Multi-Interface Membrane Electrode Assembly for Fuel Cells

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Solution Overview

Problem

Proton exchange membrane fuel cells (PEMFCs) face challenges in achieving high power production, particularly at low relative humidity and high temperatures, due to issues with reactant gas diffusion and water management, which are exacerbated by dense catalyst layers and symmetric gas diffusion medium (GDM) pairings.

Innovation Solution

The implementation of a dual-layered cathode catalyst coating with a high porosity layer and a low porosity layer, each with a different carbon catalyst, and asymmetric GDM pairings that enhance water management and proton conductivity, allowing for improved reactant gas diffusion and water removal.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Strength

If a dense catalyst layer is used to improve mechanical integrity and catalyst utilization, then structural strength is improved, but reactant gas diffusion is hindered

Engineering Contradiction:
Improvemechanical integrityVSAvoidreactant gas diffusion
Core Design Contradiction:
StrengthVSProductivity

Solution Approach 1:

The catalyst layer is segmented into multiple layers with different porosity characteristics. The multi-layer structure includes a first catalyst layer with higher porosity for gas diffusion and a second catalyst layer with lower porosity for mechanical support, resolving the contradiction between structural integrity and gas transport

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

Different regions of the catalyst layer are assigned different porosity properties to fulfill different functions. The layer adjacent to the gas diffusion medium has higher porosity for reactant ingress, while the layer adjacent to the membrane has lower porosity for structural stability, achieving both requirements simultaneously

Inventive Principle:
Principle #3Local quality

2Device complexity

If a symmetric GDM pairing is used to simplify manufacturing, then device complexity is reduced, but water management performance deteriorates

Engineering Contradiction:
Improvemanufacturing simplicityVSAvoidwater management performance
Core Design Contradiction:
Device complexityVSProductivity

Solution Approach 1:

The symmetric GDM pairing is replaced with an asymmetric configuration where the anode and cathode gas diffusion media have different porosity and hydrophobicity characteristics. This asymmetric design enables optimized water removal at the cathode while maintaining adequate gas supply at the anode, significantly improving water management performance

Inventive Principle:
Principle #4Asymmetry

3Productivity

If high porosity catalyst layers are used to enhance gas diffusion, then reactant gas diffusion is improved, but mechanical strength is reduced

Engineering Contradiction:
Improvereactant gas diffusionVSAvoidmechanical strength
Core Design Contradiction:
ProductivityVSStrength

Solution Approach 1:

The catalyst layer is divided into multiple functional layers where the porosity requirement for gas diffusion is satisfied in the outer layer while the mechanical strength requirement is satisfied in the inner layer, eliminating the need to compromise either property

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The multi-layer catalyst structure functions as a composite material system where layers with different porosity and mechanical properties are combined to achieve overall performance that satisfies both gas diffusion and structural requirements

Inventive Principle:
Principle #40Composite materials

4Device complexity

If conventional single-layer cathode catalyst coating is used to simplify structure, then device complexity is reduced, but power production at low humidity deteriorates

Engineering Contradiction:
Improvestructure simplicityVSAvoidpower production at low humidity
Core Design Contradiction:
Device complexityVSProductivity

Solution Approach 1:

The single-layer cathode catalyst coating is segmented into multiple layers with different porosity characteristics. This multi-layer structure enables optimized gas diffusion pathways and water management specifically tailored for low humidity operation, significantly improving power production without excessive complexity

Inventive Principle:
Principle #1Segmentation

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 results in enhanced power production, reduced ohmic resistance, and improved oxygen transport, enabling higher performance in challenging conditions without the need for a humidifier, thus simplifying and miniaturizing the fuel cell stack.

Implementation Method 1

rapid ingress of the respective reactant gases...enhanced power production...improved oxygen transport

Methodology Applied
Scientific EffectDiffusion: Diffusion

Implementation Method 2

egress of product water from the cathode...improved water management

Methodology Applied
Scientific EffectPorosity: Porosity

Implementation Method 3

The protons pass through the membrane to the cathode...proton conductivity

Methodology Applied
Scientific EffectIon Exchange: Ion Exchange

Implementation Method 4

electrochemical device that converts a fuel and an oxidizing agent into electricity...catalysts, which catalyze the respective reaction

Methodology Applied
Scientific EffectCatalysis: Catalysis

Data Source

PatentUS11616247B2Multi-interface membrane electrode assembly
Publication Date: 2023.03.28 THE UNITED STATES OF AMERICA AS REPRESENTED BY THE SECRETARY OF THE NAVY
  • US11616247B2 patent drawing
  • US11616247B2 patent drawing
  • US11616247B2 patent drawing

AI summary

A fuel cell membrane electrode assembly having: a proton exchange membrane, an anode catalyst coating on one side of the membrane, and a cathode catalyst coating on the other side of the membrane. The cathode catalyst coating has at least two carbon catalyst layers, with a low porosity layer adjacent to a high porosity layer. The high porosity layers have a volume fraction that is higher than the volume fraction of the low porosity layers.