Membrane Distillation Arrangement Side Inlet Sealing

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Solution Overview

Problem

Existing multilayer membrane distillation arrangements face challenges with sealing integrity and fluid flow distribution due to fluid passages through sealing gaskets, leading to heat loss and difficulties in assembly and disassembly.

Innovation Solution

The configuration of side inlets and outlets within dividers directs fluid flow into and out of the membrane distillation arrangement without passing through fluid seals, enhancing sealing integrity and allowing for independent flow distribution, with a perimeter seal providing a continuous, unbroken seal between layers.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Ease of operation

If fluid passages are extended through sealing gaskets to create inlet and outlet conduits, then fluid flow distribution is achieved, but sealing integrity is compromised

Engineering Contradiction:
Improvefluid flow distributionVSAvoidsealing integrity
Core Design Contradiction:
Ease of operationVSReliability

Solution Approach 1:

The support frame is segmented into multiple sections with inlet and outlet conduits formed separately within the frame structure itself, rather than extending through sealing gaskets. This segmentation allows fluid flow distribution while maintaining seal integrity by keeping passages contained within rigid frame boundaries.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The fluid passage function is extracted from the sealing gasket and relocated to the support frame structure. By removing the requirement for gaskets to contain fluid passages, the sealing function is purified and optimized, while fluid distribution is handled by the dedicated conduit system in the support frame.

Inventive Principle:
Principle #2Taking out (Extraction)

2Reliability

If multiple seals and tighter sealing protocols are used to improve sealing integrity, then sealing reliability is enhanced, but assembly and disassembly difficulty increases

Engineering Contradiction:
Improvesealing integrityVSAvoidassembly and disassembly
Core Design Contradiction:
ReliabilityVSEase of manufacture

Solution Approach 1:

The support frame is divided into modular sections that can be easily assembled and disassembled. Each section maintains its own fluid conduits and sealing interfaces, allowing for simple module replacement without affecting other parts of the system, thus facilitating maintenance while preserving seal integrity.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The sealing system uses visual indicators or color-coded sealing surfaces to ensure proper alignment and sealing during assembly, reducing the need for multiple seals while maintaining reliability through improved assembly accuracy.

Inventive Principle:
Principle #32Color changes

3Ease of operation

If fluid passages are created through sealing gaskets, then inlet and outlet conduits are formed, but heat loss increases

Engineering Contradiction:
Improveconduit formationVSAvoidheat loss
Core Design Contradiction:
Ease of operationVSLoss of energy

Solution Approach 1:

Fluid passages are extracted from the thermal path by relocating them to external conduits in the support frame, away from the membrane and process fluid channels. This separation eliminates heat loss through gasket passages while maintaining effective fluid distribution through the dedicated conduit system.

Inventive Principle:
Principle #2Taking out (Extraction)

Solution Approach 2:

The support frame acts as an intermediary structure that carries fluid conduits separately from the thermal process zones. This mediator structure allows fluid distribution without creating thermal bridges or heat loss paths through the sealing gaskets.

Inventive Principle:
Principle #24Intermediary (Mediator)

4Ease of operation

If aligned passages and apertures are formed through support plates and seals, then fluid flow distribution is achieved, but sealing integrity is compromised

Engineering Contradiction:
Improvefluid flow distributionVSAvoidsealing integrity
Core Design Contradiction:
Ease of operationVSReliability

Solution Approach 1:

The fluid distribution system is segmented into dedicated conduits within the support frame, separate from the sealing interfaces. This eliminates the need for aligned passages through seals, as fluid flow and sealing functions are spatially separated into different structural elements.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The fluid passage function is extracted from the sealing gasket structure and placed in dedicated conduits within the support frame. This extraction allows sealing surfaces to be continuous and intact, while fluid distribution is achieved through the separate conduit system with appropriate connections.

Inventive Principle:
Principle #2Taking out (Extraction)

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 design improves sealing and assembly ease, ensures effective fluid distribution, and reduces heat loss by eliminating fluid passages through seals, resulting in a more efficient and reliable membrane distillation process.

Implementation Method 1

The driving force for the diffusion is a vapour pressure difference created by the temperature difference across the membrane

Methodology Applied
Scientific EffectVapour pressure difference: Vapour Pressure

Implementation Method 2

The driving force for the diffusion is a vapour pressure difference created by the temperature difference across the membrane

Methodology Applied
Scientific EffectTemperature difference: Temperature Gradient

Implementation Method 3

Separation is achieved utilising the relative volatility of various components in the vapourising fluid enabling vapour from components in the vapourising fluid of higher volatility to pass through the membrane pores by a convective or diffusive mechanism

Methodology Applied
Scientific EffectDiffusion: Diffusion

Implementation Method 4

Separation is achieved utilising the relative volatility of various components in the vapourising fluid enabling vapour from components in the vapourising fluid of higher volatility to pass through the membrane pores by a convective or diffusive mechanism

Methodology Applied
Scientific EffectConvection: Convection

Implementation Method 5

The retained components remain in the vapourising fluid by the hydrophobicity of the membrane material which is a barrier to the liquid phase but allows vapour to pass through the membrane

Methodology Applied
Scientific EffectHydrophobicity: Hydrophobe

Implementation Method 6

The vapour penetrates through the porous membrane, and condenses in the cooler fluid or surface on the condensing permeate side

Methodology Applied
Scientific EffectCondensation: Condensation

Data Source

PatentEP2922616B1Membrane distillation arrangement
Publication Date: 2021.05.12 PARKWAY PROCESS TECH PTY LTD
  • EP2922616B1 patent drawingFigure 1~1A
  • EP2922616B1 patent drawingFigure 2~3
  • EP2922616B1 patent drawingFigure 4~5

AI summary

A membrane distillation arrangement (100) comprising: at least two dividers (120), each divider (120) having a top (122) and a base (124) and at least one side (126) which extends between the top (122) and the base (124); at least one transfer element (132) selected from a membrane, heat transfer component or combination thereof, each transfer element (132) having a top (134) and a base (136), each transfer element (132) being supported between two dividers (120); a plurality of perimeter seals (130), at least one perimeter seal (130) extending around the perimeter of the top (134) or the base (136) of each transfer element (132), each perimeter seal (130) forming a substantially fluid tight seal and a fluid flow space (140, 141) between the respective top (134) or base (136) of each transfer element (132) and a respective adjacent face of a divider (120). Each divider (120) includes at least one side inlet (114) and at least one side outlet (116), each side inlet (114) and side outlet (116) extending into the at least one side of each divider (120), and being in fluid communication with the respective fluid flow space (140, 141) formed between the adjacent transfer element (32) and the respective adjacent face of a divider (120).