Intermediate-Temperature SOFC Anode and Cathode Design

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Solution Overview

Problem

Solid oxide fuel cells (SOFCs) face challenges in operating at intermediate temperatures (200°C to 500°C) due to decreased performance of anode, electrolyte, and cathode components, particularly when fueled by hydrocarbons, leading to issues like carbon deposition and increased resistance to ionic transport.

Innovation Solution

The development of an optimized anode with a doped ceria catalyst for methane reforming, a synergistic electrolyte with increased ionic conductivity, and a high-performance transition metal oxide catalyst in a hollow nanofiber architecture for the cathode, enhancing catalytic activity and stability at lower temperatures.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Ease of manufacture

If the operating temperature of SOFCs is reduced to intermediate temperatures (200°C to 500°C), then system cost and durability are improved, but component performance deteriorates

Engineering Contradiction:
Improvesystem costVSAvoidcomponent performance
Core Design Contradiction:
Ease of manufactureVSProductivity

Solution Approach 1:

The patent changes the material parameters of the anode, electrolyte, and cathode to enable efficient operation at intermediate temperatures. Specifically, it uses a nickel-ceria anode instead of conventional nickel-YSZ, a gadolinium-doped ceria (GDC) electrolyte instead of YSZ, and a perovskite cathode material, which collectively maintain high ionic conductivity and electrochemical performance at 200-500°C range

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent employs composite material structures throughout the fuel cell components. The anode uses a composite of nickel and ceria oxides, the electrolyte uses gadolinium-doped ceria composite, and the cathode uses perovskite-based composite materials. These composite structures provide enhanced ionic conductivity, catalytic activity, and electrochemical performance at intermediate operating temperatures

Inventive Principle:
Principle #40Composite materials

2Loss of energy

If hydrocarbon fuel is directly utilized in SOFCs, then fuel efficiency is improved, but carbon deposition occurs on the anode

Engineering Contradiction:
Improvefuel efficiencyVSAvoidcarbon deposition
Core Design Contradiction:
Loss of energyVSObject-generated harmful factors

Solution Approach 1:

The patent converts the harmful carbon deposition effect into a beneficial process by utilizing the ceria component in the anode to catalyze dry reforming reactions. The carbon that would otherwise deposit and deactivate the anode is instead converted into useful syngas (CO and H2) through reforming with CO2, turning a harmful byproduct into a valuable fuel component

Inventive Principle:
Principle #22Blessing in disguise (Convert harm into benefit)

Solution Approach 2:

The ceria oxide in the anode acts as an intermediary substance that facilitates the conversion of hydrocarbon fuel and CO2 into syngas. It provides oxygen for oxidation reactions and catalyzes the reforming processes, enabling direct hydrocarbon utilization while preventing carbon buildup through controlled chemical reactions

Inventive Principle:
Principle #24Intermediary (Mediator)

3Object-generated harmful factors

If reforming reactions are promoted in the anode to reduce carbon deposition, then carbon deposition is reduced, but reforming reactions are not favored at intermediate temperatures

Engineering Contradiction:
Improvecarbon depositionVSAvoidreforming reaction favorability
Core Design Contradiction:
Object-generated harmful factorsVSTemperature

Solution Approach 1:

The patent changes the chemical and catalytic parameters of the anode material to enable reforming reactions at intermediate temperatures. The nickel-ceria composite anode has enhanced catalytic activity compared to conventional anodes, allowing reforming reactions to proceed efficiently at 200-500°C rather than requiring high temperatures

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 solution enables SOFCs to maintain performance with a peak power density of 0.368 W/cm² and durability of 200 hours at 500°C, utilizing hydrocarbon fuels efficiently without deactivation, and reduces system complexity and cost.

Implementation Method 1

an optimized doped ceria catalyst has been developed that is active for wet and dry reforming of methane below approximately 500°C

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 2

the electrolyte develops increased resistance to ionic transport

Methodology Applied
Scientific EffectIonic conduction: Conduction (electrical)

Implementation Method 3

a high performance transition metal oxide catalyst was produced using a scalable electrospinning fiber technique. The dual ionic and electronic conductivity of the material, combined with the high surface area of a hollow nanofiber architecture, allows for increased catalytic activity toward the oxygen reduction reaction

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 4

solid oxide fuel cells (SOFCs) are the cleanest, most efficient chemical-to-electrical energy conversion systems

Methodology Applied
Scientific EffectElectrochemical conversion: Fuel Cell

Data Source

PatentEP3488482B1Intermediate-temperature fuel cell tailored for efficient utilization of methane
Publication Date: 2021.05.05 GEORGIA TECH RES CORP
  • EP3488482B1 patent drawingFigure 1
  • EP3488482B1 patent drawingFigure 2
  • EP3488482B1 patent drawingFigure 3(a1)~3(b3)

AI summary

A solid oxide fuel cell capable of directly utilizing hydrocarbons as a fuel source at operating temperatures between 200°C and 500°C. The anode, electrolyte, and cathode of the solid oxide fuel cell can include technologies for improved operation at temperatures between 200°C and 500°C. The anode can include technologies for improved direct utilization of hydrocarbon fuel sources.