Methane Production Membrane Electrode Assembly with Localized Catalyst Loading

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Solution Overview

Problem

Current carbon oxide reduction technologies face challenges in achieving high selectivity and efficiency for methane production due to limitations in catalyst loading, membrane thickness, and salt ion concentration, which affect the performance and stability of membrane electrode assemblies (MEAs) in carbon oxide reduction reactors.

Innovation Solution

The development of a membrane electrode assembly (MEA) with a cathode catalyst layer having a low catalyst loading, a bipolar structure with thin cation and anion conducting polymer layers, and optimized salt ion concentrations to enhance methane selectivity and stability, utilizing copper catalysts and specific polymer electrolyte membranes to promote carbon oxide reduction to hydrocarbons, alcohols, and carboxylic acids.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If high catalyst loading is used in the cathode layer, then methane production rate increases, but selectivity and current efficiency decrease

Engineering Contradiction:
Improvemethane production rateVSAvoidmethane selectivity
Core Design Contradiction:
ProductivityVSReliability

Solution Approach 1:

The patent applies local quality by creating distinct functional zones within the cathode catalyst layer with varying catalyst loadings. The layer includes a first region with lower catalyst loading (0.1-1.0 mg/cm²) that promotes high selectivity for methane, and a second region with higher catalyst loading (1.0-5.0 mg/cm²) that enhances overall production rate. This spatial variation in catalyst distribution allows simultaneous optimization of both selectivity and productivity.

Inventive Principle:
Principle #3Local quality

2Strength

If thick polymer electrolyte membrane is used, then mechanical stability improves, but ionic resistance increases and cell voltage rises

Engineering Contradiction:
Improvemembrane mechanical stabilityVSAvoidcell voltage
Core Design Contradiction:
StrengthVSUse of energy by moving object

Solution Approach 1:

The patent employs composite materials by combining the polymer electrolyte membrane with catalyst layers and support structures to create a composite membrane electrode assembly. The membrane has controlled thickness (15-50 micrometers) and is integrated with catalyst layers containing metal particles (0.1-5.0 mg/cm² loading). This composite structure provides both mechanical stability and optimized ionic conductivity, reducing cell voltage while maintaining structural integrity.

Inventive Principle:
Principle #40Composite materials

3Productivity

If low salt ion concentration is used, then Faradaic yield increases, but system stability decreases

Engineering Contradiction:
ImproveFaradaic yieldVSAvoidsystem stability
Core Design Contradiction:
ProductivityVSStability of the object's composition

Solution Approach 1:

The patent applies parameter changes by optimizing the salt concentration in the electrolyte solution to a specific range (10-100 mM) that balances Faradaic yield and system stability. This controlled parameter adjustment, combined with optimized catalyst loading and membrane thickness, creates a stable operating condition that maintains high methane selectivity while ensuring system robustness during continuous operation.

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

This configuration improves methane production selectivity and stability by optimizing catalyst loading, membrane thickness, and salt ion concentrations, leading to higher Faradaic yield and current efficiency, and maintaining low cell voltage, thereby enhancing the overall performance of carbon oxide reduction reactors.

Implementation Method 1

a polymer electrolyte membrane (PEM) that provides ionic communication between the cathode layer and the anode layer

Methodology Applied
Scientific EffectIon conduction: Conduction (electrical)

Implementation Method 2

a cathode catalyst layer including a carbon oxide reduction catalyst that selectively promotes production of a product selected from a hydrocarbon, a carboxylic acid, or an alcohol

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 3

an anode catalyst layer including a catalyst that promotes oxidation of water

Methodology Applied
Scientific EffectOxidation: Oxidation

Implementation Method 4

systems and methods for electrolytic carbon oxide reactor operation for production of methane and other hydrocarbons

Methodology Applied
Scientific EffectElectrolysis: Electrolysis

Data Source

PatentUS12116683B2System and method for methane production
Publication Date: 2024.10.15 TWELVE BENEFIT CORP
  • US12116683B2 patent drawing
  • US12116683B2 patent drawing
  • US12116683B2 patent drawing

AI summary

Provided herein are systems and methods for operating carbon oxide (COx) reduction reactors (CRRs) for producing methane (CH4). Embodiments of the systems and methods may also be used for producing other organic compounds including alcohols, carboxylic acids, and other hydrocarbons such as ethylene (CH2CH2). According to various embodiments, the systems and methods may be characterized by one or more of the following features. In some embodiments, a membrane electrode assembly (MEA) includes a cathode catalyst layer with a relatively low catalyst loading. In some embodiments, a bipolar MEA includes a thin cation-conducting layer and a thin anion-conducting layer, with the cation-conducting layer being thicker than the anion-conducting layer. In other embodiments a pure anion exchange polymer only membrane may be used to bridge the cathode catalyst and the anode catalyst. These and other features are described further below.