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Clean Hydrogen Partnership

Explosion at a high-pressure furnace

Event

Event ID
1212
Quality
Description

The accident occurred during the manufacture of pharmaceutical intermediates using a high-pressure gas reactor. The reactor used a metal catalyst to react a liquid intermediate with hydrogen to produce a pharmaceutical raw material. The reactor's operating pressure (approximately 14 MPa) was controlled by adjusting the hydrogen supply quantity. The hydrogen was supplied by a battery of tubes on a trailer, at approximately 18 MPa.

The reactor was shut down due to a blockage in the sampling line caused by a powder metal catalyst. The reactor was then depressurised, and the sampling line was removed for cleaning and maintenance. The next day, a nitrogen gas cartridge was connected to the reactor's pneumatic test line to perform a leak test. However, the valve on the hydrogen supply line was not closed, allowing hydrogen to mix with the nitrogen gas. The mixed gas was then released into the sampling box, where it ignited and exploded due to static electricity.

Event Initiating system
Classification of the physical effects
Hydrogen Release and Ignition
Nature of the consequences
Macro-region
Asia
Country
Japan
Date
Component involved
reactor / oven / furnace / test chamber
Failure mode
internal explosion
Initiating cause
wrong component
Root CAUSE analysis

The INITIATING CAUSE was a hydrogen supply valve accidentally left open when performing a leak test with nitrogen. When the testing gas was released via the high-pressure reaction into the sampling box containing air, hydrogen ignited.

The IGNITION SOURCE was static electricity discharge. The sampling box made of PVC, which is prone to static electricity. It was insufficiently grounded. The fact that the metal catalyst remained in the reactor during testing was probably an additional ignition factor.

The leak test was executed according to verbal instruction only. The fact that the supply valve was left open can be attributed to a human mistake, but it was triggered by the lack of written procedure for leak test and the absence of an independent check on a status of a component critical to safety. Deficiencies in the safety design contributed as well.

Root causes
Date entry in HIAD
30/03/2026

Facility

Application
Chemical industry
Sub-application
Pharmaceutical production
Hydrogen supply chain stage
Process temperature range [C]
ambient temperature (-50°C to +50°C)
Location type
Confined
Location
unknown
Operational condition
Description of the facility/unit/process/substances

The process was working at high pressure (short below 15 Mpa). The proces cemperature is not provided. The event occurred the process suhut down and in the samling box, at a pressure probably not much higher than the ambient pressure.

Emergency & Consequences

Number of fatalities
0
Number of injured persons
0
Currency
Yen
Property loss (onsite)
100.000
Post-event summary

The front door and the side panel of teh sampling box wasdamaged, for approximately 100,000 yen.

Emergency action

Timeline of Accident:
June 19: Reactor shutdown, sampling line removal, and maintenance
June 20:
- 9:00 AM: Nitrogen gas cartridge connected to reactor's pneumatic test line
- 11:44 AM: Explosion occurred during depressurisation of reactor
- 11:56 AM: Emergency services notified
- 12:00 PM: County fire department arrived at the scene
- 1:40 PM: Fire department left the scene

Lesson Learnt

Lesson Learnt

This event highlighted the importance of written and communicated procedures and the independent assessment of their execution.
As stated also by the KHK report, the event reminded:
1. The need for careful planning and execution of work involving flammable gases.
2. The importance of communication when executing work in a team.
3. The need for a regular check of the hazards and risks, in combination with safety inspections and safety training.

Corrective Measures

The production process was suspended until countermeasures were completed, two months later.

(1) Improvement of the design by adopting physical countermeasures: the sampling box was replaced with a metal one. Its grounding ensured and ignition source during sampling avoided.

(2) Management countermeasures (also avoiding the possibility of a human error): leak test instruction were written, a check on the valve status foreseen and a final formal communication that all preparatory steps had been executed.

In-depth data

Release type
gas
Involved substances (% vol)
H2 100%
Release temperature [°C]
25
Probable IGNITION SOURCE
Explosion type

References

Sources categories
KHK
Reference & weblink

KHK accidents database, incident 2023-188 (in japanese):
https://www.khk.or.jp/Portals/0/khk/hpg/accident/2023/05_2023-188.pdf
(accessed may 2025)

KHK accidents database, incident 2023-188 (translated in EN):