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Clean Hydrogen Partnership

Explosion in a pharmaceutical plant

Event

Event ID
664
Quality
Description

A hydrogen gas holder exploded.
It is assumed that there was diaphragm leak in the hydrogen-oxygen electrolytic cell used to produce high purity hydrogen for a pharmaceutical hydrogenation.

Event Initiating system
Classification of the physical effects
Hydrogen Release and Ignition
Nature of the consequences
Macro-region
Europe
Date
Component involved
gasholder/gasometer (H2)
Failure mode
internal explosion
Initiating cause
malfunctioning (electrolyser, cross-over)
Root CAUSE analysis

The INITIATING CAUSE was a through the diaphragm of the electrolyser cell membrane, which caused injection of oxygen into the hydrogen stream flow, ending in the hydrogen storage.

The ROOT CAUSE is not reported, but it could be assigned to design (lack of measures of process parameters) and management (inadequate risk assessment).

Root causes
Date entry in HIAD
01/01/2020

Facility

Application
Hydrogen production
Sub-application
Water electrolysis
Hydrogen supply chain stage
All components affected

electrolytic cell, diafragm, gasholder

Process temperature range [C]
ambient temperature (-50°C to +50°C)
Location type
Unknown
Location
unknown
Operational condition

Emergency & Consequences

Number of fatalities
unknown
Number of injured persons
unknown

Lesson Learnt

Lesson Learnt

The incident occurred at the hydrogen storage tank, but it was caused by a cross-over of oxygen into the hydrogen stream flow.
This incident occurred a lot of time before the incident reported in HIAD_970, occurred in Korea in 2019. Oxygen and hydrogen cross-over in the electrolytic cell is a well-known phenomenon. The severity of the occurrence depends on the electrolysis technology and the operative parameter, nevertheless it is a hazard which must be monitored, and its consequences prevented. Without proper diagnostic able to detect timely the formation of flammable mixture in the hydrogen line, this is not possible. Little is known about this incident, but an automatic system able to stop hydrogen production when concentrations trespass a threshold would have been able to avoid the creation of flammable mixture in the gas holder.

In-depth data

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

References

Sources categories
News
Reference & weblink

Loss Prevention, Vol 3.