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Clean Hydrogen Partnership

Hydrogen leak at a refinery

Event

Event ID
952
Quality
Description
The release occurred on a pipeline inside a steam cracking unit located between two hydrogenation units. The gaseous mixture transported through this line (2" diameter, 30 bar, 40°C) was composed of 95% hydrogen, 4% methane and 1% nitrogen. The line was located in a rack within the cold sector, at a height of 6 m.
The personnel shut down the steam cracker and isolated the sector and the units cuts were sent to the flare system. The leak was successfully sealed at noon, and the steam cracker remained down for a full 24 hours.

Runoff due to water vapour condensation was observed on a cold pipe located above the perforated piping assembly. This drop-by-drop action had weakened the pipeline, causing corrosion and thinning of the upper surface.
The perforation had resulted from a pressure shock during operation. The Classified Facilities inspection authorities noted that the pipeline had not been protected against corrosion by a coat of paint. This pipe section, had been monitored by an accredited inspection body focusing on individual problem areas, repainted in 1990 and then verified in both 2000 and 2007. However, during this last inspection, it had been commented that the particular section was inaccessible
due to the expansion layer formed by corrosion/erosion and therefore could not be controlled. The 2007 investigations did not allow for measuring the magnitude of corrosion, and no specific guideline was issued for the restoration of this section (painting work at the very least). The inspectors also noticed runoff on the pipe racks through this zone, along with a major degradation of pipe paint, which in some cases had totally disappeared.

Event Initiating system
Classification of the physical effects
Unignited Hydrogen Release
Nature of the consequences
Leak No Ignition (No additional details provided)
Macro-region
Europe
Country
France
Date
Root causes
Root CAUSE analysis
INITIATING cause of the leak was the weakening of the pipe due to external corrosion by water drop, followed by a mechanical shock during operation.

According to the ARIA report (see references) the root cause was the inadequate inspection and consequent failure of damage detection and repair.

Facility

Application
Petrochemical Industry
Sub-application
Steam methane reforming
Hydrogen supply chain stage
All components affected
pipeline, steam cracker
Location type
Open
Location description
Industrial Area
Operational condition

Emergency & Consequences

Number of injured persons
0
Number of fatalities
0

Lesson Learnt

Lesson Learnt

The ARIA report (see references) does not mention corrective actions, but it appears clear that the inspection methodology must improve, to avoid recurrence of similar accidents.

Event Nature

Release type
gas mixture
Involved substances (% vol)
H2 95%
CH4 4%
N2 1%
Actual pressure (MPa)
3
Design pressure (MPa)
3
Presumed ignition source
No ignition

References

Reference & weblink

Event description in the French database ARIA<br />
https://www.aria.developpement-durable.gouv.fr/accident/38140/<br />
(accessed October 2020)<br />

JRC assessment