Hydrogen Generator Reformer Catalyst Protection During Shutdown

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Solution Overview

Problem

Conventional hydrogen generators face challenges in maintaining catalytic activity during stop operations due to high-temperature oxidization and inappropriate internal gas replacement, leading to decreased performance and efficiency.

Innovation Solution

A hydrogen generator with a controller that adjusts the composition of the replacement gas based on the temperature condition of the reformer, using a mixture of materials, steam, air, and inert gases to prevent catalytic deactivation, and includes sensors to detect temperature and operating states for precise gas replacement.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Duration of action of moving object

If the hydrogen generator is stopped after operation, then the system can be shut down for maintenance or relocation, but the catalyst undergoes high-temperature oxidization and deactivation

Engineering Contradiction:
Improveoperational flexibilityVSAvoidcatalytic activity
Core Design Contradiction:
Duration of action of moving objectVSReliability

Solution Approach 1:

The controller performs preliminary cooling of the catalyst by continuing to supply water for steam generation even after the heater is stopped. This preliminary cooling action prevents the catalyst from undergoing high-temperature oxidization when air enters the generator during shutdown, thereby maintaining catalytic activity while allowing operational flexibility

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The system maintains an inert steam atmosphere around the catalyst during the cooling phase after shutdown. By continuing to generate steam from supplied water and preventing air ingress during this critical period, the catalyst is protected from oxidization in an inert environment until it cools to a safe temperature

Inventive Principle:
Principle #39Inert atmosphere (Inert environment)

2Reliability

If internal gas replacement operation is performed with inert gas, then catalytic activity is protected, but infrastructure for inert gas supply is required

Engineering Contradiction:
Improvecatalytic activityVSAvoidgas supply infrastructure
Core Design Contradiction:
ReliabilityVSDevice complexity

Solution Approach 1:

The system uses its own water supply to generate steam that serves as the protective atmosphere during shutdown. The controller continues to supply water to the steam generation section, and the resulting steam automatically replaces and protects the catalyst without requiring external inert gas infrastructure

Inventive Principle:
Principle #25Self-service

Solution Approach 2:

The system changes the parameter of the protective gas from external inert gas to internally generated steam by controlling the water supply parameter. The controller adjusts water supply timing and quantity to generate sufficient steam for catalyst protection, eliminating the need for external gas infrastructure while maintaining catalytic activity

Inventive Principle:
Principle #35Parameter changes

3Productivity

If the heater continues operating during stop operation, then temperature is maintained for quick restart, but energy consumption increases and catalyst damage risk increases

Engineering Contradiction:
Improverestart speedVSAvoidenergy consumption
Core Design Contradiction:
ProductivityVSLoss of energy

Solution Approach 1:

The system performs preliminary cooling of the catalyst using the steam generation method after the heater is stopped. This preliminary cooling action prevents catalyst damage while the steam maintains a safe temperature range, enabling relatively quick restart without continuous heater operation

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The water supply for steam generation continues after the heater stops, maintaining a useful thermal environment for the catalyst through steam rather than direct heating. This continuous steam supply protects the catalyst while reducing energy consumption compared to continuous heater operation

Inventive Principle:
Principle #20Continuity of useful action

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 configuration ensures stable hydrogen production by preventing catalytic deactivation, reducing carbon deposition, and optimizing gas replacement according to varying temperature conditions, thereby extending catalyst life and maintaining generator efficiency.

Implementation Method 1

a reformer configured to generate a hydrogen-rich reformed gas by causing a material containing an organic compound comprised of at least carbon and hydrogen to react with steam with the use of a catalyst

Methodology Applied
Scientific EffectSteam reforming: Chemical Transport Reactions

Implementation Method 2

a heater configured to heat at least the reformer

Methodology Applied
Scientific EffectHeating: Heating

Implementation Method 3

a water supply portion configured to supply water that is evaporated into the steam to the hydrogen generating portion

Methodology Applied
Scientific EffectEvaporation: Evaporation

Implementation Method 4

the controller is configured to control at least the heater, the material supply portion, and the water supply portion; the hydrogen generator being configured to stop heating in the heater at a start of a stop operation

Methodology Applied
Scientific EffectCooling: Cooling

Data Source

PatentUS7419518B2Hydrogen generator and fuel cell system
Publication Date: 2008.09.02 PANASONIC HOLDINGS CORP
  • US7419518B2 patent drawing
  • US7419518B2 patent drawing
  • US7419518B2 patent drawing

AI summary

In a hydrogen generator according to the invention, a reformer temperature sensor detects the temperature of a reformer at a start of a stop operation of a hydrogen generator. In a controller, a processing and controlling portion compares the detected temperature with first to fourth reference temperatures pre-stored in a storage portion, and determines which of the following conditions is the temperature condition of the hydrogen generator at the stop; a first condition in which water condensation occurs, a second condition in which water condensation and carbon deposition are avoidable, a third condition in which carbon deposition occurs, a fourth condition in which disproportionation reaction occurs, and a fifth condition in which oxidization of catalyst occurs. According to the determination result, an appropriate setting is selected among first to fifth replacement settings pre-stored in the controller corresponding to the first to fifth conditions, and an internal gas replacement operation is performed according to the selected setting.