Hollow Fiber Membrane Module with Vertical Diffuser Tubes

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Solution Overview

Problem

Existing filtration devices face inefficiencies in removing suspension components from membrane surfaces and between membranes, leading to reduced filtration performance and increased device size due to inadequate air diffusion, particularly in densely packed hollow fiber membrane modules.

Innovation Solution

A filtration device with a membrane module featuring bundled hollow fiber membranes and diffuser tubes inserted co-directionally across the membrane axes, allowing for efficient air bubbling and vibration of membranes, enabling effective removal of deposits while allowing high-density membrane arrangement and downsizing of the device.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If air diffusion is performed all over the hollow fiber membranes from diffuser openings on a diffuser plate, then air diffusion coverage is improved, but the device size increases due to required spacing between membrane modules

Engineering Contradiction:
Improveair diffusion coverageVSAvoiddevice size
Core Design Contradiction:
ReliabilityVSVolume of stationary object

Solution Approach 1:

The diffuser is divided into multiple diffuser plates arranged in the vertical direction, each with diffuser openings at different positions. This segmentation allows air to be diffused at multiple levels throughout the membrane bundle, improving air diffusion coverage without requiring horizontal spacing between modules, thus maintaining compact device size.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The invention transitions from horizontal air diffusion (single diffuser plate) to vertical air diffusion by arranging multiple diffuser plates at different heights. This dimensional change allows air to reach membranes throughout the bundle volume, improving coverage while enabling high-density membrane arrangement in a compact vertical configuration.

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

2Productivity

If hollow fiber membranes are disposed in high density, then filtration performance is improved, but air diffusion to between membranes becomes insufficient

Engineering Contradiction:
Improvefiltration performanceVSAvoidair diffusion to between membranes
Core Design Contradiction:
ProductivityVSReliability

Solution Approach 1:

Multiple diffuser plates are positioned at different vertical levels within the membrane bundle, creating segmented air diffusion zones. This allows air to penetrate between membranes at multiple heights, ensuring thorough cleaning of densely packed membranes that would be inaccessible from a single diffuser location.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The invention introduces vertical distribution of diffuser openings throughout the membrane bundle height, enabling air to reach between densely packed membranes in the radial direction while maintaining high membrane density. This multi-level approach overcomes the limitation of single-plane air diffusion.

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

3Ease of manufacture

If only one end (lower end) of hollow fiber membranes is open, then membrane fixing is simplified, but air diffusion to inner surface of membranes is insufficient

Engineering Contradiction:
Improvemembrane fixing simplicityVSAvoidair diffusion to inner surface
Core Design Contradiction:
Ease of manufactureVSReliability

Solution Approach 1:

Multiple diffuser plates are positioned at different vertical levels, with diffuser openings oriented to blow air toward the membrane bundle center. This segmented vertical arrangement ensures air reaches the inner surfaces of membranes at multiple heights, improving cleaning effectiveness while maintaining the simple one-end-open configuration.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

Instead of opening both ends of membranes or reversing the diffuser orientation, the invention inverts the approach by using multiple vertically distributed diffuser plates that blow air inward toward the bundle center, effectively reaching inner membrane surfaces while keeping the one-end-open simplicity.

Inventive Principle:
Principle #13The other way round (Inversion)

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 solution enhances cleaning efficiency and filtration performance by ensuring thorough air diffusion to all membrane surfaces and between membranes, allowing for a higher density of hollow fiber membranes and a more compact filtration device design.

Implementation Method 1

introduces air from the lower part of the membrane module in a state where an immersion tank is filled with a liquid to be treated and separates deposits on the surface of membranes by means of air bubbling which gives vibration to hollow fiber membranes with provided bubbles

Methodology Applied
Scientific EffectAir bubbling: Bubble

Implementation Method 2

separates deposits on the surface of membranes by means of air bubbling which gives vibration to hollow fiber membranes with provided bubbles

Methodology Applied
Scientific EffectVibration: Vibration

Implementation Method 3

performing solid-liquid separation by immersion type suction filtration or external pressure filtration by allowing a liquid containing suspension components to permeate a membrane module

Methodology Applied
Scientific EffectPermeation: Permeation

Data Source

PatentEP1716914B1Hollow fibre filtration device with aeration tubes
Publication Date: 2009.07.22 MAEZAWA IND
  • EP1716914B1 patent drawingFigure 1
  • EP1716914B1 patent drawingFigure 2
  • EP1716914B1 patent drawingFigure 3

AI summary

There is provided a compact filtration device capable of efficiently separate and remove suspension components adhered to membrane surfaces or to between membranes by allowing bubbling action by means of bubbles from an air diffusion tube to effectively affect the entire hollow fiber membrane, and capable of disposing inside hollow fiber membranes in high density. In a filtration device 11 for performing solid-liquid separation by allowing a liquid to be treated 12 containing suspension components to permeate a membrane module 14 for immersion type suction filtration or external pressure filtration, said membrane module 14 is formed from bundled membranes 16 in which a multiplicity of hollow fiber membranes 15 with their axes being in the vertical direction are contacted closely with each other at the upper and lower ends thereof, and a diffuser tube 21 is threaded into between said multiplicity of hollow fiber membranes 15 for insertion at the lower part of the bundled membrane 16.