Ammonia Synthesis System with Microwave Reactive Catalyst Beds

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Solution Overview

Problem

Conventional ammonia synthesis systems face inefficiencies due to fluctuating hydrogen flow rates from renewable energy sources, non-uniform flow rate distribution, and temperature deviations within catalyst beds, leading to reduced yield and increased energy consumption.

Innovation Solution

An ammonia synthesis system utilizing a catalyst bed with a microwave reactive catalyst mixture, including a catalyst and carbon body, and a distribution system with backflow prevention and microwave heating, which maintains uniform flow distribution and temperature uniformity across the catalyst bed.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If conventional ammonia synthesis systems use hydrogen from renewable energy sources, then environmental sustainability is improved, but flow rate fluctuations reduce synthesis efficiency

Engineering Contradiction:
Improveammonia synthesis efficiencyVSAvoidhydrogen flow rate stability
Core Design Contradiction:
ProductivityVSStability of the object's composition

Solution Approach 1:

The system performs preliminary actions by using multiple catalyst beds in sequence and implementing pre-heating zones to prepare the reaction conditions before the actual synthesis occurs. This allows the system to handle flow rate variations more effectively by having buffer zones and preparatory stages that stabilize the reaction process.

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The system implements dynamic control through multiple catalyst beds that can operate at different stages, allowing the synthesis process to adapt to changing flow rates. The distributed catalyst beds enable the system to dynamically adjust reaction conditions across different zones to maintain efficiency despite hydrogen flow fluctuations.

Inventive Principle:
Principle #15Dynamics

2Loss of energy

If hydrogen flow rate is decreased to match renewable energy availability, then energy waste is reduced, but non-uniform flow rate distribution before catalyst bed increases

Engineering Contradiction:
Improveenergy wasteVSAvoidflow rate distribution uniformity
Core Design Contradiction:
Loss of energyVSManufacturing precision

Solution Approach 1:

The system segments the catalyst bed into multiple distributed beds along the reactor length. This segmentation allows the flow to be distributed more uniformly across different reaction zones, preventing the non-uniform distribution that occurs with single-bed configurations when flow rates are reduced.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The system introduces intermediary elements such as distribution plates and flow control structures between the hydrogen source and catalyst beds. These intermediaries help regulate and evenly distribute the hydrogen flow across multiple catalyst beds, maintaining uniformity even at reduced flow rates.

Inventive Principle:
Principle #24Intermediary (Mediator)

3Use of energy by moving object

If catalyst bed operation begins without preheating, then energy consumption is reduced, but temperature deviation between central and outer parts reduces ammonia synthesis yield

Engineering Contradiction:
Improveenergy consumptionVSAvoidammonia synthesis yield
Core Design Contradiction:
Use of energy by moving objectVSProductivity

Solution Approach 1:

The system implements preliminary preheating zones before the main catalyst beds, using waste heat from product streams or external sources to bring the reactants and catalyst to optimal temperature. This preliminary action ensures uniform temperature distribution across the catalyst bed before synthesis begins, eliminating the need for continuous high energy input during operation.

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The system utilizes thermal expansion principles by designing the catalyst bed structure and flow distribution to naturally promote uniform heat distribution. The multi-bed configuration allows thermal gradients to equalize across beds, reducing temperature deviations between central and outer parts without requiring excessive energy input.

Inventive Principle:
Principle #37Thermal expansion

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 enhances ammonia synthesis yield by stabilizing flow rates, reducing temperature deviations, and optimizing energy use, thereby improving overall efficiency and extending catalyst replacement cycles.

Implementation Method 1

a microwave heating device for emitting microwaves to each of the two or more catalyst beds

Methodology Applied
Scientific EffectMicrowave heating: Microwave Radiation

Implementation Method 2

the catalyst bed contains a microwave reactive catalyst mixture including a catalyst and a carbon body

Methodology Applied
Scientific EffectDielectric heating: Dielectric Heating

Data Source

PatentUS20250206628A1Ammonia synthesis system including catalyst bed containing microwave reactive catalyst mixture
Publication Date: 2025.06.26 SK INNOVATION CO LTD
  • US20250206628A1 patent drawing
  • US20250206628A1 patent drawing
  • US20250206628A1 patent drawing

AI summary

Provided is an ammonia synthesis system including an ammonia synthesis reactor; two or more catalyst beds included in the ammonia synthesis reactor; a backflow prevention plate disposed downstream from each of the catalyst beds except for the catalyst bed disposed at the lowest of the two or more catalyst beds for preventing a backflow of mixed gas; a distribution device disposed upstream from each of the two or more catalyst beds for distributing the mixed gas to the catalyst bed; mixed gas supply lines arranged to supply the mixed gas to each distribution device; and a microwave heating device for emitting microwaves to each of the two or more catalyst beds, wherein the catalyst bed contains a microwave reactive catalyst mixture including a catalyst and a carbon body.