Cooling Tower Fill Sheet Airflow Channels and Mist Reduction

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Solution Overview

Problem

Current fill sheet arrangements in direct heat exchange units, such as cooling towers, face inefficiencies in heat and mass transfer due to suboptimal air flow pathways and liquid distribution, leading to reduced thermal efficiency and increased evaporative liquid mist at the outlet.

Innovation Solution

The use of adjacent fill sheets with male and female separators, ridges, grooves, angled sections, and a transition zone to create efficient air flow channels and reduce liquid mist, along with an air inlet louver zone for improved air distribution and heat transfer, enhances the thermal efficiency of the direct heat exchanger.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If traditional fill sheet arrangements are used, then the structure is simple, but heat and mass transfer efficiency is reduced due to suboptimal air flow pathways

Engineering Contradiction:
Improveheat and mass transfer efficiencyVSAvoidfill sheet structure complexity
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The fill sheet is segmented into multiple functional zones including ridges, grooves, angled raised sections, and angled lowered sections. These segments create differentiated air flow channels (major and minor air paths) that optimize heat and mass transfer by directing air flow through specific pathways while maintaining a relatively simple overall sheet structure.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

Different regions of the fill sheet are given different local characteristics through the ridges, grooves, and angled sections. The male and female separators create localized air flow channels with specific flow patterns, while the transition zone provides localized liquid distribution control. This local differentiation maximizes transfer efficiency without requiring complex overall structure.

Inventive Principle:
Principle #3Local quality

2Productivity

If air flow channels are optimized with separators, then heat transfer improves, but device complexity increases

Engineering Contradiction:
Improveheat transfer rateVSAvoidair flow channel structure
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The male and female separators are merged with the ridges and grooves of the fill sheet, integrating the air flow channel formation into the basic fill sheet structure rather than adding separate components. This merging creates efficient air flow channels while minimizing additional structural complexity.

Inventive Principle:
Principle #5Merging (Combining)

Solution Approach 2:

The separators extend into the air flow direction (third dimension relative to the sheet plane), creating three-dimensional air flow channels between the fill sheets. This dimensional approach optimizes air flow pathways without requiring complex two-dimensional patterns, achieving efficient heat transfer through vertical separation of air and liquid phases.

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

3Productivity

If transition zone is added to reduce liquid mist, then thermal efficiency improves, but fill sheet complexity increases

Engineering Contradiction:
Improvethermal efficiencyVSAvoidfill sheet structure
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The transition zone is positioned at the outlet side edge of the fill sheet to preliminarily redirect liquid flow before it reaches the mist eliminator. This preliminary action prevents liquid mist formation at the outlet by gradually changing flow direction through the transition zone geometry, improving thermal efficiency without requiring complex liquid control mechanisms throughout the entire fill sheet.

Inventive Principle:
Principle #10Preliminary action

4Productivity

If angled sections are used to nudge air flow, then mass transfer rate increases, but manufacturing precision requirements increase

Engineering Contradiction:
Improvemass transfer rateVSAvoidangled section geometry
Core Design Contradiction:
ProductivityVSManufacturing precision

Solution Approach 1:

The angled raised and lowered sections use moderate angle parameters that provide effective air flow redirection and mass transfer enhancement while remaining manufacturable. The angles are optimized to create sufficient flow disruption for improved transfer rates without requiring extremely precise manufacturing tolerances. The geometry parameters balance performance with manufacturing feasibility.

Inventive Principle:
Principle #35Parameter changes

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 configuration improves air flow and heat transfer rates by creating specific air flow channels and reducing evaporative liquid mist, thereby increasing the thermal efficiency of the direct heat exchanger and minimizing liquid reaching the mist eliminator.

Implementation Method 1

The air interacts with the evaporative liquid for heat and mass transfer

Methodology Applied
Scientific EffectHeat transfer: Convection

Implementation Method 2

an evaporative liquid, usually water, coursing over the material

Methodology Applied
Scientific EffectEvaporation: Evaporation

Data Source

PatentEP3027999B1Cooling tower fill
Publication Date: 2022.11.30 BALTIMORE AIRCOIL CO INC
  • EP3027999B1 patent drawingFigure 1
  • EP3027999B1 patent drawingFigure 2
  • EP3027999B1 patent drawingFigure 3~6

AI summary

A fill sheet for use in a fill arrangement in a direct heat exchange section of a cooling tower is provided. Each fill sheet includes ridges, grooves, separators, that improve the performance of the fill sheet arrangement when installed as a direct heat exchange section of a cooling tower. The separators are located in minor air paths between the fill sheet to improve the air flow capabilities and performance of the direct heat exchange section.