Air Feed Control for Reformer Catalyst Temperature

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Solution Overview

Problem

In heat and hydrogen generation devices, the reformer catalyst temperature rises excessively due to self-heating, leading to degradation, as the air fed into the burner combustion chamber is heated by the gas flowing out from the reformer catalyst, creating a feedback loop that increases the catalyst temperature.

Innovation Solution

A heat and hydrogen generation device with a controlled air feed system that includes a heat exchange part to regulate air temperature, using an electronic control unit to switch between high and low temperature air flow routes to maintain the reformer catalyst temperature below a predetermined safe level, preventing excessive heating.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Use of energy by moving object

If the air fed into the burner combustion chamber is heated by the gas flowing out from the reformer catalyst, then the heating efficiency is improved, but the temperature of the reformer catalyst rises excessively causing degradation

Engineering Contradiction:
Improveheating efficiencyVSAvoidreformer catalyst lifespan
Core Design Contradiction:
Use of energy by moving objectVSReliability

Solution Approach 1:

The system uses temperature detection means to continuously monitor the reformer catalyst temperature and feeds this information back to the air feed control means. The electronic control unit adjusts the air feed amount based on the detected temperature to maintain it within a predetermined range, preventing excessive temperature rise while preserving heating efficiency through controlled feedback regulation.

Inventive Principle:
Principle #23Feedback

Solution Approach 2:

The system dynamically changes the air feed parameter (air feed amount) based on the detected reformer catalyst temperature. When the temperature approaches the upper limit, the air feed amount is reduced; when the temperature is lower, the air feed amount is increased. This parameter adjustment maintains optimal operating conditions without causing catalyst degradation.

Inventive Principle:
Principle #35Parameter changes

2Productivity

If the temperature of the reformer catalyst is maintained high for efficient hydrogen generation, then the hydrogen generation efficiency is improved, but the catalyst degrades due to excessive heat

Engineering Contradiction:
Improvehydrogen generation efficiencyVSAvoidheat degradation
Core Design Contradiction:
ProductivityVSObject-affected harmful factors

Solution Approach 1:

The temperature detection means continuously monitors the reformer catalyst temperature and provides feedback to the air feed control means. This feedback mechanism allows the system to maintain the catalyst temperature within the optimal range for hydrogen generation while preventing it from exceeding the degradation threshold, thus preserving both productivity and catalyst integrity.

Inventive Principle:
Principle #23Feedback

Solution Approach 2:

The system establishes a predetermined temperature range with an upper limit that is set below the catalyst degradation temperature. By maintaining the temperature within this pre-defined safe range through continuous monitoring and control, the system prevents harmful thermal effects before they can occur, cushioning against potential catalyst damage.

Inventive Principle:
Principle #11Beforehand cushioning (Prior cushioning)

3Productivity

If the air feed amount is increased to control the reaction equilibrium temperature, then the reaction efficiency is improved, but the temperature of the air fed rises causing catalyst overheating

Engineering Contradiction:
Improvereaction efficiencyVSAvoidair fed temperature
Core Design Contradiction:
ProductivityVSTemperature

Solution Approach 1:

The air feed control means dynamically adjusts the air feed amount parameter based on real-time temperature detection. When the reformer catalyst temperature approaches the upper limit, the air feed amount is decreased; when the temperature is within the safe range, the air feed amount is maintained at optimal levels for reaction efficiency. This dynamic parameter change coordinates reaction efficiency with temperature control.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The electronic control unit receives temperature information from the temperature detection means and uses this feedback to adjust the air feed amount. This closed-loop control ensures that the air feed amount is optimized for reaction efficiency while simultaneously preventing the air fed temperature from rising to levels that would cause catalyst overheating.

Inventive Principle:
Principle #23Feedback

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 solution effectively prevents reformer catalyst degradation by controlling air temperature fed into the burner combustion chamber, ensuring the catalyst operates within a safe temperature range, thereby extending its lifespan and maintaining efficient hydrogen and heat generation.

Implementation Method 1

the air feed device being provided with a heat exchange part for heating the air fed from the burner into the burner combustion chamber by the burner combustion gas

Methodology Applied
Scientific EffectHeat exchange: Heat Exchanger

Implementation Method 2

a reformer catalyst to which burner combustion gas is fed, and heat and hydrogen being generated by performing the burner combustion

Methodology Applied
Scientific EffectCatalysis: Catalysis

Data Source

PatentUS10494256B2Heat and hydrogen generation device with ECU controlling air feed device
Publication Date: 2019.12.03 TOYOTA JIDOSHA KK
  • US10494256B2 patent drawing
  • US10494256B2 patent drawing
  • US10494256B2 patent drawing

AI summary

A burner combustion chamber (3), a reformer catalyst (4) to which burner combustion gas is fed, and a heat exchange part (13a) for heating the air fed to the burner (7) are provided. When the temperature of the reformer catalyst (4) exceeds the allowable catalyst temperature (TX) or when it is predicted the temperature of the reformer catalyst (4) will exceed the allowable catalyst temperature (TX), the air circulation route for guiding air to the burner (7) is switched from a high temperature air circulation route (13) for guiding air heated by the heat exchange part (13a) to the burner (7) to a low temperature air circulation route (14) for guiding air not flowing within the heat exchange part (13a) and lower in temperature than the air heated at the heat exchange part (13a) to the burner (7).