Area heater element, method for producing same and tool

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Solution Overview

Problem

Existing surface heat exchanger elements face challenges in manufacturing with minimal material usage while maintaining thermal efficiency, particularly when dealing with small pipe cross-sections that can lead to flow issues and evaporation problems.

Innovation Solution

The design incorporates a support plate with parallel, U-shaped pipe branches having smaller cross-sections than the connection cross-section, allowing for reduced material usage and optimized heat exchange, facilitated by a manufacturing method that uses heat transfer plates with grooved channels and a modified tooling process to accommodate circular pipe sections without deformation.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Loss of substance

If pipe cross-section is reduced to minimize material usage, then material consumption decreases, but fluid flow performance deteriorates and evaporation problems occur

Engineering Contradiction:
Improvematerial usageVSAvoidfluid flow performance
Core Design Contradiction:
Loss of substanceVSReliability

Solution Approach 1:

The piping system is divided into multiple parallel pipe branches instead of using a single large-diameter pipe. Each branch has a smaller cross-section (6-9 mm) but collectively they provide sufficient flow capacity. This segmentation allows material reduction while maintaining overall flow performance through parallel pathways.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

Different pipe cross-sections are used in different locations: smaller cross-sections (6-9 mm) in the parallel branches for material efficiency, and larger connection cross-sections (12-18 mm) at inlet/outlet connections for optimal fluid entry/exit. This local differentiation optimizes both material usage and flow performance.

Inventive Principle:
Principle #3Local quality

2Loss of substance

If pipe cross-section is reduced, then material usage decreases, but start-up time increases due to fluid volume reduction

Engineering Contradiction:
Improvematerial usageVSAvoidstart-up time
Core Design Contradiction:
Loss of substanceVSLoss of time

Solution Approach 1:

Multiple parallel pipe branches are implemented to distribute the fluid flow paths. Although each individual branch has reduced fluid volume, the parallel configuration provides multiple simultaneous flow paths, reducing the overall start-up time compared to a single large pipe with equivalent material content.

Inventive Principle:
Principle #1Segmentation

3Loss of substance

If pipe cross-section is reduced, then material usage decreases, but flow disruptions and evaporation issues arise

Engineering Contradiction:
Improvematerial usageVSAvoidflow disruptions and evaporation
Core Design Contradiction:
Loss of substanceVSObject-affected harmful factors

Solution Approach 1:

The flow path is segmented into multiple parallel branches, preventing flow stagnation and disruptions that would occur in a single narrow pipe. The parallel configuration ensures continuous flow distribution and reduces evaporation risks by maintaining adequate flow velocity across multiple pathways.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

Larger connection cross-sections (12-18 mm) are provided at inlet and outlet connections to ensure smooth fluid entry and exit, preventing flow disruptions at these critical points despite the smaller branch cross-sections.

Inventive Principle:
Principle #3Local quality

4Ease of manufacture

If conventional tooling is used for manufacturing, then manufacturing process remains simple, but pipe deformation occurs due to lack of accommodation for circular pipe sections

Engineering Contradiction:
Improvemanufacturing simplicityVSAvoidpipe section integrity
Core Design Contradiction:
Ease of manufactureVSManufacturing precision

Solution Approach 1:

Heat transfer plates with grooved channels serve as intermediaries between the circular pipe sections and the flat support plate. The grooves accommodate the circular pipe cross-sections without deformation, allowing conventional pressing tools to be used while maintaining pipe integrity. The heat transfer plates transfer the pressing force evenly around the circular pipes.

Inventive Principle:
Principle #24Intermediary (Mediator)

5Power

If parallel pipe branches are implemented, then heat exchange efficiency improves, but device complexity increases

Engineering Contradiction:
Improveheat exchange efficiencyVSAvoidpiping system complexity
Core Design Contradiction:
PowerVSDevice complexity

Solution Approach 1:

Multiple pipe branches are merged into a single support plate structure with integrated grooves. The heat transfer plates combine the functions of thermal conduction and mechanical support, while the grooves integrate multiple pipe accommodations into a unified manufacturing process. This merging reduces the complexity that would otherwise arise from assembling separate components.

Inventive Principle:
Principle #5Merging (Combining)

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 approach enables efficient heat exchange with lower fluid volumes, reduced start-up times, and minimized material usage, while avoiding flow disruptions and evaporation issues, allowing for simple installation and fabrication.

Implementation Method 1

The straight pipe sections are fixed to the support plate by means of heat transfer plates

Methodology Applied
Scientific EffectThermal conduction: Conduction (thermal)

Data Source

PatentEP2765366B1Area heater element, method for producing same and tool
Publication Date: 2025.11.19 KME SCHMOLE
  • EP2765366B1 patent drawingFigure 1
  • EP2765366B1 patent drawingFigure 1a
  • EP2765366B1 patent drawingFigure 2

AI summary

The element (10) has a support plate (11) at which a piping system (13) is defined with the help of transfer of heat metal sheets (14a-14f), and an input terminal (15) and an output terminal (16). The input terminal and the output terminal are provided with a connection pipe portion (17) with a cross-section connection (18). A set of parallel switched spacer branches (19a-19c) is arranged with rectilinearly trained line sections (20a-20f). Each line section is arranged along a common flow direction (22) and has a pipe cross-section (24) that is smaller than connection cross-section. Independent claims are also included for the following: (1) a method for manufacturing a surface heat exchange element (2) a tool for manufacturing a surface heat exchange element.