Iridium Oxide OER Catalyst for Reduction-Stable Fuel Cells

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Solution Overview

Problem

Existing oxygen evolution reaction (OER) catalysts like IrO2 and RuO2 suffer from instability under fuel cell conditions, leading to dissolution and contamination, reducing the power density and catalytic activity due to reduction by hydrogen, especially during startup/shutdown cycles and fuel starvation.

Innovation Solution

An OER catalyst comprising iridium oxide with a weight loss of less than 1% by weight and a BET specific surface area of more than 15 m2/g is produced through a process involving high-temperature treatment, grinding, and subsequent moderate heat treatment, ensuring high stability and catalytic activity.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If IrO2 and RuO2 are used as OER catalysts to prevent carbon oxidation during fuel starvation, then carbon corrosion is avoided, but the catalyst is reduced to metallic form and dissolves, leading to ionic contamination and reduced power density

Engineering Contradiction:
Improvestability against carbon oxidationVSAvoidcatalyst dissolution
Core Design Contradiction:
ReliabilityVSLoss of substance

Solution Approach 1:

The patent applies parameter changes by heat-treating the iridium oxide catalyst at elevated temperatures (500-1000°C) to modify its crystal structure and surface properties. This thermal treatment stabilizes the oxide phase and reduces its tendency to reduce to metallic form under fuel cell operating conditions, thereby preventing catalyst dissolution while maintaining OER activity

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent employs composite material strategies by combining iridium oxide with support materials such as titanium dioxide (TiO2) or carbon. These composites provide structural stability, prevent agglomeration, and enhance the overall resistance to reduction and dissolution of the iridium oxide component during operation

Inventive Principle:
Principle #40Composite materials

2Reliability

If IrO2 and RuO2 are used as OER catalysts to prevent carbon oxidation, then carbon corrosion is avoided, but catalytic activity decreases due to reduction and dissolution

Engineering Contradiction:
Improveprotection against carbon corrosionVSAvoidpower density
Core Design Contradiction:
ReliabilityVSProductivity

Solution Approach 1:

Heat treatment at optimized temperatures modifies the crystal structure and surface chemistry of iridium oxide, enhancing its stability against reduction while preserving its oxygen evolution reaction activity. This ensures high power density is maintained even during startup/shutdown and fuel starvation conditions

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent extracts and eliminates the problematic reduction-dissolution pathway by stabilizing the iridium oxide through thermal treatment and composite formation, thereby preventing the transformation from active oxide phase to inactive metallic phase that would otherwise reduce power density

Inventive Principle:
Principle #2Taking out (Extraction)

3Reliability

If thermal treatment at high temperatures is applied to stabilize IrO2, then reduction stability improves, but particle agglomeration occurs, reducing catalytic activity

Engineering Contradiction:
Improvereduction stabilityVSAvoidcatalytic activity
Core Design Contradiction:
ReliabilityVSProductivity

Solution Approach 1:

The patent uses composite materials where iridium oxide is supported on high-surface-area materials like TiO2 or porous carbon. These supports physically separate iridium oxide particles, preventing agglomeration during heat treatment while maintaining high dispersion and catalytic activity. The support also provides thermal stability and prevents sintering

Inventive Principle:
Principle #40Composite materials

Solution Approach 2:

The patent employs porous support materials with controlled pore sizes and high surface areas. These porous structures accommodate iridium oxide particles, prevent their agglomeration during thermal treatment, and maintain high surface area-to-volume ratios that are critical for catalytic activity while allowing heat treatment to proceed at stabilizing temperatures

Inventive Principle:
Principle #31Porous 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 maintains high OER activity and prevents carbon corrosion during cell reversal, retaining enduring power density and stability under fuel starvation and startup/shutdown conditions.

Implementation Method 1

the reduction of these noble metal oxides by hydrogen can occur spontaneously at the operating temperature of the fuel cell

Methodology Applied
Scientific EffectReduction: Reduction

Implementation Method 2

Simon Geiger et al.: 'Activity and Stability of Electrochemically and Thermally Treated Iridium for the Oxygen Evolution Reaction,' Journal of The Electrochemical Society, 163 (11), F3132-F3138 (2016) discloses thermal treatments, for example, sintering

Methodology Applied
Scientific EffectThermal treatment: Heat Treatment

Implementation Method 3

sintering at high temperatures leads to agglomeration of iridium particles

Methodology Applied
Scientific EffectSintering: Sintering

Implementation Method 4

the activity of the catalyst is proportional to the specific surface area thereof

Methodology Applied
Scientific EffectCatalysis: Catalysis

Data Source

PatentUS12609326B2Oxygen evolution catalyst, production and use of same, membrane electrode arrangement and fuel cell or electrolytic cell
Publication Date: 2026.04.21 GREENERITY GMBH
  • US12609326B2 patent drawing
  • US12609326B2 patent drawing
  • US12609326B2 patent drawing

AI summary

An oxygen evolution reaction catalyst includes iridium oxide that exhibits a weight loss of less than 1% by weight upon exposure of the oxygen evolution reaction catalyst to a 3.3 vol % hydrogen stream in argon at a temperature of 80° C. for 12 hours and has a BET specific surface area of more than 15 m2/g.