Fuel Cell Catalyst Sulfate Poisoning via Potential Control

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Solution Overview

Problem

Conventional core-shell catalysts are prone to poisoning by sulfate ions due to the lack of potential control during the platinum substitution step after Cu-UPD, leading to a decrease in oxygen reduction activity and practical power generation performance in fuel cells.

Innovation Solution

A method involving a copper covering step followed by a platinum covering step, where a constant potential is applied between the oxidation reduction potential of copper and platinum to prevent copper desorption and ensure uniform platinum deposition, resulting in a less defective platinum-containing outermost layer that reduces sulfate ion adsorption.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Ease of manufacture

If potential treatment is not carried out during platinum substitution, then the process is simpler and faster, but the catalyst becomes prone to poisoning by sulfate ions

Engineering Contradiction:
Improveprocess simplicityVSAvoidcatalyst resistance to sulfate ion poisoning
Core Design Contradiction:
Ease of manufactureVSReliability

Solution Approach 1:

The patent applies a constant potential in the range of 0.37 to 0.70 V (vs. RHE) during the platinum substitution step. This parameter control prevents copper oxidation and maintains a stable electrochemical environment, allowing platinum to uniformly replace copper atoms without forming defects that would attract sulfate ions. The controlled potential ensures the catalyst maintains high resistance to sulfate ion poisoning.

Inventive Principle:
Principle #35Parameter changes

2Object-affected harmful factors

If potential is applied during platinum substitution, then sulfate ion adsorption is reduced, but the manufacturing process becomes more complex

Engineering Contradiction:
Improvesulfate ion adsorptionVSAvoidprocess complexity
Core Design Contradiction:
Object-affected harmful factorsVSDevice complexity

Solution Approach 1:

The patent implements a constant potential application (0.37-0.70 V vs. RHE) during platinum substitution. This single parameter control achieves dual benefits: it prevents copper oxidation that would create defects, and it ensures uniform platinum deposition. The result is a catalyst surface with minimal defect sites for sulfate ion adsorption, achieved through a relatively simple controlled potential approach rather than multiple complex process steps.

Inventive Principle:
Principle #35Parameter changes

3Productivity

If copper is allowed to oxidize naturally, then the platinum substitution process is faster, but the outermost layer becomes defective and exposes palladium core

Engineering Contradiction:
Improveplatinum substitution speedVSAvoidoutermost layer completeness
Core Design Contradiction:
ProductivityVSManufacturing precision

Solution Approach 1:

The patent maintains a constant potential of 0.37-0.70 V (vs. RHE) during platinum substitution, which is below the oxidation potential of copper. This prevents copper oxidation while allowing platinum to gradually replace copper atoms through controlled substitution. The slow, controlled process ensures complete and uniform platinum coverage without creating defects or exposing the palladium core, achieving both high productivity and manufacturing precision.

Inventive Principle:
Principle #35Parameter changes

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 method effectively inhibits sulfate ion adsorption and maintains catalytic activity, enhancing the stability and performance of fine catalyst particles in fuel cell environments by forming a non-defective platinum-containing outermost layer.

Implementation Method 1

covering at least part of the fine palladium-containing particle with copper by preparing a second dispersion by mixing a first dispersion comprising fine palladium-containing particles being dispersed in an acid solution with a copper-containing solution, and applying a potential that is nobler than the oxidation reduction potential of copper to the fine palladium-containing particles in the second dispersion

Methodology Applied
Scientific EffectElectrodeposition: Electrodeposition

Implementation Method 2

covering at least part of the fine palladium-containing particle with platinum by substituting the copper covering at least part of the fine palladium-containing particle with platinum by mixing the second dispersion and a platinum-containing solution after the copper covering step, with applying a constant potential that is in a range between a potential that is nobler than the oxidation reduction potential of copper and a potential that is less than the oxidation reduction potential of platinum

Methodology Applied
Scientific EffectElectrochemical substitution: Electrodeposition

Data Source

PatentUS9950314B2Method for producing fine catalyst particles and method for producing carbon-supported catalyst
Publication Date: 2018.04.24 TOYOTA JIDOSHA KK
  • US9950314B2 patent drawing
  • US9950314B2 patent drawing
  • US9950314B2 patent drawing

AI summary

The present invention is to provide fine catalyst particles to which sulfate ions are less likely to be adsorbed, and a carbon-supported catalyst to which sulfate ions are less likely to be adsorbed. Disclosed is a method for producing fine catalyst particles comprising a fine palladium-containing particle and a platinum-containing outermost layer covering at least part of the fine palladium-containing particle, wherein the method comprises: a copper covering step of covering at least part of the fine palladium-containing particle with copper by preparing a second dispersion by mixing a first dispersion comprising fine palladium-containing particles being dispersed in an acid solution with a copper-containing solution, and applying a potential that is nobler than the oxidation reduction potential of copper to the fine palladium-containing particles in the second dispersion, and a platinum covering step of covering at least part of the fine palladium-containing particle with platinum by substituting the copper covering at least part of the fine palladium-containing particle with platinum by mixing the second dispersion and a platinum-containing solution after the copper covering step, with applying a constant potential that is in a range between a potential that is nobler than the oxidation reduction potential of copper and a potential that is less than the oxidation reduction potential of platinum, to the fine palladium-containing particles.