Membrane Electrode Assembly With Porous Interlayer for CO2 Retention

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Solution Overview

Problem

Existing electrochemical systems for CO2 reduction face challenges in efficiently converting CO2 into valuable carbon compounds while minimizing carbonate formation and loss of CO2 as a raw material, particularly due to inefficiencies in ion exchange membranes and intermediate layers.

Innovation Solution

A membrane electrode assembly with a cation-exchange membrane and a hydrophilic, conductive porous intermediate layer between the electrodes, which includes an electrolyte solution channel, reduces carbonate formation and minimizes CO2 loss by controlling ion movement and reaction pathways.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If an ion-exchange membrane is used to separate electrodes in CO2 electrolysis, then ion transport is enabled, but carbonate formation occurs and CO2 is lost

Engineering Contradiction:
Improveion transport efficiencyVSAvoidCO2 loss
Core Design Contradiction:
ReliabilityVSLoss of substance

Solution Approach 1:

A hydrophilic intermediate layer is introduced between the ion-exchange membrane and the cathode to act as a mediator. This layer prevents direct contact between CO2 and the membrane, blocking the harmful chemical reaction that produces carbonates, while still allowing efficient ion transport through its hydrophilic porous structure.

Inventive Principle:
Principle #24Intermediary (Mediator)

Solution Approach 2:

The patent converts the hydrophilic property of the intermediate layer, which could be seen as attracting unwanted water molecules, into a benefit by using it to preferentially transport water ions while blocking CO2, thus protecting the CO2 feedstock from being consumed in unwanted side reactions.

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

2Reliability

If a conventional intermediate layer is used, then electrode protection is provided, but CO2 permeation increases leading to raw material loss

Engineering Contradiction:
Improveelectrode protectionVSAvoidCO2 permeation loss
Core Design Contradiction:
ReliabilityVSLoss of substance

Solution Approach 1:

The intermediate layer is designed with specific local properties: hydrophilic character to attract and transport water ions, controlled porosity (30-70%) to allow ion passage while blocking CO2, and specific thickness (10-500 μm) to provide protection without excessive CO2 permeation. These localized quality adjustments resolve the contradiction between protection and permeation control.

Inventive Principle:
Principle #3Local quality

3Stability of the object's composition

If hydrophobic materials are used in the intermediate layer, then water management is improved, but ion conductivity decreases

Engineering Contradiction:
Improvewater managementVSAvoidion conductivity
Core Design Contradiction:
Stability of the object's compositionVSReliability

Solution Approach 1:

The patent changes the key parameter of the intermediate layer from hydrophobic to hydrophilic character. This parameter change fundamentally alters the layer's interaction with water and ions, enabling both effective water management and high ion conductivity simultaneously, as the hydrophilic structure naturally facilitates ion transport while maintaining water balance.

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

The assembly effectively enhances the conversion of CO2 into carbon compounds like carbon monoxide, methane, and ethanol, while maintaining high Faradaic efficiency and reducing carbonate deposition, thus improving the overall efficiency and longevity of the electrochemical process.

Implementation Method 1

an ion-exchange membrane provided between the first electrode and the second electrode

Methodology Applied
Scientific EffectIon exchange: Ion Exchange

Implementation Method 2

an intermediate layer between the second electrode and the ion-exchange membrane, wherein the intermediate layer is a conductive porous body

Methodology Applied
Scientific EffectPorosity: Porosity

Data Source

PatentUS20260081195A1Membrane electrode assembly, electrochemical cell, stack, and electrolytic system
Publication Date: 2026.03.19 KK TOSHIBA
  • US20260081195A1 patent drawing
  • US20260081195A1 patent drawing
  • US20260081195A1 patent drawing

AI summary

A membrane electrode assembly includes a first electrode, a second electrode, an ion-exchange membrane provided between the first electrode and the second electrode, and an intermediate layer between the second electrode and the ion-exchange membrane. The intermediate layer is a conductive porous body.