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Clean Hydrogen Partnership

Fire from a LH2 tanker during transfer

Event

Event ID
370
Quality
Description
A liquid hydrogen tanker was preparing to transfer hydrogen to a stationary tank belonging to a manufacturing facility. The tanker was being pressurised before transfer, when a burst disc failed prematurely. The hydrogen ignited at the vent stack. The fire lasted approximately one hour. The emergency responders decided to evacuate the manufacturing facility and a nearby bowling alley.
The bursting disc was one of two pressure relief devices protecting the tanker from over-pressurisation. In this sense, even if it failed prematurely, it resulted in a safe situation, with the hydrogen venting via the vent stack and the tank reducing internal pressure.

The disc was rated for 210 psig (14.5) but failed prematurely at approximately 145 psig (ca. 11 bar).
Event Initiating system
Classification of the physical effects
Hydrogen Release and Ignition
Nature of the consequences
Fire (No additional details provided)
Macro-region
North America
Country
United States
Date
Main component involved?
Prd (Burst Disc)
How was it involved?
Premature Activation
Initiating cause
Unknown
Root causes
Root CAUSE analysis
The INITIAL CAUSE was the premature failure of a burst disc.
In absence of the results of an post-incident investigation, it is impossible to attribute a ROOT CAUSE which could be related to material ageing, or to wrong installation or to a wrong choice of materials.

Facility

Application
Hydrogen Transport And Distribution
Sub-application
LH2 tanker
Hydrogen supply chain stage
Hydrogen Transfer (No additional details provided)
All components affected
burst disc
Location type
Open
Location description
Industrial Area
Operational condition

Emergency & Consequences

Number of injured persons
0
Number of fatalities
0
Environmental damage
0
Currency
US$
Property loss (onsite)
1500
Property loss (offsite)
0
Post-event summary
A negligible amount of hydrogen was released.

Lesson Learnt

Lesson Learnt


The safety system worked as expected. The tank was equipped with two independent pressure relief devices, protecting the trailer tank from over-pressurisation. Even if one of the two burst discs failed prematurely, it resulted in a safe situation, with the hydrogen venting via the vent stack and the tank reducing internal pressure.

Event Nature

Release type
gas
Involved substances (% vol)
H2 100%
Released amount
16.8
Actual pressure (MPa)
1.1
Design pressure (MPa)
1.45
Presumed ignition source
Not reported

References

Reference & weblink

Incident I-1995040335 of the US Pipeline and Hazardous Materials Safety Administration PHMSA: <br />
https://portal.phmsa.dot.gov/analytics/saw.dll?Portalpages&PortalPath=%… />
(accessed September 2024)

JRC assessment