Ammonia Cracking Reactor Heat Integration

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Solution Overview

Problem

Ammonia is not effectively used as a fuel due to its low flame speed, narrow ignition limits, and high ignition energy, but it has potential as a carbon dioxide-free fuel source with sufficient energy density and cost-effective storage, especially with renewable energy production becoming more viable.

Innovation Solution

A process that converts ammonia into a gas mixture of 75% hydrogen and 25% nitrogen by splitting it at high temperatures using a cracking catalyst, with energy supplied by burning some of the produced hydrogen, optimizing heat transfer and energy recovery in a double-tube reactor design.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Object-affected harmful factors

If ammonia is used directly as fuel, then carbon dioxide-free combustion and cost-effective storage are achieved, but flame speed is very low and ignition limits are narrow

Engineering Contradiction:
Improvecarbon dioxide emissionsVSAvoidflame speed
Core Design Contradiction:
Object-affected harmful factorsVSSpeed

Solution Approach 1:

The invention changes the chemical composition parameter of the fuel by converting ammonia into a hydrogen-nitrogen mixture (75% H2, 25% N2). This parameter change transforms the fuel properties: hydrogen provides high flame speed and wide ignition limits while maintaining carbon dioxide-free combustion, thus resolving the contradiction between low flame speed and zero emissions.

Inventive Principle:
Principle #35Parameter changes

2Productivity

If ammonia is cracked at high temperatures above 600°C, then conversion to hydrogen and nitrogen is efficient, but large amounts of energy are required to maintain the reaction

Engineering Contradiction:
Improveammonia conversion efficiencyVSAvoidenergy input for cracking
Core Design Contradiction:
ProductivityVSUse of energy by moving object

Solution Approach 1:

The invention merges the ammonia cracking reaction with the hydrogen combustion reaction in a single integrated reactor system. The heat released from burning a portion of the produced hydrogen is directly used to maintain the high temperature required for ammonia cracking, creating a self-sustaining thermal process that minimizes external energy input while maintaining high conversion efficiency.

Inventive Principle:
Principle #5Merging (Combining)

Solution Approach 2:

The system uses a portion of its own output (hydrogen) to fuel the cracking process. By combusting part of the produced hydrogen to generate the necessary heat, the system becomes self-sufficient thermally, eliminating the need for continuous external energy supply and resolving the contradiction between high productivity and high energy consumption.

Inventive Principle:
Principle #25Self-service

3Loss of energy

If a double-tube reactor design is used with hydrogen combustion in the inner tube, then heat transfer efficiency is improved, but device complexity increases

Engineering Contradiction:
Improveheat lossVSAvoidreactor structure
Core Design Contradiction:
Loss of energyVSDevice complexity

Solution Approach 1:

The invention employs a nested double-tube reactor structure where the combustion chamber is positioned inside the ammonia cracking reactor. This nesting arrangement allows direct thermal coupling between the hot combustion gases in the inner tube and the ammonia feed in the outer tube, maximizing heat transfer efficiency and minimizing energy losses while containing the complexity within a compact integrated design.

Inventive Principle:
Principle #7Nested doll (Nesting)

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 process achieves high energetic efficiency, with over 90% of the energy content of ammonia being retained in the product gas stream, making it suitable for use in heat engines with minimal energy losses.

Implementation Method 1

The annular gap between the inner and outer tubes is filled with a standard catalyst for splitting ammonia

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 2

The splitting reaction of ammonia to hydrogen and nitrogen is endothermic. It usually takes place with the support of a cracking catalyst at temperatures above 400 °C, usually above 600 °C

Methodology Applied
Scientific EffectThermolysis: Thermolysis

Implementation Method 3

Heating occurs by burning the hydrogen in the inner tube

Methodology Applied
Scientific EffectCombustion: Combustion

Implementation Method 4

Because of the endothermy, an energy supply from outside is required to maintain the reaction. This energy is generated by burning some of the hydrogen produced by ammonia splitting

Methodology Applied
Scientific EffectExothermic Reaction: Exothermic Reaction

Implementation Method 5

To improve the heat balance, the ammonia gas is also mixed with the outgoing combustion exhaust gases via a heat exchanger WT1 before flowing into the cracking reactor preheated

Methodology Applied
Scientific EffectHeat Exchanger: Heat Exchanger

Implementation Method 6

The reaction is expediently carried out in a countercurrent process, since in this case the heat losses are kept small

Methodology Applied
Scientific EffectConvection: Convection

Data Source

PatentEP3028990B1Method for the preparation of hydrogen as a fuel by ammonia cracking
Publication Date: 2017.08.02 WANNEMACHER GERHARD
  • EP3028990B1 patent drawingFigure 1~4

AI summary

The present invention provides a practical method for using ammonia as a fuel, for example, for building heating or in a heat engine. Combustion does not occur directly; instead, the ammonia is first split into its components, hydrogen and nitrogen, and this gas mixture is used as fuel. The splitting reaction takes place in a fixed-bed catalyst, with the energy required for the endothermic splitting reaction being generated by burning a portion of the hydrogen-nitrogen mixture obtained from the ammonia splitting and being supplied to the fixed-bed catalyst via heat exchanger surfaces.