Stratified Methanation Reactor for CO2 Conversion

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Solution Overview

Problem

Existing technologies face challenges in achieving a cost-effective and simple process for converting carbon dioxide (CO2) and hydrogen into methane, particularly at various scales including modular systems to match distributed CO2 collection and hydrogen generation production sites.

Innovation Solution

A modular renewable fuel generation system that utilizes a stratified methanation reactor with interspersed inert sections, integrated with active cooling, to manage heat and improve conversion efficiency, allowing for scalable and portable methane production.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Device complexity

If a conventional methanation reactor is used for CO2 and hydrogen conversion, then the process can be simplified, but the peak temperatures become too high reducing catalyst performance and longevity

Engineering Contradiction:
Improveprocess simplicityVSAvoidpeak temperature
Core Design Contradiction:
Device complexityVSTemperature

Solution Approach 1:

The reactor bed is segmented into multiple zones with alternating catalyst and inert materials, creating distinct thermal zones that prevent temperature runaway while maintaining overall reaction efficiency

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

Inert sections are introduced as intermediary elements between catalyst sections to act as thermal barriers, absorbing excess heat and preventing direct thermal coupling that would lead to peak temperature problems

Inventive Principle:
Principle #24Intermediary (Mediator)

2Productivity

If the reactor operates at high temperature to improve reaction rate, then methane production efficiency increases, but catalyst longevity decreases

Engineering Contradiction:
Improvemethane production efficiencyVSAvoidcatalyst longevity
Core Design Contradiction:
ProductivityVSDuration of action of stationary object

Solution Approach 1:

By segmenting the reactor bed into alternating catalyst and inert zones, the system maintains lower peak temperatures that protect catalyst longevity while still achieving high overall productivity through the distributed reaction zones

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The system changes the temperature distribution parameters by introducing thermal barriers, transforming from a uniform high-temperature profile to a controlled multi-zone temperature profile that balances reaction rate and catalyst stability

Inventive Principle:
Principle #35Parameter changes

3Adaptability or versatility

If a modular system design is implemented to match distributed CO2 collection sites, then adaptability improves, but device complexity increases

Engineering Contradiction:
Improveadaptability to distributed sitesVSAvoidsystem complexity
Core Design Contradiction:
Adaptability or versatilityVSDevice complexity

Solution Approach 1:

The system is divided into modular reactor units that can be independently deployed at distributed CO2 collection sites, with each module containing its own catalyst and inert sections, enabling flexible adaptation to various locations while maintaining manageable complexity through standardization

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The modular reactor design serves multiple functions: it can be deployed at different scales, adapted to various CO2 sources, and configured for different production requirements, making a single design applicable across diverse distributed sites

Inventive Principle:
Principle #6Universality (Multi-functionality)

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 system effectively reduces peak temperatures, enhances catalyst performance and longevity, and improves methane production efficiency, making it suitable for a range of process scales from modular to industrial.

Implementation Method 1

integrated with active cooling, to manage heat and improve conversion efficiency

Methodology Applied
Scientific EffectHeat transfer: Conduction (thermal)

Implementation Method 2

The Sabatier reaction is a strongly exothermic process that catalytically converts CO2 with 4 moles of hydrogen to form methane and 2 moles of water

Methodology Applied
Scientific EffectExothermic reaction: Exothermic Reaction

Implementation Method 3

The Sabatier reaction is a strongly exothermic process that catalytically converts CO2 with 4 moles of hydrogen to form methane and 2 moles of water

Methodology Applied
Scientific EffectCatalysis: Catalysis

Data Source

PatentUS12325674B1Modular system for renewable fuel generation
Publication Date: 2025.06.10 GENERAL GALACTIC TECHNOLOGIES CORP
  • US12325674B1 patent drawing
  • US12325674B1 patent drawing
  • US12325674B1 patent drawing

AI summary

A modular system is configured to generate renewable fuel. The system includes a modular container that has inlets/outlets and houses a treatment subsystem configured to produce treated water and an electrolysis subsystem configured to perform electrolysis of the treated water to produce hydrogen and oxygen. The modular container further includes a reactor configured to perform an exothermic reaction in as little as a single pass using the hydrogen and carbon dioxide to produce the renewable fuel. The modular container can further include a post-processing subsystem configured to perform further processing of the renewable fuel.