Microfluidic Flow Focusing for Monodisperse Microbubble Mass Production

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Solution Overview

Problem

Current methods for producing microbubbles for medical ultrasound imaging and drug delivery fail to generate monodisperse microbubbles with controlled diameters below 10 μm, leading to polydispersity issues that limit their therapeutic effectiveness.

Innovation Solution

A microfluidic flow focusing device is used to produce monodisperse microbubbles by creating a co-flow of dispersed and continuous phase fluids, forming a gradually thinning jet that breaks off to produce microbubbles with a narrow size distribution, specifically in the range of 2-5 μm, allowing for high production rates without size-sorting steps.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Manufacturing precision

If sonication or mechanical agitation is used to produce microbubbles, then microbubbles can be generated in liquid, but the microbubbles are polydisperse which limits therapeutic effectiveness

Engineering Contradiction:
Improvebubble size uniformityVSAvoidproduction rate
Core Design Contradiction:
Manufacturing precisionVSProductivity

Solution Approach 1:

The patent employs a microfluidic flow focusing device where gas (dispersed phase) and liquid (continuous phase) flows are precisely controlled through microchannels. The flow rates and channel geometries are designed to create a co-flow regime that focuses the gas-liquid interface, producing monodisperse microbubbles at high production rates without requiring size sorting steps

Inventive Principle:
Principle #29Pneumatics and hydraulics

2Manufacturing precision

If microbubbles with diameter 1-10 μm are produced for medical applications, then therapeutic effectiveness is improved, but conventional methods cannot achieve monodispersity

Engineering Contradiction:
Improvebubble diameter controlVSAvoidapparatus structure
Core Design Contradiction:
Manufacturing precisionVSDevice complexity

Solution Approach 1:

The device segments the gas-liquid flow into discrete microbubble units through a flow focusing junction. The microchannel geometry divides the continuous gas-liquid interface into individual bubbles with controlled diameters, achieving monodispersity through spatial segmentation rather than post-production sorting

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The patent transitions from conventional bulk bubble generation to microscale channel-based generation. By confining the gas-liquid interface within microchannels with specific dimensional ratios (Lbfc/Dbfc >> 1), the system achieves precise diameter control in the 1-10 μm range that is inaccessible to macro-scale methods

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

3Ease of manufacture

If larger diameter bubbles are used, then easier production is achieved, but bubbles cannot safely flow through smallest capillaries and provoke edema

Engineering Contradiction:
Improveproduction simplicityVSAvoidedema and capillary blockage
Core Design Contradiction:
Ease of manufactureVSObject-affected harmful factors

Solution Approach 1:

The patent systematically controls critical parameters including channel dimensions (Lbfc, Dbfc), flow rates of gas and liquid phases, and pressure gradients to produce microbubbles with diameters strictly within the 1-10 μm safe range. These parameter optimizations ensure both ease of production and biocompatibility without requiring post-production size selection

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

The apparatus enables the rapid mass production of monodisperse microbubbles with extremely narrow size distribution, achieving production rates above 105 microbubbles per second, suitable for use as contrast agents or drug carriers with precise control over bubble diameter.

Implementation Method 1

a flow of dispersed phase fluid discharging from the outlet of the dispersed phase fluid supply channel is engageable in co-flow by a focusing flow of continuous phase fluid discharging from the outlet of the at least one continuous phase fluid supply channel

Methodology Applied
Scientific EffectCo-flow:

Implementation Method 2

under formation of a gradually thinning jet of dispersed phase fluid that extends into the inlet of the bubble formation channel

Methodology Applied
Scientific EffectJet formation: Jet

Implementation Method 3

monodisperse microbubbles, having a diameter smaller than the hydraulic diameter of the bubble formation channel break off a tip of said jet

Methodology Applied
Scientific EffectCapillary instability:

Implementation Method 4

monodisperse microbubbles, having a diameter smaller than the hydraulic diameter of the bubble formation channel break off a tip of said jet

Methodology Applied
Scientific EffectSurface tension: Surface Tension

Data Source

PatentUS9782733B2Apparatus and method for mass producing a monodisperse microbubble agent
Publication Date: 2017.10.10 SOLSTICE PHARMA BV
  • US9782733B2 patent drawing
  • US9782733B2 patent drawing
  • US9782733B2 patent drawing

AI summary

An apparatus for mass producing monodisperse microbubbles contains a microfluidic flow focusing device. The microfluidic flow focusing device includes a dispersed phase fluid supply channel having an outlet that discharges into a flow focusing junction, a continuous phase fluid supply channel having an outlet that discharges into the flow focusing junction, and a bubble formation channel having an inlet disposed at the flow focusing junction. The configuration of the flow focusing junction is such that, in operation, a flow of dispersed phase fluid discharging from the outlet of the dispersed phase fluid supply channel is engageable in co-flow by a focusing flow of continuous phase fluid discharging from the outlet of the at least one continuous phase fluid supply channel under formation of a gradually thinning jet of dispersed phase fluid that extends into the inlet of the bubble formation channel.