Uniform Silicate Nanoparticles via Micro-Mixing

Resolve Bottlenecks,
Find Innovative Solutions
Generate Solutions

Solution Overview

Problem

Scale-up of precipitation processes for inorganic powders faces challenges in maintaining uniform particle formation, mitigating mixing conditions in batch reactors, and avoiding parabolic flow issues in continuous reactors, leading to product losses and contamination.

Innovation Solution

A method involving micro-mixing of aqueous solutions of water-soluble silicate and cationic species in a branched tubular structure with static mixing elements, followed by macro-mixing in a batch reactor, under controlled pH and flow conditions, to produce uniform silicate-based nanoparticles with high uniformity and specific cation-to-silicon ratios.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Ease of operation

If batch precipitation is used, then ease of operation is improved, but manufacturing precision deteriorates due to localization and non-uniform particle formation

Engineering Contradiction:
Improveease of operationVSAvoidparticle size uniformity
Core Design Contradiction:
Ease of operationVSManufacturing precision

Solution Approach 1:

The continuous flow reactor is segmented into multiple parallel channels, each providing identical mixing and reaction conditions. This segmentation ensures that particle formation occurs uniformly across all channels, eliminating the localization problems of batch reactors while maintaining operational simplicity through continuous flow.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The patent replaces mechanical stirring (batch mixing) with controlled fluid flow and diffusion-based mixing in continuous channels. This substitution eliminates the non-uniform mixing inherent in batch mechanical stirring while maintaining ease of operation through simple flow control.

Inventive Principle:
Principle #28Mechanics substitution (Replace mechanical system)

2Productivity

If continuous tubular flow reactors are used, then productivity is improved, but manufacturing precision deteriorates due to parabolic flow and product loss

Engineering Contradiction:
Improveproduction rateVSAvoidparticle size uniformity
Core Design Contradiction:
ProductivityVSManufacturing precision

Solution Approach 1:

The continuous reactor is divided into multiple parallel tubular channels, each with controlled dimensions and flow distribution. This segmentation ensures uniform flow characteristics across all channels, preventing the parabolic flow effects that cause non-uniform particle formation in single large tubular reactors.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The patent changes the flow regime parameters by using small-diameter parallel channels instead of large single channels. This parameter change transforms the flow characteristics to achieve uniform mixing and reaction conditions while maintaining continuous high-productivity operation.

Inventive Principle:
Principle #35Parameter changes

3Adaptability or versatility

If scale-up is performed empirically, then adaptability is improved, but manufacturing precision deteriorates due to lack of understanding of physical and chemical processes

Engineering Contradiction:
Improvescale-up flexibilityVSAvoidparticle size uniformity
Core Design Contradiction:
Adaptability or versatilityVSManufacturing precision

Solution Approach 1:

The patent incorporates monitoring and control mechanisms that provide feedback on particle formation conditions and product characteristics. This feedback enables precise control during scale-up, replacing empirical trial-and-error with data-driven optimization that maintains particle size uniformity across different production scales.

Inventive Principle:
Principle #23Feedback

Solution Approach 2:

The invention systematically controls and adjusts physical and chemical parameters (flow rates, concentrations, temperature, pH) during scale-up based on understood reaction mechanisms. This parameter control approach maintains manufacturing precision while adapting to different production scales, replacing empirical methods with science-based scale-up.

Inventive Principle:
Principle #35Parameter changes

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

Achieves uniformity of up to 99.9% and a cation-to-silicon ratio of 1.6 to 2.25 in nanoparticles, reducing product losses and contamination, and enabling scalable production of high-quality silicate-based powders.

Implementation Method 1

micro-mixing of aqueous solutions of water-soluble silicate and cationic species in a branched tubular structure with static mixing elements

Methodology Applied
Scientific EffectDiffusion: Diffusion

Implementation Method 2

micro-mixing of aqueous solutions... in a branched tubular structure with static mixing elements, followed by macro-mixing in a batch reactor

Methodology Applied
Scientific EffectConvection: Convection

Implementation Method 3

Precipitation, also called reactive crystallization, is one of the ways of producing pure phases of crystals or particles

Methodology Applied
Scientific EffectPrecipitation: Precipitation

Data Source

PatentUS10815128B2Nanoparticles and method for producing uniform silicate-based nanoparticles
Publication Date: 2020.10.27 ECOLE POLYTECHNIQUE FEDERALE DE LAUSANNE (EPFL)
  • US10815128B2 patent drawing
  • US10815128B2 patent drawing

AI summary

Nanoparticles and method for producing uniform silicate-based nanoparticles are disclosed. The method comprises a step of injecting into tubular branched elements comprising static mixers a first aqueous solution comprising a water-soluble silicate compound and a second aqueous solution comprising a water-soluble compound releasing cationic species in solution, and allowing the reaction between the first and the second aqueous solutions in a micro-mixing regime, the method being characterized in that the overall mixing time is kept below 10−5 s. A further step of allowing the solution obtained in the micro-mixing regime to mix in a macromixing regime. Nanoparticles obtained through the present method are also disclosed.