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Clean Hydrogen Partnership

Hydrogen fire in a refinery

Event

Event ID
958
Quality
Description
A hydrogen leak occurred on the hydrogen line of a hydro-desulphurisation unit, followed by ignition . The failure was located on a supply manifold of the unit at a support beam. The unit was shut down.

The accident was caused by external corrosion which had developed at a support point, under the pipe insulation. A regular thinning of the piping was observed over a length of 450 mm on the lower semi-circumference. The maximum thickness loss was 6.5 mm. The mechanical analysis concluded that the operating pressure was sufficient to cause this initial failure in the weakened area. Its propagation resulted from the dynamic load applied to the line.
Event Initiating system
Classification of the physical effects
Hydrogen Release and Ignition
Nature of the consequences
Fire (No additional details provided)
Macro-region
Europe
Country
France
Date
Main component involved?
Manifold
How was it involved?
Leak & Formation Of A Flammable H2-Air Mixture
Initiating cause
Material Degradation (External Corrosion)
Root causes
Root CAUSE analysis
INITIATING CAUSE was the thinning of the pipe wall caused by external, not further specified corrosion.

The ROOT CAUSE is not provided, but by proxy with similar cases, it could be concluded that lack of correct non-distructive assessment system did not allow for timely detection of the loss of wall thickness due to corrosion.

Facility

Application
Petrochemical Industry
Sub-application
Hydrodesulphurisation process
Hydrogen supply chain stage
All components affected
hydrogen pipeline, manifold
Location type
Open
Location description
Industrial Area
Operational condition

Emergency & Consequences

Number of injured persons
0
Number of fatalities
0
Environmental damage
0

Lesson Learnt

Lesson Learnt
Undetected external corrosion of high-temperature pipe connection is a common cause of loss of confinement. The presence of a thermal insulation layers around the piping does not allow for a visual inspection of the components, and in absence of sound non-destructive assessment tools and methods, the corrosion can proceed and reduce the load-bearing section of the pipe, until the internal pressure cause it burst. Similar cases are described, among others, by events HIAD_ 1067 and HIAD_83.

Event Nature

Release type
gas
Involved substances (% vol)
H2 100%
Release duration
unknown
Presumed ignition source
Not reported
Flame type
Other

References

Reference & weblink

Event description in the French database ARIA<br />
https://www.aria.developpement-durable.gouv.fr/accident/52695/<br />
(accessed October 2020)<br />

JRC assessment