Electrodialysis Deionization Battery Cell Segmentation

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Solution Overview

Problem

Current desalination technologies face challenges such as high energy demands, environmental concerns, and material issues related to corrosion and fouling of membranes, limiting their widespread use for producing fresh water from saline sources.

Innovation Solution

The development of a deionization battery cell that includes intercalation host electrodes and an ion exchange membrane assembly with alternating anion and cation exchange membranes, separated by water stream compartments, which uses electric current to separate ions from saline water, producing fresh water and a concentrated brine stream.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Use of energy by moving object

If conventional desalination processes are used, then water can be desalinated, but high energy demands are required

Engineering Contradiction:
Improveenergy demandVSAvoiddesalination efficiency
Core Design Contradiction:
Use of energy by moving objectVSProductivity

Solution Approach 1:

The device is segmented into multiple compartments separated by alternating cation-exchange membranes and anion-exchange membranes, creating a series of chambers that process water in stages. This segmentation allows for progressive ion removal while distributing energy consumption across multiple smaller units rather than requiring high energy in a single stage, thereby reducing overall energy demand while maintaining productivity.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The electrodialysis process operates through periodic application of electric current to drive ion migration across membranes. By applying electric potential periodically and reversing polarity in alternating chambers, the system efficiently removes ions through controlled periodic action rather than continuous high-energy input, reducing energy demand while sustaining desalination productivity.

Inventive Principle:
Principle #19Periodic action

2Object-affected harmful factors

If conventional desalination processes are used, then water can be desalinated, but environmental concerns arise

Engineering Contradiction:
Improveenvironmental impactVSAvoiddesalination output
Core Design Contradiction:
Object-affected harmful factorsVSProductivity

Solution Approach 1:

The system converts the harmful effect of concentrated brine waste into a beneficial byproduct stream that can be separately managed and potentially reused. By efficiently concentrating salts in specific chambers through electrodialysis, the process transforms what would be dispersed environmental pollution into a concentrated stream suitable for industrial reuse or controlled disposal, reducing environmental impact while maintaining high desalination productivity.

Inventive Principle:
Principle #22Blessing in disguise (Convert harm into benefit)

Solution Approach 2:

The process separates and recovers valuable components from the water stream while discarding only the necessary minimal waste. Through selective ion removal via ion-exchange membranes, the system recovers fresh water as the primary product and concentrates salts in a manageable brine stream, minimizing environmental discharge requirements and enabling sustainable desalination operations.

Inventive Principle:
Principle #34Discarding and recovering

3Reliability

If conventional membranes are used in desalination, then ion separation can be achieved, but material issues related to corrosion and fouling occur

Engineering Contradiction:
Improvemembrane lifespanVSAvoidmembrane maintenance
Core Design Contradiction:
ReliabilityVSEase of manufacture

Solution Approach 1:

The system employs composite membrane structures combining ion-exchange resins with supportive polymer matrices, creating materials that resist corrosion and fouling. These composite membranes integrate the selective ion transport properties of ion-exchange materials with the mechanical strength and chemical stability of polymer supports, enhancing reliability and reducing maintenance requirements while maintaining ease of manufacture through established polymer processing techniques.

Inventive Principle:
Principle #40Composite materials

Solution Approach 2:

The membranes are designed with optimized parameters including cross-linking density, pore size distribution, and functional group composition to resist corrosion and fouling. By adjusting these parameters during manufacturing, the membranes achieve enhanced chemical stability and anti-fouling properties, extending service life and reducing maintenance frequency without complicating the manufacturing process.

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 solution effectively reduces the energy requirements for desalination, minimizes environmental impact, and extends the lifespan of membrane components by using a dual-ion electrochemical deionization process, thereby enhancing the efficiency and sustainability of water desalination.

Implementation Method 1

an ion exchange membrane assembly including a plurality of anion exchange membranes separated from each other, and from one or more cation exchange membranes positioned between the anion exchange membranes

Methodology Applied
Scientific EffectIon exchange: Ion Exchange

Implementation Method 2

dual-ion electrochemical deionization process

Methodology Applied
Scientific EffectElectrochemical deionization: Electrolysis

Data Source

PatentUS12234164B2Electrodialysis deionization battery cells
Publication Date: 2025.02.25 ROBERT BOSCH GMBH
  • US12234164B2 patent drawing
  • US12234164B2 patent drawing
  • US12234164B2 patent drawing

AI summary

A deionization battery cell including a first electrode compartment containing a first intercalation host electrode and includes a first water stream compartment in fluid communication with the first electrode compartment. The deionization battery cell further includes a second electrode compartment containing a second intercalation host electrode and a second water stream compartment in fluid communication with the second electrode compartment. The deionization battery cell also includes an ion exchange membrane assembly including a plurality of anion exchange membranes separated from each other, and from one or more cation exchange membranes positioned between the anion exchange membranes, by a plurality of intervening water stream compartments. The first and second water stream compartments are separated from one another by the ion exchange membrane assembly.