Fuel Cell Catalyst with Segmented Pores for Gas Transport

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Solution Overview

Problem

Existing polymer electrolyte fuel cells face challenges in reducing the cost of noble metal catalysts like platinum and maintaining catalyst activity and gas transportability, particularly due to issues with catalyst metal and electrolyte contact and gas transport resistance under high load conditions.

Innovation Solution

A catalyst with a specific pore distribution, featuring micropores and mesopores that allow catalyst metals to be supported inside mesopores, preventing contact with the electrolyte while ensuring efficient gas transport through micropores, thereby enhancing catalyst activity and power generation performance.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If catalyst metals are supported inside fine pores which the electrolyte cannot enter, then contact between electrolyte and catalyst metal particles is prevented, but gas transport distance is increased and gas transportability is deteriorated

Engineering Contradiction:
Improvecatalyst activityVSAvoidgas transportability
Core Design Contradiction:
ReliabilityVSProductivity

Solution Approach 1:

The catalyst structure is segmented into two distinct pore systems: fine pores (0.3-1 nm) for electrolyte exclusion and protection of catalyst activity, and coarse pores (1-10 nm) for efficient gas transport. This segmentation allows each pore type to fulfill its specific function without compromising the other, resolving the contradiction between preventing electrolyte contact and maintaining gas transportability.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

Different regions of the catalyst structure are assigned different pore size characteristics: the inner regions contain fine pores to protect catalyst metals from electrolyte contact, while outer regions contain coarse pores to facilitate gas transport. This local differentiation of pore qualities allows simultaneous optimization of both catalyst activity protection and gas transport efficiency.

Inventive Principle:
Principle #3Local quality

2Quantity of substance

If catalyst metals are supported on conductive support with average particle diameter larger than average pore diameter, then catalyst particles are not allowed to enter fine pores and use efficiency of noble metal is improved, but electrolyte and catalyst metal particles come into contact and catalyst activity decreases

Engineering Contradiction:
Improvenoble metal utilization efficiencyVSAvoidcatalyst activity
Core Design Contradiction:
Quantity of substanceVSReliability

Solution Approach 1:

Coarse pores (1-10 nm) act as intermediary channels between the electrolyte and catalyst metals supported on fine pores. These intermediate pores allow gas transport and maintain the functional separation between electrolyte and catalyst, preventing direct contact while enabling necessary mass transport, thus preserving both noble metal efficiency and catalyst activity.

Inventive Principle:
Principle #24Intermediary (Mediator)

Solution Approach 2:

The catalyst employs a hierarchical porous structure with dual pore size distributions (fine pores: 0.3-1 nm and coarse pores: 1-10 nm). This porous material design allows selective access: fine pores protect catalyst metals from electrolyte, while coarse pores provide transport pathways, simultaneously achieving high noble metal utilization and sustained catalyst activity.

Inventive Principle:
Principle #31Porous materials

3Reliability

If catalyst metals are supported inside fine pores to prevent electrolyte contact, then catalyst activity is maintained, but gas transport resistance increases and performance deteriorates under high load conditions

Engineering Contradiction:
Improvecatalyst effectivenessVSAvoidpower generation performance
Core Design Contradiction:
ReliabilityVSProductivity

Solution Approach 1:

The pore system is segmented into fine pores (0.3-1 nm) for catalyst protection and coarse pores (1-10 nm) for high-speed gas transport. This segmentation enables the catalyst to maintain effectiveness through electrolyte exclusion while achieving high power generation performance through efficient gas supply via coarse pores, even under high load conditions.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The catalyst combines two pore structure types (fine and coarse pores) within a single composite structure. This composite porous architecture integrates the benefits of both pore sizes: fine pores provide catalyst protection and activity, while coarse pores provide low-resistance gas transport pathways, enabling high performance under varying load conditions.

Inventive Principle:
Principle #40Composite materials

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 catalyst design improves catalyst activity and power generation performance by reducing gas transport resistance and maintaining catalyst effectiveness, even under high load conditions, while potentially reducing the amount of expensive noble metals required.

Implementation Method 1

a transporting distance of a gas such as oxygen is increased

Methodology Applied
Scientific EffectDiffusion: Diffusion

Implementation Method 2

an electrode catalyst having catalyst metal particles supported on a conductive support

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 3

a polymer electrolyte fuel cell uses a proton conductive solid polymer membrane

Methodology Applied
Scientific EffectElectrochemical reaction:

Data Source

PatentUS11031604B2Catalyst and electrode catalyst layer, membrane electrode assembly, and fuel cell using the catalyst
Publication Date: 2021.06.08 NISSAN MOTOR CO LTD
  • US11031604B2 patent drawing
  • US11031604B2 patent drawing

AI summary

Provided is a catalyst having excellent gas transportability. Disclosed is a catalyst comprising a catalyst support and a catalyst metal supported on the catalyst support, wherein the catalyst includes pores having a radius of less than 1 nm and pores having a radius of 1 nm or more, wherein a pore volume of the pores having a radius of less than 1 nm is 0.3 cc/g support or more or a mode radius of a pore distribution of the pores having a radius of less than 1 nm is 0.3 nm or more and less than 1 nm, and wherein the catalyst metal is supported inside the pores having a radius of 1 nm or more.