle:
Principle #10Preliminary action

3Stability of the object's composition

If rapid cooling is applied to limit particle growth, then amorphous structure is maintained, but aggregate size is restricted

Engineering Contradiction:
Improveamorphous structureVSAvoidaggregate size
Core Design Contradiction:
Stability of the object's compositionVSLength of moving object

Solution Approach 1:

The invention segments the thermal history into distinct phases: high-temperature formation in the flame maintains amorphous structure through rapid cooling, while a separate lower-temperature aggregation phase in the post-flame zone allows aggregate growth without crystallization. This temporal segmentation enables both amorphous structure preservation and increased aggregate size.

Inventive Principle:
Principle #1Segmentation

4Ease of manufacture

If conventional processes are used, then production is simple, but rheological properties cannot be improved

Engineering Contradiction:
Improveprocess simplicityVSAvoidrheological properties
Core Design Contradiction:
Ease of manufactureVSReliability

Solution Approach 1:

The invention introduces dynamic control of aggregation conditions in the post-flame zone, allowing adjustment of aggregation kinetics through parameters such as residence time, temperature profile, and gas flow rates. This dynamic control enables optimization of rheological properties while maintaining relative process simplicity through a single reactor design.

Inventive Principle:
Principle #15Dynamics

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 process produces fumed silica with improved viscosity, dispersibility, and elastic modulus, offering enhanced rheological and reinforcement properties by achieving larger aggregate sizes and coefficients of structure.

Implementation Method 1

combusting the stream of combustible gas with the silica precursor to form a stream of combusted gas with fumed silica particles suspended therein

Methodology Applied
Scientific EffectCombustion: Combustion

Implementation Method 2

the particles are initially in a semi-liquid form and grow into aggregates up to a certain extent, depending on the flame temperature

Methodology Applied
Scientific EffectCoalescence: Coagulation

Data Source

PatentEP2364272B1Processes for manufacturing the same fumed silica of controlled aggregate size
Publication Date: 2023.12.20 CABOT CORP
  • EP2364272B1 patent drawingFigure 1
  • EP2364272B1 patent drawingFigure 2
  • EP2364272B1 patent drawingFigure 3

AI summary

The invention provides fumed silica comprising aggregates that have an aggregate size and a surface area that satisfy particular formulas relating aggregate size to surface area, as well as aggregates that exhibit particular viscosity, power law exponent index, and/or elastic modulus characteristics when dispersed in liquid media. The invention also provides processes of preparing such fumed silica by combining a silica precursor with a stream of combustible gas, combusting the stream, and producing a stream of combusted gas and fumed silica particles, wherein dopants are introduced, the time/temperature profile, or history, of the stream of combusted gas and fumed silica particles is adjusted to allow for post-quench aggregate growth, and/or additional silica precursor is introduced into the stream of combusted gas.