Anode Catalyst Aggregations for PEM Electrolyzer Efficiency

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Solution Overview

Problem

Current proton exchange membrane (PEM) electrolyzers face high costs and inefficiencies due to high anode over-potential caused by poor oxygen evolution reaction kinetics, primarily attributed to the use of large iridium oxide particles without supports, which lead to carbon corrosion at high voltages.

Innovation Solution

A novel anode catalyst comprising a support with catalyst particles arranged in aggregations, where each particle is in physical contact with others, using metal oxides or doped metal oxides as supports and iridium or platinum-based catalyst particles, deposited via electroless plating, to form a stable and efficient catalyst layer.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Quantity of substance

If conventional carbon supports are used to increase electrochemical surface area, then the amount of catalyst required is reduced, but fast electrochemical oxidation occurs at high voltages leading to significant carbon loss

Engineering Contradiction:
Improveamount of catalystVSAvoidcatalyst stability
Core Design Contradiction:
Quantity of substanceVSReliability

Solution Approach 1:

The patent changes the material parameter of the support from conventional carbon to metal oxide, which has different electrochemical stability characteristics that prevent oxidation at operating voltages while maintaining high surface area properties

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent creates a composite catalyst system combining metal oxide support with catalyst particles, where the metal oxide provides both structural support and electrochemical stability, eliminating the harmful oxidation reactions that occur with carbon supports

Inventive Principle:
Principle #40Composite materials

2Ease of manufacture

If large particle sizes (20-100 nm) are used for IrO2 catalyst, then the catalyst is easier to manufacture, but the anode over-potential remains high due to poor oxygen evolution reaction kinetics

Engineering Contradiction:
Improvecatalyst fabricationVSAvoidoxygen evolution reaction rate
Core Design Contradiction:
Ease of manufactureVSProductivity

Solution Approach 1:

The patent utilizes porous metal oxide support structures that provide high surface area for catalyst dispersion, enabling increased catalyst activity without requiring smaller particle sizes or more complex fabrication processes

Inventive Principle:
Principle #31Porous materials

Solution Approach 2:

The patent transitions from considering only particle size as the variable for improving kinetics to utilizing the dimensional advantage of porous support structures, which provide additional surface area in three-dimensional space

Inventive Principle:
Principle #17Another dimension (Dimensionality change)

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 novel anode catalyst reduces overpotential and enhances the electrochemical surface area, improving the efficiency and longevity of PEM electrolyzers by stabilizing the catalyst layer and reducing carbon corrosion.

Implementation Method 1

deposited via electroless plating, to form a stable and efficient catalyst layer

Methodology Applied
Scientific EffectElectroless plating: Electroplating

Implementation Method 2

Standard water electrolysis generates hydrogen and oxygen gases by applying a direct current in order to dissociate the water reactant

Methodology Applied
Scientific EffectElectrolysis: Electrolysis

Data Source

PatentUS11124885B2Anode catalyst suitable for use in an electrolyzer
Publication Date: 2021.09.21 PLUG POWER
  • US11124885B2 patent drawing
  • US11124885B2 patent drawing
  • US11124885B2 patent drawing

AI summary

An anode catalyst suitable for use in an electrolyzer. The anode catalyst includes a support and a plurality of catalyst particles disposed on the support. The support may include a plurality of metal oxide or doped metal oxide particles. The catalyst particles, which may be iridium, iridium oxide, ruthenium, ruthenium oxide, platinum, and/or platinum black particles, may be arranged to form one or more aggregations of catalyst particles on the support. Each of the aggregations of catalyst particles may include at least 10 particles, wherein each of the at least 10 particles is in physical contact with at least one other particle. The support particles and their associated catalyst particles may be dispersed in a binder.