Offset Corrugated Heat Exchanger Plate Design

Resolve Bottlenecks,
Find Innovative Solutions
Generate Solutions

Solution Overview

Problem

Conventional heat exchanger plates in cooling towers, such as those used in power plants, face inefficiencies in heat transfer due to their design, particularly at low water/high air loading conditions, leading to suboptimal performance and material usage.

Innovation Solution

The development of heat exchanger plates with a unique corrugated design featuring offset corrugation segments and recessed surfaces, which enhance airflow and water flow passage configurations, allowing for improved heat transfer efficiency and reduced material requirements.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Ease of manufacture

If conventional heat exchanger plates with vertically-extending corrugations are used, then the structure is simple and manufacturing is easy, but heat transfer efficiency is insufficient particularly at low water/high air loading conditions

Engineering Contradiction:
Improveease of manufactureVSAvoidheat transfer efficiency
Core Design Contradiction:
Ease of manufactureVSProductivity

Solution Approach 1:

The corrugations are divided into multiple segments (first, second, and third corrugation segments) rather than being continuous. This segmentation creates distinct functional zones: the first and second segments provide structural support while the third segment creates enhanced flow passages. This resolves the contradiction by maintaining manufacturability through simple geometric shapes while improving heat transfer through optimized flow patterns.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

Different portions of the heat exchanger plate are given different corrugation characteristics. The first and second corrugation segments have specific geometries for structural integrity, while the third segment is designed to create specific flow patterns. This local differentiation allows the plate to simultaneously maintain structural simplicity for easy manufacture and create localized zones of enhanced heat transfer efficiency.

Inventive Principle:
Principle #3Local quality

2Quantity of substance

If conventional heat exchanger plates are used, then material usage is straightforward, but the number of plates required per unit volume is high leading to increased material consumption

Engineering Contradiction:
Improvematerial usageVSAvoidperformance per unit volume
Core Design Contradiction:
Quantity of substanceVSProductivity

Solution Approach 1:

The corrugation segments are arranged to create three-dimensional flow passages that utilize the vertical dimension more effectively. The offset arrangement of segments in the widthwise direction creates staggered flow paths that increase the effective heat transfer volume within the same plate thickness, reducing the number of plates needed.

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

Solution Approach 2:

The multiple corrugation segments are nested within each other in a staggered arrangement, with each segment contributing to the overall heat transfer function. This nested structure maximizes the heat transfer surface area and volume utilization within a single plate, reducing the total number of plates required.

Inventive Principle:
Principle #7Nested doll (Nesting)

3Device complexity

If vertically-extending corrugations are used, then the plate structure is simple, but airflow and water flow passage configurations are suboptimal

Engineering Contradiction:
Improveplate structure complexityVSAvoidflow passage configuration
Core Design Contradiction:
Device complexityVSProductivity

Solution Approach 1:

The continuous vertical corrugations are segmented into distinct sections with different geometries and orientations. This segmentation creates differentiated flow passages for air and water while maintaining the overall simplicity of the corrugated plate structure. Each segment can be optimized for its specific flow function without complicating the entire plate design.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The corrugation segments are designed with asymmetric geometries where the first, second, and third segments have different characteristics. This asymmetry creates optimized flow patterns that differ from conventional symmetric designs, improving heat transfer efficiency while the overall corrugated structure remains relatively simple to manufacture.

Inventive Principle:
Principle #4Asymmetry

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 new design improves heat transfer characteristics, particularly at low water/high air loading conditions, while reducing the number of plates needed per unit volume, resulting in enhanced performance and cost savings.

Implementation Method 1

heat exchanger plate fabricated from sheet material... efficiently transfer heat from one medium to another

Methodology Applied
Scientific EffectHeat conduction: Conduction (thermal)

Implementation Method 2

ambient air AA enters at the bottom of hyperboloid cooling tower 10, flows upwardly through the fill pack assembly 14... heated water 12h flows, i.e. drips or rains, downwardly through the fill pack assembly 14

Methodology Applied
Scientific EffectConvection: Convection

Implementation Method 3

use the evaporation of water to remove waste heat and cool water to near the wet-bulb air temperature

Methodology Applied
Scientific EffectEvaporation: Evaporation

Data Source

PatentEP2800936B1Heat exchanger plate and a fill pack of heat exchanger plates
Publication Date: 2017.03.22 EVAPCO INC
  • EP2800936B1 patent drawing
  • EP2800936B1 patent drawing
  • EP2800936B1 patent drawing

AI summary

A heat exchanger plate includes a corrugated sheet of stiff material configured in a repetitive series of elongated corrugations. Each corrugation has a first corrugation segment, a second corrugation segment disposed offset from and extending parallel to the first corrugation segment and an intermediate corrugation segment. The first and second corrugation segments extend vertically. The intermediate corrugation segment is disposed between and interconnects the first corrugation segment and the second corrugation segment and extends obliquely relative to the first corrugation segment and the second corrugation segment to form a continuous, uninterrupted offset corrugation. A plurality of the heat exchanger plates are connected together to form a fill pack.