Dynamic Catalytic Reactor Zoning for Variable Hydrogen Feed

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Solution Overview

Problem

Catalytic reactors for CO2 hydrogenation face challenges in utilizing renewable energy due to its fluctuating nature, requiring large-scale energy storage and high-cost hydrogen storage, leading to increased production costs and inefficiencies.

Innovation Solution

A dynamic catalytic conversion reactor that adjusts its operation based on fluctuating renewable energy sources, eliminating the need for energy storage by using a modular design with separate zones and a heat transfer medium to maintain consistent reactor temperature and hydrogen supply.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If steady-state operation mode is used for catalytic reactors, then consistent reaction performance is achieved, but large-scale energy storage is required to handle fluctuating renewable energy supply

Engineering Contradiction:
Improvereaction performance consistencyVSAvoidenergy storage system
Core Design Contradiction:
ReliabilityVSDevice complexity

Solution Approach 1:

The reactor system dynamically adjusts its operation mode between steady-state and transient regimes based on real-time hydrogen feed availability. The control system monitors hydrogen supply fluctuations and automatically transitions between operational modes, eliminating the need for large energy storage systems while maintaining reliable reaction performance.

Inventive Principle:
Principle #15Dynamics

Solution Approach 2:

The system changes operational parameters such as reaction temperature, pressure, and feed flow rates to adapt to varying hydrogen supply conditions. By adjusting these parameters dynamically, the reactor can maintain optimal performance across different operating conditions without requiring extensive energy storage infrastructure.

Inventive Principle:
Principle #35Parameter changes

2Productivity

If green hydrogen is produced from water electrolysis using renewable electricity, then sustainable chemicals and fuels can be produced, but high electricity costs and energy loss from DC to AC conversion occur

Engineering Contradiction:
Improvesustainable chemicals productionVSAvoidelectricity cost
Core Design Contradiction:
ProductivityVSUse of energy by moving object

Solution Approach 1:

The system maintains continuous operation by utilizing transient hydrogen feeds directly from water electrolysis without interruption. The reactor is designed to handle variable feed rates continuously, eliminating the need for hydrogen storage and avoiding energy losses associated with liquefaction or compression, thereby reducing overall energy costs.

Inventive Principle:
Principle #20Continuity of useful action

Solution Approach 2:

The reactor acts as an intermediary that receives variable hydrogen feeds from water electrolysis and converts them into stable chemical products. This intermediary function absorbs the variability in hydrogen supply and delivers consistent product output, eliminating the need for expensive hydrogen storage and energy-intensive processing steps.

Inventive Principle:
Principle #24Intermediary (Mediator)

3Adaptability or versatility

If transient renewable energy is used to drive water electrolysis, then direct utilization of variable power is achieved, but hydrogen storage becomes problematic due to its low density

Engineering Contradiction:
Improverenewable energy utilizationVSAvoidhydrogen storage capacity
Core Design Contradiction:
Adaptability or versatilityVSQuantity of substance

Solution Approach 1:

The system extracts and utilizes hydrogen directly from the water electrolysis process as it is produced, feeding it continuously into the reactor. By taking out hydrogen immediately upon production and avoiding storage, the system eliminates the problems associated with hydrogen's low density while fully utilizing transient renewable energy for chemical production.

Inventive Principle:
Principle #2Taking out (Extraction)

4Temperature

If conventional multitubular reactors are used for CO2 hydrogenation, then exothermic reaction heat is managed, but the reactor cannot quickly adapt to varying hydrogen feed rates

Engineering Contradiction:
Improvereaction temperature controlVSAvoidhydrogen feed rate adjustment
Core Design Contradiction:
TemperatureVSAdaptability or versatility

Solution Approach 1:

The reactor incorporates dynamic control mechanisms that allow rapid adjustment of operational parameters in response to varying hydrogen feed rates. The system can quickly transition between different operating modes while maintaining temperature control, enabling it to adapt to transient renewable energy supply fluctuations without compromising reaction temperature management.

Inventive Principle:
Principle #15Dynamics

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

Enables efficient utilization of renewable energy for CO2 conversion, reducing production costs and maintaining catalyst activity, with the ability to quickly adapt to varying hydrogen feed rates, thus producing sustainable chemicals and fuels competitively with fossil fuels.

Implementation Method 1

a heat transfer medium to maintain consistent reactor temperature

Methodology Applied
Scientific EffectHeat transfer: Conduction (thermal)

Implementation Method 2

catalytic conversion reactor... converts CO2 and hydrogen into a variety of chemicals and fuels

Methodology Applied
Scientific EffectCatalysis: Catalysis

Data Source

PatentUS12478938B2Dynamic catalytic conversion reactor and systems and methods using the same
Publication Date: 2025.11.25 AIR CO HLDG INC
  • US12478938B2 patent drawing
  • US12478938B2 patent drawing
  • US12478938B2 patent drawing

AI summary

A dynamic catalytic conversion reactor having a plurality of operating zones is disclosed that adjusts operation based on incoming hydrogen from a fluctuating renewable energy source. The dynamic reactor is configured to turn on and off supply of feed gas to certain zones based on hydrogen supply, and maintains catalyst activity within all operating and idle zones by applying one of a number of gas flow options through the idle zones. Methods and systems of using the dynamic reactor are also disclosed.