Electrochemical Cell Deionization Loop for Metal Ion Removal

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Solution Overview

Problem

The degradation of components in hydrogen electrochemical cells, such as fuel cells and electrolyzers, due to metal ions and other impurities leads to efficiency losses and maintenance challenges, as these ions can diffuse into the membrane and cause chemical reactions that reduce cell efficiency and longevity.

Innovation Solution

A deionization subsystem using a selectively binding chelator with pKa values different from the operating pH of the cell, capable of binding metal ions like iron, is integrated into the water recirculation loop or upstream/downstream of the electrolyzer cell, along with a regeneration device to strip bound ions, ensuring minimal interference with hydrogen ions and maintaining membrane integrity.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If a deionization subsystem with selectively binding chelator is introduced to remove metal ions, then membrane degradation is reduced and cell efficiency is maintained, but device complexity increases due to additional subsystem components

Engineering Contradiction:
Improvemembrane integrityVSAvoidsystem complexity
Core Design Contradiction:
ReliabilityVSDevice complexity

Solution Approach 1:

A selectively binding chelator is introduced as an intermediary substance that mediates between metal ions and the membrane. The chelator binds metal ions through coordination chemistry, preventing them from reaching and degrading the membrane while allowing protons to pass through unaffected. This intermediary approach resolves the contradiction by protecting the membrane without requiring complex physical barriers or modification of the membrane structure itself.

Inventive Principle:
Principle #24Intermediary (Mediator)

Solution Approach 2:

The chelator's binding affinity is tuned by adjusting its chemical structure and pKa values to selectively bind metal ions at the operating pH of the electrolyzer. By changing the chemical parameters of the chelator (such as selecting specific functional groups like carboxylic acids, phosphonic acids, or hydroxamic acids), the system achieves selective metal ion removal while maintaining proton conductivity, thus protecting the membrane without adding complex mechanical systems.

Inventive Principle:
Principle #35Parameter changes

2Object-affected harmful factors

If a chelator with pKa values different from operating pH is used to bind metal ions, then selective binding is achieved and proton interference is minimized, but manufacturing precision is required to ensure proper pKa selection

Engineering Contradiction:
Improvemetal ion binding selectivityVSAvoidpKa value selection
Core Design Contradiction:
Object-affected harmful factorsVSManufacturing precision

Solution Approach 1:

The chelator molecule is designed with specific functional groups (carboxylic acids, phosphonic acids, hydroxamic acids, etc.) that have predetermined pKa values. By selecting and combining these functional groups in specific configurations, the chelator's pKa is tuned to be different from the electrolyzer's operating pH (typically 2-14). This parameter tuning ensures that the chelator remains in its binding form at operating conditions, selectively capturing metal ions while not interfering with proton transport through the membrane.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

Rather than requiring ultra-precise manufacturing of the chelator's pKa value, the system uses readily available chelating functional groups with known, well-characterized pKa values. This approach accepts a range of acceptable pKa values rather than demanding exact precision, making the system more manufacturable and less sensitive to manufacturing variations while still achieving effective metal ion removal.

Inventive Principle:
Principle #27Cheap short-living objects (Disposable)

3Reliability

If deionization subsystem is integrated into water recirculation loop, then metal ion removal is achieved, but loss of time occurs during ion binding and regeneration cycles

Engineering Contradiction:
Improvecell efficiencyVSAvoidion removal time
Core Design Contradiction:
ReliabilityVSLoss of time

Solution Approach 1:

The chelator is integrated into the water recirculation loop of the electrolyzer, allowing continuous removal of metal ions as water flows through the system. Rather than requiring periodic batch treatment, the chelator continuously binds metal ions from the recirculating water, maintaining cell efficiency without interrupting operation. The regeneration of the chelator can also be performed continuously or semi-continuously, minimizing downtime.

Inventive Principle:
Principle #20Continuity of useful action

Solution Approach 2:

The chelator acts as a mobile intermediary carried through the water recirculation loop, dynamically binding and transporting metal ions away from the membrane. This continuous intermediary action occurs throughout the recirculation cycle, efficiently removing ions without requiring separate treatment steps that would consume time and interrupt electrolyzer operation.

Inventive Principle:
Principle #24Intermediary (Mediator)

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 captures and removes unwanted metal ions, reducing membrane degradation and maintaining cell efficiency over time, thereby prolonging the lifespan and performance of hydrogen electrochemical systems.

Implementation Method 1

a deionization subsystem using a selectively binding chelator with pKa values different from the operating pH of the cell, capable of binding metal ions like iron

Methodology Applied
Scientific EffectChelation: Adsorption

Data Source

PatentUS20250003096A1Electrochemical cell deionization system
Publication Date: 2025.01.02 ROBERT BOSCH GMBH
  • US20250003096A1 patent drawing
  • US20250003096A1 patent drawing
  • US20250003096A1 patent drawing

AI summary

A hydrogen electrochemical system includes a cell including a membrane electrolyte and catalyst-loaded catalyst layers and a deionization subsystem including a selectively binding chelator binding one or more metal ions, the selectively binding chelator having pKa value(s) at which its hydrogen(s) dissociate, the pKa value(s) being different from pH value(s) of the cell in operation, the deionization subsystem being located in a water recirculation loop of the cell.