SOFC Cathode Oxygen-Reducing Layer Enhances Efficiency

Resolve Bottlenecks,
Find Innovative Solutions
Generate Solutions

Solution Overview

Problem

The cathode in solid oxide fuel cells (SOFCs) is a limiting factor for energy conversion efficiency and stability due to slow oxygen reduction reactions, which is exacerbated by the sluggish kinetics of oxygen reduction at the cathode surface.

Innovation Solution

A mixed ionic-electronic conductor (MIEC) cathode with a thin oxygen-reducing layer of single element oxides or carbonates, less than 30 nm thick, is used to enhance oxygen reduction reactions by creating a dielectric/insulating surface that increases electron emission and oxygen ion diffusion.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If a conventional porous cathode material is used, then the cathode structure is simple and easy to manufacture, but the oxygen reduction reaction kinetics are sluggish, limiting energy conversion efficiency

Engineering Contradiction:
Improveenergy conversion efficiencyVSAvoidcathode structure complexity
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The cathode is constructed as a composite material system combining a porous MIEC substrate with a thin non-porous oxide layer coating. The MIEC provides bulk ionic and electronic conductivity, while the thin oxide layer surface enhances oxygen reduction reaction kinetics. This composite structure resolves the contradiction by integrating materials with complementary properties to achieve high efficiency without excessive complexity.

Inventive Principle:
Principle #40Composite materials

Solution Approach 2:

The thin oxide layer is applied specifically at the cathode surface where oxygen reduction reactions occur, providing localized enhancement of reaction kinetics. The bulk MIEC material maintains its porous structure for ion transport, while the surface layer provides catalytic activity. This local quality modification addresses the contradiction by optimizing only the critical reaction zone rather than redesigning the entire cathode structure.

Inventive Principle:
Principle #3Local quality

2Power

If the cathode operates at high current rates, then power output increases, but oxygen reduction reaction kinetics become the limiting factor, reducing overall performance

Engineering Contradiction:
Improvepower outputVSAvoidreaction kinetics stability
Core Design Contradiction:
PowerVSReliability

Solution Approach 1:

The thin oxide layer modifies the surface chemical and electronic parameters of the cathode, creating a surface with enhanced oxygen adsorption and reduction properties. This parameter change at the surface level enables sustained high current operation by improving the rate-determining oxygen reduction step, thereby maintaining reliability at high power output levels.

Inventive Principle:
Principle #35Parameter changes

3Productivity

If a thin oxide layer is applied to the MIEC cathode, then oxygen reduction reactions are accelerated, but the manufacturing precision requirements increase due to the thin layer thickness control

Engineering Contradiction:
Improveoxygen reduction reaction rateVSAvoidlayer thickness control
Core Design Contradiction:
ProductivityVSManufacturing precision

Solution Approach 1:

The thin oxide layer is designed to be sufficiently thin (much less than 10 nm) that imperfections or variations in thickness do not significantly impact overall cathode performance. The layer acts as a surface modifier rather than a structural component, allowing greater manufacturing tolerance. This approach resolves the contradiction by making the layer thickness less critical to function, effectively reducing manufacturing precision requirements.

Inventive Principle:
Principle #27Cheap short-living objects (Disposable)

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

This configuration significantly accelerates oxygen reduction reactions, leading to higher current rates and efficiencies by increasing the availability of oxygen ions and improving the stability of the cathode, thereby enhancing the overall performance of the SOFC.

Implementation Method 1

establishing a dielectric/insulator surface between the MIEC and the electrocatalytic material, which significantly increases electron emissions

Methodology Applied
Scientific EffectField emission: Thermionic Emission

Implementation Method 2

increases the diffusion of oxygen ions through the MIEC and electrolyte

Methodology Applied
Scientific EffectDiffusion: Diffusion

Implementation Method 3

a mixed ionic-electronic conductor (MIEC) with a thin coating of an electrocatalytic material

Methodology Applied
Scientific EffectIonic conduction: Conduction (electrical)

Implementation Method 4

MIEC having a minimum electrical conductivity of 100 S/m at 800° C., and having a minimum ionic conductivity of 0.1 S/m at 800° C.

Methodology Applied
Scientific EffectElectronic conduction: Conduction (electrical)

Implementation Method 5

oxygen reduction takes place, and the ability to generate electricity in fuel cells at high current rates and efficiencies is generally limited by the cathode

Methodology Applied
Scientific EffectElectrochemical reduction: Reduction

Data Source

PatentUS9935318B1Solid oxide fuel cell cathode with oxygen-reducing layer
Publication Date: 2018.04.03 THE UNITED STATES AS REPRESENTED BY THE DEPARTMENT OF ENERGY
  • US9935318B1 patent drawing
  • US9935318B1 patent drawing
  • US9935318B1 patent drawing

AI summary

The disclosure provides a SOFC comprised of an electrolyte, anode, and cathode, where the cathode comprises an MIEC and an oxygen-reducing layer. The oxygen-reducing layer is in contact with the MIEC, and the MIEC is generally between and separating the oxygen-reducing layer and the electrolyte. The oxygen-reducing layer is comprised of single element oxides, single element carbonates, or mixtures thereof, and has a thickness of less than about 30 nm. In a particular embodiment, the thickness is less than 5 nm. In another embodiment, the thickness is about 3 monolayers or less. The oxygen-reducing layer may be a continuous film or a discontinuous film with various coverage ratios. The oxygen-reducing layer at the thicknesses described may be generated on the MIEC surface using means known in the art such as, for example, ALD processes.