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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
Macro-region
North America
Country
United States
Date
Component involved
PRD (burst disc)
Failure mode
premature activation & venting
Initiating cause
unknown
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.

Root causes
Date entry in HIAD
16/11/2024

Facility

Application
Hydrogen transport and distribution
Sub-application
LH2 tanker
Hydrogen supply chain stage
All components affected

burst disc

Process temperature range [C]
cryogenic temperature (below -50°C)
Process pressure range [MPa]
low to medium pressure (below 2 MPa)
Location type
Open
Location
industrial area
Operational condition

Emergency & Consequences

Number of fatalities
0
Number of injured persons
0
Currency
US$
Property loss (onsite)
1.500
Post-event summary

A negligible amount of hydrogen was released.

Emergency action

The fire was left extinguish by itself. The manufacturing site was evacuate, as well as a neighbourhood.

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.

In-depth data

Release type
gas
Involved substances (% vol)
H2 100%
Released amount (kg)
16.8
Release pressure [MPa]
1.45
Probable IGNITION SOURCE

References

Sources categories
PHMSA
Reference & weblink

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