Hydrogen Generator Ammonia Poisoning Control

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Solution Overview

Problem

Conventional fuel cell systems face performance deterioration due to ammonia poisoning of the oxidation catalyst in the purifier, leading to reduced carbon monoxide removal capability and unstable electric power generation, especially when nitrogen-containing compounds are used in the reforming reaction.

Innovation Solution

A hydrogen generator configuration that includes a reformer, a CO remover with an oxidation catalyst, and a control unit to regenerate the oxidation catalyst when a cumulative ammonia threshold is reached, ensuring the catalyst's performance is maintained and carbon monoxide levels are adequately reduced, even with nitrogen-containing compounds in the reforming reaction.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If nitrogen-containing compounds are supplied to the reformer during the reforming reaction, then the productivity of hydrogen-containing gas is improved, but the oxidation catalyst is poisoned by ammonia and the carbon monoxide removal capability deteriorates

Engineering Contradiction:
Improvehydrogen-containing gas productionVSAvoidcarbon monoxide removal capability
Core Design Contradiction:
ProductivityVSReliability

Solution Approach 1:

The control unit performs preliminary action by monitoring the cumulative supply amount of nitrogen-containing compounds and predicting ammonia generation before the oxidation catalyst is severely poisoned. When the predicted cumulative ammonia amount reaches a predetermined threshold, the control unit proactively switches to a regeneration mode, preventing catastrophic catalyst deactivation and maintaining continuous carbon monoxide removal capability.

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The invention changes operational parameters by switching between normal operation mode and catalyst regeneration mode. During regeneration, the supply of nitrogen-containing compounds is stopped or reduced, and the oxidation catalyst is treated with reducing conditions to remove accumulated ammonia. This parameter change restores the catalyst's carbon monoxide removal capability while allowing continued hydrogen production during normal operation.

Inventive Principle:
Principle #35Parameter changes

2Device complexity

If the oxidation catalyst is continuously operated without regeneration, then the device complexity is reduced, but the catalyst performance deteriorates due to ammonia accumulation

Engineering Contradiction:
Improvesystem structureVSAvoidcatalyst performance
Core Design Contradiction:
Device complexityVSReliability

Solution Approach 1:

The system implements self-service through the control unit that automatically monitors the cumulative supply amount of nitrogen-containing compounds, predicts ammonia accumulation, and autonomously switches between normal operation and catalyst regeneration modes. This self-monitoring and self-regulating mechanism maintains catalyst performance without requiring external intervention or complex additional regeneration equipment.

Inventive Principle:
Principle #25Self-service

Solution Approach 2:

The invention applies periodic action by alternating between normal operation phases (where nitrogen-containing compounds are supplied for hydrogen production) and catalyst regeneration phases (where the oxidation catalyst is treated to remove ammonia). The control unit determines the timing of regeneration based on cumulative supply thresholds, creating a periodic cycle that maintains catalyst effectiveness over extended operation periods.

Inventive Principle:
Principle #19Periodic 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 stabilizes the supply of high-quality hydrogen-containing gas with reduced carbon monoxide levels, preventing catalyst poisoning and ensuring long-term stable electric power generation in fuel cell systems.

Implementation Method 1

In the steam reforming, a hydrocarbon raw material (material gas), such as a natural gas, a propane gas, naphtha, gasoline and kerosene and water are mixed, or an alcohol material, such as methanol and water are mixed. Then, the mixture is supplied to a reformer including a reforming catalyst. In the reformer, a steam-reforming reaction proceeds, so that the hydrogen-containing gas containing hydrogen is generated.

Methodology Applied
Scientific EffectSteam reforming reaction: Chemical Transport Reactions

Implementation Method 2

a purifier which is disposed downstream of the shift converter and has at least one of an oxidation catalyst which causes an oxidation between oxygen in the air and carbon monoxide to proceed

Methodology Applied
Scientific EffectOxidation: Oxidation

Implementation Method 3

The CO reducer usually includes a shift converter which causes a water gas shift reaction to proceed at a shift catalyst disposed therein to generate hydrogen and carbon dioxide from carbon monoxide and steam.

Methodology Applied
Scientific EffectWater gas shift reaction: Chemical Transport Reactions

Implementation Method 4

an oxidation catalyst which causes an oxidation between oxygen in the air and carbon monoxide to proceed

Methodology Applied
Scientific EffectOxidation: Oxidation

Data Source

PatentUS8652224B2Hydrogen generator, fuel cell system and their operating methods
Publication Date: 2014.02.18 PANASONIC HOLDINGS CORP
  • US8652224B2 patent drawing
  • US8652224B2 patent drawing
  • US8652224B2 patent drawing

AI summary

A hydrogen generator (4) includes: a reformer (5) which is supplied with a raw material to generate a hydrogen-containing gas through a reforming reaction; a first gas supplying unit (1) which supplies a gas containing a nitrogen-containing compound to the reformer; a CO remover (7) which has an oxidation catalyst containing a metal to be poisoned by ammonia and uses the oxidation catalyst and an oxidation gas to remove carbon monoxide in the hydrogen-containing gas through an oxidation; a second gas supplying unit (3) which supplies the oxidation gas to the CO remover; and a control unit (10), wherein the gas containing the nitrogen-containing compound is supplied from the first gas supplying unit to the reformer during the reforming reaction, a fuel cell system (100) includes the hydrogen generator (4), and the control unit is configured to control to carry out a regeneration operation of the oxidation catalyst if a parameter regarding a cumulative amount of ammonia supplied to the CO remover has reached a predetermined threshold or more.