Variable Height Turbulising Elements Plate Heat Exchanger

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Solution Overview

Problem

Existing countercurrent plate heat exchangers face significant hydraulic resistance issues when working agents undergo substantial volume changes or state transitions during the heat exchange process, leading to exponential growth in resistance.

Innovation Solution

The proposed plate heat exchange module features two plates with a rib structure comprising turbulising elements arranged in rows, where the height of successive rows differs uniformly. This design allows for a changing cross-sectional area between the plates, accommodating volume changes of the working agent and reducing hydraulic resistance.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Ease of manufacture

If the cross-sectional area between plates remains constant along the entire length, then the structure is simple and easy to manufacture, but hydraulic resistance increases exponentially when the working agent volume increases substantially

Engineering Contradiction:
Improvestructural simplicityVSAvoidhydraulic resistance
Core Design Contradiction:
Ease of manufactureVSObject-affected harmful factors

Solution Approach 1:

The patent applies the dynamics principle by making the cross-sectional area variable rather than constant. The distance between adjacent plates changes along the flow direction, creating a dynamic flow channel geometry that adapts to volume changes of the working agent, thereby preventing exponential growth of hydraulic resistance while maintaining manufacturability through standard plate stacking.

Inventive Principle:
Principle #15Dynamics

Solution Approach 2:

The patent implements parameter changes by varying the cross-sectional area parameter along the flow path. By changing the plate spacing parameter dynamically rather than keeping it constant, the system adapts to working agent volume changes and reduces hydraulic resistance without complicating the manufacturing process.

Inventive Principle:
Principle #35Parameter changes

2Productivity

If the working agent volume increases substantially during heat exchange, then the heat exchange capacity is improved, but hydraulic resistance increases exponentially

Engineering Contradiction:
Improveheat exchange capacityVSAvoidhydraulic resistance
Core Design Contradiction:
ProductivityVSObject-affected harmful factors

Solution Approach 1:

The variable cross-sectional area design allows the flow channel to dynamically expand where working agent volume increases, maintaining heat exchange capacity while preventing exponential hydraulic resistance growth through adaptive geometry rather than fixed dimensions.

Inventive Principle:
Principle #15Dynamics

Solution Approach 2:

By changing the cross-sectional area parameter along the flow direction, the system accommodates working agent volume changes and maintains optimal flow conditions, preventing hydraulic resistance from increasing exponentially while preserving heat exchange productivity.

Inventive Principle:
Principle #35Parameter changes

3Device complexity

If turbulising elements with uniform height are used, then the structure is simple, but heat transfer efficiency is limited

Engineering Contradiction:
Improverib structure simplicityVSAvoidheat transfer efficiency
Core Design Contradiction:
Device complexityVSTemperature

Solution Approach 1:

The patent applies local quality by varying the height of turbulising elements at different locations along the flow path. This creates locally optimized flow disturbance that enhances heat transfer efficiency in different sections, with higher elements where greater turbulence is needed and lower elements where flow is already well-mixed, without requiring completely complex structures.

Inventive Principle:
Principle #3Local quality

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 module effectively manages hydraulic resistance and maintains desired thermodynamic parameters by adjusting the Reynolds number through varying turbulising element heights, enhancing both heat transfer and flow resistance coefficients.

Implementation Method 1

The rib structure takes the form of turbulising elements arranged in rows on one side of each of the plates

Methodology Applied
Scientific EffectTurbulence: Turbulence

Implementation Method 2

the height of the turbulising elements in any successive row is different with respect to the preceding row by the same value, and where the plates are set together so that positioned on one plate on its side which features the lowest turbulising elements is the side of the other plate with the highest turbulising elements

Methodology Applied
Scientific EffectHydraulic resistance reduction through variable cross-section:

Implementation Method 3

a plate heat exchange module which comprises two plates featuring a rib structure

Methodology Applied
Scientific EffectHeat exchange: Heat Exchanger

Data Source

PatentEP4556840A1Plate heat exchange module
Publication Date: 2025.05.21 AIC SPOLKA AKCYJNA
  • EP4556840A1 patent drawingFigure 1~2
  • EP4556840A1 patent drawingFigure 3~4
  • EP4556840A1 patent drawingFigure 5~7

AI summary

A plate heat exchange module comprising two plates featuring a rib structure, where each plate is fitted with an inlet connection and outlet connection for the working agent which flows through the plate is characterised in that the rib structure takes the form of turbulising elements (2) arranged in rows on one side of each of the plates (1A, 1B), while the other side of each plate (1A, 1B) is flat, where the height (h) of the turbulising elements (2) in any successive row is different with respect to the preceding row by the same value, and where the plates (1A, 1B) are set together so that positioned on one plate on its side which features the lowest turbulising elements (2) is the side of the other plate with the highest turbulising elements (2).