Microfluidic Cross-Junction Emulsification Process

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Solution Overview

Problem

Existing methods for producing multiple emulsions, particularly double or triple emulsions, face challenges in achieving consistent droplet sizes and monodispersity, especially with high-viscosity oils, leading to instability and practical limitations in commercial applications.

Innovation Solution

A microfluidic process that involves a cross-junction geometry microchannel system with controlled flow rates and temperature optimization, allowing for the production of multiple emulsions with a coefficient of variation in droplet diameter of less than 5%, independent of the system used, by setting the ratio of dispersed phase flow rate to continuous phase flow rate within a specific operating window defined by fluid properties.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Stability of the object's composition

If two-step emulsification technique is used to produce multiple emulsions, then emulsion formation is achieved, but droplet size consistency and monodispersity deteriorate

Engineering Contradiction:
Improveemulsion formationVSAvoiddroplet size consistency
Core Design Contradiction:
Stability of the object's compositionVSManufacturing precision

Solution Approach 1:

The invention divides the emulsification process into two distinct microfluidic junctions: the first junction forms primary droplets (e.g., aqueous droplets in oil phase), and the second junction forms the multiple emulsion structure (e.g., encapsulating primary droplets in outer aqueous phase). This segmentation allows independent control of each emulsification step, achieving both emulsion formation and droplet size consistency with coefficient of variation less than 5%.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The invention introduces a transient intermediate state where primary droplets formed at the first junction are carried through a channel to the second junction before final emulsion formation. This intermediate transport phase allows precise control of droplet size and composition before the final encapsulation step, resolving the contradiction between forming stable multiple emulsions and maintaining monodispersity.

Inventive Principle:
Principle #24Intermediary (Mediator)

2Stability of the object's composition

If high-viscosity oils are used in multiple emulsions, then emulsion stability improves, but droplet size control and monodispersity deteriorate

Engineering Contradiction:
Improveemulsion stabilityVSAvoiddroplet size control
Core Design Contradiction:
Stability of the object's compositionVSManufacturing precision

Solution Approach 1:

The invention changes the physical parameters of the system by precisely controlling flow rates of dispersed and continuous phases through the microfluidic device. By adjusting the ratio of dispersed phase flow rate to continuous phase flow rate within a specific operating window, the system achieves droplet size consistency with coefficient of variation less than 5% even with high-viscosity oils, while maintaining emulsion stability.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The invention replaces traditional mechanical mixing methods with microfluidic flow control to achieve emulsification. The microfluidic junctions use controlled fluid flow rather than mechanical shear forces to form droplets, enabling precise droplet size control with high-viscosity oils that would be difficult to control using conventional mechanical emulsification methods.

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

3Productivity

If conventional emulsification methods are used, then emulsion production is achieved, but system dependence and reproducibility deteriorate

Engineering Contradiction:
Improveemulsion productionVSAvoidsystem independence
Core Design Contradiction:
ProductivityVSReliability

Solution Approach 1:

The invention creates a universal microfluidic platform that can produce multiple emulsions with consistent results across different systems. The process is defined by dimensionless numbers (Ohnesorge number, capillary number) and flow rate ratios rather than system-specific parameters, making the method transferable and reproducible across different microfluidic devices and laboratories while maintaining high productivity.

Inventive Principle:
Principle #6Universality (Multi-functionality)

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 process achieves highly monodisperse multiple emulsions with stable droplet sizes, enhancing the viability of these emulsions in industrial applications by ensuring consistent droplet formation and stability, regardless of the system used, without requiring changes in channel hydrophobicity or hydrophilicity and without the need for surfactants.

Implementation Method 1

Interfacial tension controlled W/O and O/W 2-phase flows in microchannel

Methodology Applied
Scientific EffectInterfacial tension: Surface Tension

Implementation Method 2

controlled flow rates and temperature optimization, allowing for the production of multiple emulsions with a coefficient of variation in droplet diameter of less than 5%

Methodology Applied
Scientific EffectCapillary pressure: Capillary Pressure

Data Source

PatentEP2337627B1Process for preparing monodispersed emulsions
Publication Date: 2013.07.17 TECH UNIV EINDHOVEN
  • EP2337627B1 patent drawingFigure 1
  • EP2337627B1 patent drawingFigure 2~3
  • EP2337627B1 patent drawingFigure 4

AI summary

A process for preparing an emulsion is disclosed comprising: injecting a first liquid as dispersed phase liquid through a central inlet of a microchannel (15) system with a cross junction geometry chip and injecting a second liquid as continuous phase liquid through the outer cross inlet (16), which continuous phase liquid does not instantly mix with said injected first liquid prior to the cross junction, wherein the flow rate Qc of the continuous phase in cubic meters per second is given by (I) where A is the exit area of the microchannel (17) in square meters, y the interfacial tension between the first liquid and the second liquid in Newtons per meter and µd the viscosity of the dispersed phase in Pascal-seconds, characterized in that f is in the range from 0.04 to 0.25.