EDI Module Block Arrangement for Current Efficiency

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Solution Overview

Problem

Existing EDI modules face challenges with complex manufacturing and assembly, insufficient interaction of flow-through channels with ion-exchange materials, and decreased current efficiency, leading to high costs and inefficient purification of aqueous liquids.

Innovation Solution

The EDI module features a unique arrangement of anion-exchange and cation-exchange material blocks within the diluate compartment, with complementary protrusions and recesses, allowing for efficient ion removal and regeneration without recombination, thereby enhancing purification performance and reducing assembly complexity.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Measurement precision

If ion-exchange materials are arranged in parallel layers adjacent to membranes, then the active surface for ion removal is increased, but the flow path becomes long and requires high membrane area per volume

Engineering Contradiction:
Improvepurification performanceVSAvoidmembrane area per volume
Core Design Contradiction:
Measurement precisionVSDevice complexity

Solution Approach 1:

The patent transitions from a two-dimensional layered arrangement (parallel to membranes) to a three-dimensional block configuration. The ion-exchange blocks are positioned perpendicular to the membranes, creating a volumetric utilization that reduces the required membrane area while maintaining effective ion removal surface area.

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

Solution Approach 2:

The ion-exchange materials are divided into separate cation-exchange blocks and anion-exchange blocks positioned at opposite ends of the diluate compartment. This segmentation allows each block to interact efficiently with the liquid flow independently, reducing the overall path length required for purification.

Inventive Principle:
Principle #1Segmentation

2Productivity

If grafted materials are used to intensify purification, then ion removal efficiency increases, but assembly complexity and manufacturing difficulty increase

Engineering Contradiction:
Improvepurification intensityVSAvoidassembly complexity
Core Design Contradiction:
ProductivityVSEase of manufacture

Solution Approach 1:

The grafted materials are manufactured as pre-formed blocks with standardized dimensions and configurations. These modular blocks can be easily assembled into the diluate compartment without complex manufacturing processes, separating the intensification function from the assembly complexity.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The block structure acts as an intermediary form that bridges the gap between the intensive purification capability of grafted materials and the ease of assembly requirement. The blocks encapsulate the complex grafted material structure while presenting a simple geometric form for assembly.

Inventive Principle:
Principle #24Intermediary (Mediator)

3Use of energy by moving object

If ion-exchange materials are positioned to maximize contact with liquid flow, then current efficiency increases, but manufacturing and assembly become more difficult

Engineering Contradiction:
Improvecurrent efficiencyVSAvoidmanufacturing complexity
Core Design Contradiction:
Use of energy by moving objectVSDevice complexity

Solution Approach 1:

The blocks are positioned perpendicular to the liquid flow direction, maximizing the contact surface area between the ion-exchange materials and the flowing liquid. This three-dimensional arrangement optimizes current efficiency while maintaining a simple block geometry that is easy to manufacture and assemble.

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

Solution Approach 2:

The cation-exchange block and anion-exchange block are positioned asymmetrically at opposite ends of the diluate compartment, optimized for their respective ion removal functions. This asymmetric arrangement maximizes current efficiency by positioning each block where it can most effectively intercept ions in the liquid flow.

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

This configuration improves the quality of purified water, increases current efficiency, and reduces operational and manufacturing costs, enabling the production of high-purity water with a more straightforward assembly process.

Implementation Method 1

sorption of these ions to a material capable of exchanging these ions either for hydrogen ions (for cations) or hydroxide ions (for anions)

Methodology Applied
Scientific EffectIon exchange: Ion Exchange

Implementation Method 2

transfer of ions under the influence of an electric field between an anode and a cathode

Methodology Applied
Scientific EffectElectrophoresis: Electrophoresis

Implementation Method 3

sorption of these ions to a material capable of exchanging these ions

Methodology Applied
Scientific EffectSorption: Sorption

Data Source

PatentEP2888205B1Improved electrodeionization module and apparatus
Publication Date: 2018.10.24 MERCK PATENT GMBH
  • EP2888205B1 patent drawingFigure 1
  • EP2888205B1 patent drawingFigure 2
  • EP2888205B1 patent drawingFigure 3

AI summary

The present invention relates to an improved electrodeionization (EDI) module and apparatus adapted to transfer ions present in a liquid under the influence of an electric field. In particular, the EDI module according to the present invention comprises a cathode (7) and an anode (8) spaced apart from the cathode (7), having therebetween at least two ion permeable membranes comprising at least one anion permeable membrane (2) and at least one cation permeable membrane (1) and delimiting one or more diluate compartments (5) and one or more concentrate compartments (6), wherein at least one diluate compartment (5) contains at least two blocks, a first block containing anion-exchange material (4) and a second block containing cation-exchange material (3), wherein a surface of said first block is adjacent to an anion permeable membrane (2) and a surface of said second block is adjacent to a cation permeable membrane (1) and wherein said two blocks are arranged side by side in a liquid-passing direction thereby forming an interface between said two blocks such that said interface is spaced apart from said anion permeable membrane (2) and said cation permeable membrane (1) and a straight line in a liquid- passing direction may pass the interface between said two blocks at least one time.