Flat Oval Heat Exchanger Tubes That Resist Deformation

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Solution Overview

Problem

Existing heat exchangers face issues with deformation of flat elliptic heat transfer pipes due to internal pressure, leading to reduced contact with plate-like fins, increased pressure loss, and higher assembly costs, which affect heat transfer performance and ventilation resistance.

Innovation Solution

A heat exchanger design featuring flat-shaped heat transfer pipes with oval sections and D-shaped through holes, bulkhead partitioning, and protruding strips, bonded using pipe-expanding burette balls, maintains pressure capacity and ensures close contact with plate-like fins, reducing deformation and assembly complexity.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Device complexity

If a flat elliptic heat transfer pipe with a single through hole is used, then the pipe structure is simple, but the heat transfer pipe is expanded and deformed by internal pressure during operation, deteriorating close contact with the plate-like fin

Engineering Contradiction:
Improveheat transfer pipe structureVSAvoidclose contact with plate-like fin
Core Design Contradiction:
Device complexityVSReliability

Solution Approach 1:

The single through hole of the heat transfer pipe is divided into multiple refrigerant flow passages (first and second passages). This segmentation increases the structural rigidity of the pipe wall, preventing deformation under internal pressure while maintaining the flat elliptic shape for good contact with plate-like fins. The multiple passages are arranged symmetrically to balance stress distribution.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

Protruding strips are added locally on the inner wall face of the refrigerant flow passages. These protruding strips create turbulence in the refrigerant flow, enhancing heat transfer performance in specific regions where it is most needed, without affecting the overall pipe shape or contact with fins.

Inventive Principle:
Principle #3Local quality

2Temperature

If the heat transfer pipe is made into a multi-hole structure with reduced size and diameter, then heat transfer rate in the pipe is increased, but pressure loss is increased and manufacturing and assembly costs increase due to brazing requirements

Engineering Contradiction:
Improveheat transfer rateVSAvoidpressure loss
Core Design Contradiction:
TemperatureVSLoss of energy

Solution Approach 1:

The heat transfer pipe uses multiple refrigerant flow passages with optimized dimensions and arrangements. By changing the parameters of the flow passages (number, size, shape, and distribution), the patent achieves enhanced heat transfer rate while controlling pressure loss. The symmetric D-shaped passages are designed to optimize flow characteristics and minimize pressure drop.

Inventive Principle:
Principle #35Parameter changes

3Temperature

If the heat transfer pipe size and diameter are reduced, then heat transfer performance is improved, but assembling cost is increased since manufacture and mounting are carried out by brazing

Engineering Contradiction:
Improveheat transfer performanceVSAvoidassembling cost
Core Design Contradiction:
TemperatureVSEase of manufacture

Solution Approach 1:

The patent adopts a heat transfer pipe design that can be manufactured and assembled more economically. The multi-hole flat elliptic pipe structure allows for efficient manufacturing processes and simpler assembly methods compared to traditional brazing techniques, reducing assembling costs while maintaining improved heat transfer performance through the optimized multi-passage design.

Inventive Principle:
Principle #27Cheap short-living objects (Disposable)

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 design enhances heat transfer performance, reduces ventilation resistance, and increases heat exchange capacity while maintaining reduced pipe size and diameter, with improved assembling efficiency and cost-effectiveness.

Implementation Method 1

bonded to the plate-like fin by expanding diameters of the first and second refrigerant flow passages by a pipe-expanding burette ball

Methodology Applied
Scientific EffectMechanical Force: Mechanical Force

Implementation Method 2

heat transfer pipe inserted in a direction orthogonal to the plate-like fins and through which a refrigerant flows

Methodology Applied
Scientific EffectHeat conduction: Conduction (thermal)

Implementation Method 3

plate-like fins arranged in parallel with a predetermined interval and a plurality of flat-shaped heat transfer pipes inserted in a direction orthogonal to the plate-like fins and through which a refrigerant flows

Methodology Applied
Scientific EffectConvection: Convection

Implementation Method 4

one of or both of said first and second refrigerant flow passages have a plurality of protruding strips extending in an axial direction on an inner wall face of the flow passage

Methodology Applied
Scientific EffectTurbulence: Turbulence

Data Source

PatentEP2312254B1Heat exchanger and air conditioner having the heat exchanger
Publication Date: 2017.08.30 MITSUBISHI ELECTRIC CORP
  • EP2312254B1 patent drawingFigure 1~2
  • EP2312254B1 patent drawingFigure 3~4
  • EP2312254B1 patent drawingFigure 5~6

AI summary

A heat exchanger provided with a plurality of plate-like fins 2 arranged in parallel with a predetermined interval and a plurality of flat-shaped heat transfer pipes 3 inserted in a direction orthogonal to said plate-like fins 2 and through which a refrigerant flows, in which said heat transfer pipe 3 has an outside shape with a flat outer face arranged along an air flow direction and a section substantially in an oval shape and first and second refrigerant flow passages 31a, 31b made of two symmetric and substantially D-shaped through holes having a bulkhead 32 between the two passages inside, which is bonded to said plate-like fin 2 by expanding diameters of said first and second refrigerant flow passages 31a, 31b by a pipe-expanding burette ball.