Counter-flow diverging microchannels for heat sink

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Solution Overview

Problem

Current microchannel heat sinks face challenges with high heat flux dissipation due to low critical heat flux, temperature non-uniformity, and flow instability, particularly in large heating areas, which limits their effectiveness in cooling high-power electronic devices like electric vehicle components.

Innovation Solution

The use of counter-flow diverging microchannels with a unique heat exchange design between neighboring channels, where the microchannels have a diverging angle of between zero and 1°, enhances heat transfer performance by increasing the channel wall area to base area ratio, leading to higher heat dissipation rates, more uniform temperature distribution, and reduced pressure drop.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Temperature

If conventional co-current flow microchannels are used, then the structure is simple, but the heat transfer coefficient is low and temperature uniformity is poor

Engineering Contradiction:
Improvetemperature uniformityVSAvoidchannel configuration complexity
Core Design Contradiction:
TemperatureVSDevice complexity

Solution Approach 1:

The patent inverts the conventional co-current flow arrangement by implementing counter-flow configuration where adjacent microchannels have opposite flow directions. This inversion enables lateral heat exchange between channels, significantly improving temperature uniformity across the heating surface while maintaining a relatively simple microchannel structure.

Inventive Principle:
Principle #13The other way round (Inversion)

Solution Approach 2:

The patent introduces lateral heat exchange between adjacent microchannels as a new dimension of heat transfer. By utilizing the wall area between channels for inter-channel heat exchange in addition to the primary heat transfer from the heating surface, the system achieves enhanced temperature uniformity without substantially increasing structural complexity.

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

2Productivity

If microchannel heat sink is used for high heat flux dissipation, then heat transfer area is increased, but critical heat flux is low and flow instability occurs

Engineering Contradiction:
Improveheat dissipation rateVSAvoidflow stability
Core Design Contradiction:
ProductivityVSReliability

Solution Approach 1:

The counter-flow configuration inverts the conventional approach by having adjacent channels flow in opposite directions. This creates a stabilizing effect where the cooler outlet of one channel provides lateral cooling to the inlet region of the adjacent channel, suppressing bubble formation and flow instability while maintaining high heat dissipation capacity.

Inventive Principle:
Principle #13The other way round (Inversion)

Solution Approach 2:

The lateral heat exchange between counter-flow channels provides preliminary cooling to regions where bubbles tend to form and accumulate. By pre-cooling the inlet regions of channels through lateral heat transfer from adjacent channel outlets, the system prevents premature boiling and flow instability before they can develop.

Inventive Principle:
Principle #9Preliminary anti-action

3Productivity

If diverging microchannels with larger angle are used, then bubble expansion is improved, but channel wall area to base area ratio decreases

Engineering Contradiction:
Improveheat dissipation rateVSAvoidchannel wall area
Core Design Contradiction:
ProductivityVSArea of stationary object

Solution Approach 1:

The counter-flow configuration compensates for the reduced wall area in diverging channels by utilizing lateral heat exchange between channels. The inverted flow arrangement ensures that heat is efficiently transferred through the reduced wall area by leveraging the temperature difference between adjacent channels, maintaining high heat dissipation performance despite the geometric constraints.

Inventive Principle:
Principle #13The other way round (Inversion)

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 a significantly higher heat transfer coefficient, critical heat flux, and coefficient of performance, with a 45.1% increment in heat transfer coefficient and 73.8% reduction in pressure drop compared to conventional co-current flow designs, ensuring stable two-phase flow and efficient heat dissipation.

Implementation Method 1

adjacent microchannels accommodate flow of working fluid in opposite directions and are thermally coupled to each other to enable heat exchange between the corresponding adjacent microchannels

Methodology Applied
Scientific EffectThermal conduction: Conduction (thermal)

Implementation Method 2

convective boiling in a heat sink with microchannel arrays is a very promising solution for such high heat transfer performance

Methodology Applied
Scientific EffectConvective boiling: Boiling

Implementation Method 3

utilizing latent heat through the liquid-vapor phase change

Methodology Applied
Scientific EffectPhase change: Phase Change

Implementation Method 4

each microchannel cross sectional area increases as the channel length progresses from an upstream end to a downstream end

Methodology Applied
Scientific EffectPressure gradient: Pressure Gradient

Data Source

PatentUS11991862B2Heat sink with counter flow diverging microchannels
Publication Date: 2024.05.21 CITY UNIVERSITY OF HONG KONG
  • US11991862B2 patent drawing
  • US11991862B2 patent drawing
  • US11991862B2 patent drawing

AI summary

The present invention provides a microchannel heat sink with plural microchannels, each having a respective inlet and outlet to permit flow, in particular two-phase flow, of a working fluid. The plural microchannels are arranged such that adjacent microchannels accommodate flow of working fluid in opposite directions and are thermally coupled to each other to enable heat exchange between the corresponding adjacent microchannels. In one aspect, a microchannel inlet is positioned at an angle (e.g., 90 degrees) with respect to its outlet. The plural microchannels define parallel longitudinal axes that are optionally arranged on the same plane and/or side-by-side in a single layer. Further, in one aspect, each microchannel cross-sectional area increases as the channel length progresses from an upstream end (e.g., adjacent to the inlet) to a downstream end (e.g., adjacent to the outlet) of the corresponding microchannel.