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Clean Hydrogen Partnership

Road accident involving a LH2 tanker

Event

Event ID
847
Quality
Description
A 40,000-litre capacity tanker carrying liquid hydrogen tipped over into a ditch on a curve in an intersection while travelling on a municipal road at the edge of town.
The lorry had just left a SEVESO-rated industrial gas production plant.
The cistern was retained by an electrical tower and did not completely overturn. A whitish cloud dispersed through the degassing chimney on top of the cistern.
First responders set up a 200-m safety perimeter and evacuate the neighbours. The container’s internal pressure remains at approximately 0.1 relative bar. The explosimeter measurements conducted at the degassing chimney outlet, at a height of 3-4 m, remained positive.
At 2:30, fire-fighters extended the safety perimeter to 600 m and lifted the cistern, thereby allowing technicians with the transport company to access the cistern control box. Responders closed the hydrogen degassing valve, which had been slightly opened due to the shock produced by the accident. The explosimeter measurements then turned negative.
Around 5:30 pm, the semitrailer was placed back on the road and escorted into the industrial gas production plant, which was equipped with a degassing unit. For the most part, the cloud was composed of liquid nitrogen used to maintain the hydrogen at a cold temperature. The inclined position of the cistern had caused the liquid nitrogen spillage. The cryogenic cloud dissipated thereafter.

The Inspectorate visited the site. Given the presence of nitrogen protoxide storage, only empty semitrailers were allowed on the site. According to the operator, the lorry driver had come to the site of his own initiative, looking for replacement hoses. He accessed the site without waiting for the shift foreman’s approval and entered through the door that had not immediately closed following entrance of the previous vehicle. Realising that the tanker lorry loaded with liquid hydrogen had accessed the site without authorisation, the foreman asked the driver to back up. During the manoeuvre, the lorry bumped the gate. The foreman then requested he exit the site by the rear; in advancing along this path, the driver missed a turn.
Nitrogen protoxide production resumed 3 days later.

The Inspectorate noted a procedural problem in the industrial site’s safety management system (SMS), as the vehicle filled with liquid hydrogen should never have allowed accessing the site. Inspectors requested that the site operator issue a report analysing the causes of this incident. A follow-up inspection was ordered to ensure that new organisational measures had indeed been implemented as part of the operator’s Safety management System.
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
Main component involved?
Valve (Generic)
How was it involved?
Rupture
Initiating cause
Impact, Rollover, Crash
Root causes
Root CAUSE analysis
INITIATING CAUSE was the tippingand collision with a building.
The ROOT CAUSE was a wrong manoeuvre to by the driver, and a glitch in the procedure controlling access to the site.

Facility

Application
Hydrogen Transport And Distribution
Sub-application
LH2 tanker
Hydrogen supply chain stage
Hydrogen Transport (No additional details provided)
All components affected
40,000-litre capacity tanker lorry carrying liquid hydrogen
Location type
Open
Location description
Industrial Area
Operational condition

Emergency & Consequences

Number of injured persons
0
Number of fatalities
0
Post-event summary
Plant production (nitrogen protoxide) resumed 3 days later.
Official legal action
The Classified Facilities Inspectorate noted a procedural problem in the industrial site’s safety management system (SMS).
A follow-up inspection was ordered to ensure that new organisational measures had indeed been implemented as part of the operator’s SMS.

Event Nature

Release type
gas
Involved substances (% vol)
H2 100%
Actual pressure (MPa)
0.11
Design pressure (MPa)
0.11
Presumed ignition source
No ignition

References

Reference & weblink

ARIA database event no. 34779<br />
https://www.aria.developpement-durable.gouv.fr/accident/34779/<br />
(Accessed December 2023)

JRC assessment