Hollow Fiber Degasification Modules for Balanced Parallel Flow

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Solution Overview

Problem

The degasification performance of a system with connected degasification modules is lower when liquid is supplied in parallel due to varying flow rates between upstream and downstream modules, leading to decreased overall performance.

Innovation Solution

The system is configured to balance pressure losses across connected degasification modules by increasing pressure loss in downstream modules, reducing flow rate deviations through adjustments in pipe diameters, opening sizes, and membrane densities, among other factors.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If liquid supply paths of multiple degasification modules are connected in series with parallel supply to hollow fiber membranes, then the system can handle increased flow rates and size, but the flow rate distribution becomes uneven between upstream and downstream modules, deteriorating overall degasification performance

Engineering Contradiction:
Improveflow rateVSAvoiddegasification performance
Core Design Contradiction:
ProductivityVSReliability

Solution Approach 1:

The patent applies local quality by creating different pressure loss characteristics in different parts of the system. Specifically, the connection supply pipe has varying inner diameters (smaller at downstream side), and the hollow fiber membrane bundles have different configurations (different numbers of membranes or different membrane areas) in upstream versus downstream modules. This local differentiation ensures that downstream modules, which naturally receive higher flow rates, have higher pressure losses to compensate and balance the flow distribution across all modules, thereby maintaining reliable degasification performance throughout the system.

Inventive Principle:
Principle #3Local quality

2Ease of manufacture

If the same number of hollow fiber membranes are used in all degasification modules, then manufacturing is simplified, but flow rate deviations between upstream and downstream modules cause uneven degasification performance

Engineering Contradiction:
Improvemodule uniformityVSAvoidflow rate distribution
Core Design Contradiction:
Ease of manufactureVSReliability

Solution Approach 1:

The patent implements local quality by deliberately making the hollow fiber membrane bundles different between upstream and downstream modules. The downstream modules have either more hollow fiber membranes or larger membrane areas compared to upstream modules. This local variation compensates for the higher flow rates that naturally occur in downstream modules, ensuring that each module operates at optimal efficiency despite the series connection configuration. This approach maintains manufacturing feasibility while solving the flow distribution problem.

Inventive Principle:
Principle #3Local quality

3Device complexity

If the connection supply pipe has uniform inner diameter throughout, then the system structure is simpler, but pressure loss cannot compensate for flow velocity differences, resulting in poor flow rate distribution

Engineering Contradiction:
Improvepipe configurationVSAvoidflow rate balance
Core Design Contradiction:
Device complexityVSReliability

Solution Approach 1:

The patent applies local quality to the connection supply pipe by varying its inner diameter along the flow direction. The pipe has a smaller inner diameter at the downstream side compared to the upstream side. This gradual reduction in diameter creates increasing pressure losses in downstream sections, which compensates for the higher flow velocities that naturally develop in series-connected modules. This localized geometric variation ensures balanced flow rate distribution without requiring complex active control systems.

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

This configuration improves the overall degasification performance by minimizing flow rate differences between upstream and downstream modules, enhancing the system's efficiency.

Implementation Method 1

a degasification module that degasifies a liquid using hollow fiber membranes

Methodology Applied
Scientific EffectPermeation: Permeation

Implementation Method 2

the pressure loss of the liquid from the supply port of the connection supply pipe to the discharge ports of the downstream side degasification module is larger than the pressure loss of the liquid from the supply port of the connection supply pipe to the discharge ports of the upstream side degasification module

Methodology Applied
Scientific EffectPressure loss: Pressure Drop

Data Source

PatentEP3858452B1Degasification system and liquid degasification method
Publication Date: 2025.10.29 DIC CORP
  • EP3858452B1 patent drawingFigure 1
  • EP3858452B1 patent drawingFigure 2
  • EP3858452B1 patent drawingFigure 3

AI summary

A degasification system includes a degasification unit in which a plurality of degasification modules degasifying a liquid are connected, wherein each of the plurality of degasification modules has a hollow fiber membrane bundle having a plurality of hollow fiber membranes arranged around a liquid supply path through which a liquid is supplied, and a module container which houses the hollow fiber membrane bundle, wherein the degasification unit has a connection supply pipe which connects the liquid supply paths of the plurality of degasification modules in series and in which openings through which the liquid passes are formed at positions corresponding to the plurality of degasification modules such that the liquid is supplied to the hollow fiber membrane bundles of the plurality of degasification modules in parallel, and wherein the degasification unit is configured such that a pressure loss of the liquid from a supply port of the connection supply pipe through which the liquid is supplied to the discharge ports of a downstream side degasification module is larger than a pressure loss of the liquid from the supply port to the discharge ports of an upstream side degasification module.