Variable Spacing Heat Exchanger for Thermal Stress and De-icing
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Solution Overview
Problem
Conventional heat exchangers face failure due to thermal and pressure-induced stresses in high-temperature, high-pressure applications, and require de-icing solutions for aircraft use, with tubular types being more tolerant but costly and heavy, while plate-fin types need to match tubular performance and rapid de-icing capabilities.
Innovation Solution
A heat exchanger design featuring varying fin spacings and thicknesses, connected with filleted joints, and a de-icing channel without fins, allowing for efficient heat transfer and rapid de-icing through additive layer fabrication, minimizing thermal and pressure stresses and facilitating de-icing by maximizing fluid flow in a serpentine de-icing channel.
Engineering Contradictions & Design Principles
Engineering Contradiction Analysis
1Reliability
If conventional welded or brazed joints are used in plate-fin heat exchangers, then manufacturing cost and weight are reduced compared to tubular types, but the joints fail under high temperature differentials and high pressures
Solution Approach 1:
The heat exchanger is divided into modular plate assemblies that can be independently manufactured and tested, then assembled together. This segmentation allows each module to withstand thermal stress independently, preventing catastrophic failure of the entire structure under high temperature differentials and pressures.
Solution Approach 2:
The plate-fin assemblies are pre-assembled and pre-tested for structural integrity before final integration into the complete heat exchanger system. This preliminary action ensures that joints are properly formed and stress-tested before encountering extreme operating conditions, preventing premature failure.
2Temperature
If tubular type heat exchangers are used, then tolerance for high pressure and high temperature differentials is improved, but manufacturing cost and weight increase
Solution Approach 1:
The heat exchanger employs composite construction combining metal plates with thermally-resistant coatings or bonded thermal barriers. This composite approach provides the structural strength and thermal tolerance of tubular designs while maintaining the weight and manufacturing advantages of plate-fin construction.
3Use of energy by moving object
If closely spaced fins are used in plate-fin heat exchangers, then heat transfer efficiency is improved, but ice formation occurs in cold environments
Solution Approach 1:
The fin spacing is varied locally throughout the heat exchanger structure. Critical areas prone to ice formation (such as inlet regions and exterior surfaces) have increased spacing to prevent condensation and ice accumulation, while internal heat transfer zones maintain close spacing for optimal thermal efficiency. This local differentiation resolves the contradiction between heat transfer performance and ice resistance.
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 design enhances the tolerance of plate-fin heat exchangers to high temperature and pressure differentials, matches the performance of tubular types, and enables rapid de-icing, reducing operational delays and extending lifespan by minimizing thermal stress and pressure drop.
Implementation Method 1
heat transfer elements positioned in the at least one fluid passageway and joined with the heat transfer plate
Implementation Method 2
passing bleed air through first fluid passageways of a heat exchanger, the second fluid passageways being thermally coupled with the first fluid passageways
Implementation Method 3
enables rapid de-icing, reducing operational delays and extending lifespan by minimizing thermal stress and pressure drop
Data Source
AI summary
A heat exchanger may include at least one fluid passageway adjacent a heat transfer plate and a plurality of heat transfer elements positioned in the at least one fluid passageway and joined with the heat transfer plate. The heat transfer elements may be positioned with first spacings therebetween at an inlet end of the at least one fluid passageway. The heat transfer elements may be positioned with second spacings therebetween at an outlet end of the at least one fluid passageway. The first spacings may be smaller than the second spacings.


