Microfluidic Device With Split Chambers For Heat Exchange

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Solution Overview

Problem

Microfluidic devices face challenges in enhancing heat exchange performance while maintaining or reducing pressure drop and improving mixing efficiency, particularly in achieving higher throughput without compromising thermal control and fluid dynamics.

Innovation Solution

The design incorporates multiple successive chambers within the reactant passage, featuring a split and re-direction of sub-passages with a 90-degree change in direction, a gradually narrowing exit, and a concave splitting and re-directing wall, which induces secondary flows and maximizes heat transfer and mixing efficiency while minimizing pressure drop.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Temperature

If traditional microfluidic device designs are used, then manufacturing simplicity is maintained, but heat exchange performance is insufficient

Engineering Contradiction:
Improveheat exchange performanceVSAvoiddevice structure complexity
Core Design Contradiction:
TemperatureVSDevice complexity

Solution Approach 1:

The reactant passage is divided into multiple chambers (first chamber, second chamber, third chamber) with distinct functions. Each chamber contains specific flow distribution structures (first flow distribution structure, second flow distribution structure) that segment the fluid flow paths. This segmentation enables enhanced heat exchange in specific zones while maintaining overall device manufacturability through modular design.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

Different regions of the device are assigned different structural qualities optimized for their specific functions. The first chamber has a first flow distribution structure optimized for initial mixing, the second chamber has a second flow distribution structure optimized for heat exchange, and the third chamber has a third flow distribution structure optimized for final mixing. This local optimization improves heat exchange performance without requiring complete redesign of the entire device.

Inventive Principle:
Principle #3Local quality

2Productivity

If throughput is increased, then productivity improves, but pressure drop increases

Engineering Contradiction:
ImprovethroughputVSAvoidpressure drop
Core Design Contradiction:
ProductivityVSStress or pressure

Solution Approach 1:

The flow distribution structures are designed to dynamically adapt to varying flow rates. The multiple chambers and flow distribution structures create a system where flow paths can effectively adjust to different throughput conditions, maintaining efficient fluid distribution and minimizing pressure drop across a range of operating conditions.

Inventive Principle:
Principle #15Dynamics

Solution Approach 2:

The device utilizes three-dimensional chamber configurations with vertical and horizontal flow distribution structures. This multi-dimensional approach to flow management allows for more efficient fluid distribution and reduced pressure drop compared to traditional two-dimensional channel designs, enabling higher throughput with lower pressure penalties.

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

3Stability of the object's composition

If mixing efficiency is improved, then reaction performance improves, but device complexity increases

Engineering Contradiction:
Improvemixing efficiencyVSAvoidpassage structure complexity
Core Design Contradiction:
Stability of the object's compositionVSDevice complexity

Solution Approach 1:

Multiple functions are merged into the flow distribution structures. The same structures that distribute flow also create mixing zones and facilitate heat exchange. For example, the first flow distribution structure in the first chamber serves both flow distribution and initial mixing functions, while the second flow distribution structure in the second chamber combines heat exchange with continued mixing. This merging reduces the need for separate dedicated components.

Inventive Principle:
Principle #5Merging (Combining)

Solution Approach 2:

The flow distribution structures are designed to perform multiple functions simultaneously. Each structure serves as a flow distributor, a mixing element, and a heat transfer surface. This multi-functionality achieves improved mixing efficiency without adding dedicated mixing components that would increase device complexity.

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 configuration results in improved heat transfer coefficients, enhanced mixing performance, and reduced pressure drop, achieving process intensification by maintaining or increasing throughput with reduced equipment size and energy consumption.

Implementation Method 1

a concave splitting and re-directing wall, which induces secondary flows and maximizes heat transfer and mixing efficiency

Methodology Applied
Scientific EffectSecondary flows: Turbulence

Implementation Method 2

one or more thermal control passages defined therein... in a relatively controlled thermal environment

Methodology Applied
Scientific EffectHeat transfer: Conduction (thermal)

Data Source

PatentEP2017000B1Process intensified microfluidic devices
Publication Date: 2012.09.05 CORNING INC
  • EP2017000B1 patent drawingFigure 1~2
  • EP2017000B1 patent drawingFigure 3
  • EP2017000B1 patent drawingFigure 4~5

AI summary

A microfluidic device [10] includes at least one reactant passage [26] and one or more thermal control passages defined therein, the one or more thermal control passages being positioned and arranged within two volumes [12,14] each bordered by a wall [18,20], the walls being generally planar and parallel to one another, the reactant passage positioned between said generally planar walls and defined by said generally planar walls and walls [28] extending between said generally planar walls, wherein the reactant passage comprises multiple successive chambers [34], each such chamber including a split of the reactant passage into at least two sub-passages [36], and a joining [38] of the split passages, and a change of passage direction, of at least one of the sub-passages, of at least 90 degrees.