Alternating Pore Gas Diffusion Layer for Fuel Cells

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Solution Overview

Problem

The existing gas diffusion layers in fuel cells face issues with water flooding and clogging due to the selective movement of product water, which blocks the transfer of reactive gases and deteriorates cell performance.

Innovation Solution

A gas diffusion layer with alternately formed fine and coarse pore areas on a carbon fiber support, allowing reactive gases to flow through fine pores and product water to flow through coarse pores, facilitating separate and efficient transfer of both components.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Quantity of substance

If product water moves through the gas diffusion layer via capillary pressure difference, then water removal is facilitated, but water concentrates in selected channels causing flooding and clogging

Engineering Contradiction:
Improveproduct water removalVSAvoidgas transfer continuity
Core Design Contradiction:
Quantity of substanceVSReliability

Solution Approach 1:

The gas diffusion layer is segmented into multiple types of pores (first type with smaller pore size and second type with larger pore size) that are distributed in an alternating pattern. This segmentation allows different pore types to perform different functions: smaller pores for gas transport and larger pores for water removal, preventing water concentration and flooding in any single channel while maintaining continuous gas transfer pathways.

Inventive Principle:
Principle #1Segmentation

2Ease of manufacture

If uniform pore size is used in the gas diffusion layer, then manufacturing is simplified, but water flooding occurs due to selective channel clogging

Engineering Contradiction:
Improvepore structure fabricationVSAvoidcell performance stability
Core Design Contradiction:
Ease of manufactureVSReliability

Solution Approach 1:

Different regions of the gas diffusion layer are designed with different pore characteristics. The layer contains first type pores with a first pore size and second type pores with a second pore size larger than the first. These different pore types are arranged in an alternating pattern, creating local variations in pore quality that optimize both water removal and gas transfer functions in different locations throughout the layer.

Inventive Principle:
Principle #3Local quality

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 design prevents water clogging by selectively directing product water through larger pores, ensuring uninterrupted gas transfer and improving fuel cell performance by maintaining a balance between pore sizes and proportions.

Implementation Method 1

the liquid-phase product water is moved through difference in capillary pressure in the gas diffusion layer 20 from the fine pore layer 22 to the carbon fiber support 21

Methodology Applied
Scientific EffectCapillary pressure: Capillary Pressure

Implementation Method 2

the gas diffusion layer 20 is obtained by forming a fine porous layer 22 on one or two surfaces of a carbon fiber support 21 generally including a porous carbon paper

Methodology Applied
Scientific EffectPorosity: Porosity

Data Source

PatentUS10593957B2Gas diffusion layer for fuel cells and method of manufacturing the same
Publication Date: 2020.03.17 HYUNDAI MOTOR CO LTD
  • US10593957B2 patent drawing
  • US10593957B2 patent drawing
  • US10593957B2 patent drawing

AI summary

In one embodiment, a gas diffusion layer for fuel cells includes a fine porous layer formed on a carbon fiber support and being interposed between a membrane-electrode assembly (MEA) and a separator. The carbon fiber support includes a fine pore area having a predetermined average pore size in a separator direction (thickness direction) in the membrane electrode assembly, and a coarse pore area having a larger predetermined average pore size than the average pore size of the fine pore area in the separator direction (thickness direction) in the membrane electrode assembly. The fine pore area and the coarse pore area are alternately formed.