Radiating Wall Catalytic Reactor Segmentation

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Solution Overview

Problem

Existing reactors face challenges in achieving uniform temperature distribution and efficient heat transfer during endothermic chemical reactions, leading to potential hot spots, incomplete reactions, and reduced reactor lifespan due to high temperatures.

Innovation Solution

A radiating wall catalytic reactor design with a reaction chamber comprising alternating catalyst segments and void segments, where heat is radiated from the inside wall surface to the catalyst segments, enhancing radiation-based heat transfer and maintaining a higher outside wall temperature than the inside wall, thus promoting more uniform temperature distribution and efficient heat exchange.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Temperature

If the outside surface of the reaction chamber is heated to very high temperatures to maintain high interior temperature for endothermic reactions, then the reaction temperature is sufficient, but the reactor material lifespan decreases sharply

Engineering Contradiction:
Improvereaction temperatureVSAvoidreactor material lifespan
Core Design Contradiction:
TemperatureVSDuration of action of stationary object

Solution Approach 1:

The reaction chamber is divided into alternating catalyst segments and void segments along its length. This segmentation allows different zones to serve different functions: catalyst segments for chemical reactions and void segments for radiant heat transfer from the outer wall, thereby distributing thermal stress and avoiding excessive temperatures in any single location, which extends reactor lifespan while maintaining reaction temperature.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

Different segments of the reaction chamber are given different properties: catalyst segments contain catalytic material for chemical reactions, while void segments are designed for optimal radiant heat transfer from the outer wall. This local differentiation allows the system to achieve both high reaction temperatures and reduced thermal stress on materials by concentrating heating functions in specific zones rather than uniformly throughout.

Inventive Principle:
Principle #3Local quality

2Device complexity

If conventional heating methods are used with continuous catalyst beds, then the reactor structure is simple, but temperature distribution becomes non-uniform leading to hot spots and incomplete reactions

Engineering Contradiction:
Improvereactor structureVSAvoidtemperature distribution uniformity
Core Design Contradiction:
Device complexityVSTemperature

Solution Approach 1:

The continuous catalyst bed is segmented into discrete catalyst segments separated by void segments. This segmentation interrupts the continuous catalytic zone and introduces radiant heat transfer zones, creating a more uniform temperature distribution by preventing hot spot formation while maintaining overall structural simplicity through the repeating pattern.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

Void segments act as intermediary zones between catalyst segments, facilitating radiant heat transfer from the outer reaction chamber wall to the catalyst segments. These intermediary zones mediate the heat transfer process, ensuring uniform temperature distribution across the catalyst bed without requiring complex internal heating structures.

Inventive Principle:
Principle #24Intermediary (Mediator)

3Loss of energy

If large temperature gradients exist from wall to tube centre, then heat transfer from wall is efficient, but centre region experiences lower temperatures causing incomplete reactions and requiring longer reactor length

Engineering Contradiction:
Improveheat transfer efficiencyVSAvoidreaction completion efficiency
Core Design Contradiction:
Loss of energyVSProductivity

Solution Approach 1:

The reaction chamber is segmented into alternating catalyst and void zones, which creates multiple heat transfer interfaces along the reactor length. This segmentation allows radiant heat to be delivered directly to catalyst segments from the outer wall through the void segments, maintaining efficient heat transfer while ensuring adequate temperature in the centre region for complete reactions.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The patent transitions from conventional one-dimensional convective heat transfer (wall to fluid) to multi-dimensional radiant heat transfer by introducing void segments that allow direct line-of-sight radiation from the outer wall to catalyst segments. This dimensional change in heat transfer mechanism improves both heat transfer efficiency and temperature uniformity simultaneously.

Inventive Principle:
Principle #17Another dimension (Dimensionality change)

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 design achieves improved heat exchange and more uniform temperature distribution within the reaction chamber, increasing the reactor's throughput and extending its lifespan by allowing higher heat flux across the tube wall, enabling smaller or shorter reactors to achieve similar performance.

Implementation Method 1

providing heat from the inside wall surface of a reaction chamber by radiation to support an overall endothermic reaction taking place in the reaction chamber

Methodology Applied
Scientific EffectThermal radiation: Thermal Radiation

Data Source

PatentUS9505617B2Radiating wall catalytic reactor and process for carrying out a chemical reaction in this reactor
Publication Date: 2016.11.29 ALANTUM OJROPE GMBKH
  • US9505617B2 patent drawing
  • US9505617B2 patent drawing
  • US9505617B2 patent drawing

AI summary

Disclosed are a radiating wall catalytic reactor for providing heat from the inside wall surface 8 of a reaction chamber 1 by radiation 16 to support an overall endothermic gas phase chemical reaction taking place in the reaction chamber 1, and a process for carrying out a chemical reaction in the reactor. The reaction chamber 1 is provided with an entrance port 2 for introducing a gaseous reactant(s) in a continuous manner into the chamber 1 and an exit port 3 to enable the gaseous product(s) to leave the chamber 1 in a continuous manner. The reaction chamber 1 includes a plurality of catalyst segments (A)5, which has one void segment (B)6 on either side of it; and the reaction chamber 1 is made of a material(s) that is (are) suitable to resist a temperature of 700° C. or more.