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Clean Hydrogen Partnership

Over-pressurisation of a LH2 tanker

Event

Event ID
374
Quality
Description
A liquid hydrogen tanker was loaded at the home base and dispatched to a customer (approximately 790 km). The internal vessel pressure after filling was 8 psig (1.4 bara). During transit, the pressure remained stable at 8 psig until a safety check after 8 hours indicated a pressure of 17 psig (2.2 bara).
The drivers received instructions from their home terminal to switch to the 50 psi (4.5 bara) safety relief valve. The next safety check after additional 3.5 hours revealed a pressure rise to 30 psig (3.1 bara).
The drivers were instructed to move to a safe, isolated area to conduct a controlled venting. After venting down to 18 psig, the drivers continued transit to the customer site without further blow down.
Event Initiating system
Classification of the physical effects
Unignited Hydrogen Release
Nature of the consequences
Leak No Ignition (No additional details provided)
Macro-region
North America
Country
United States
Date
Main component involved?
Lh2 Tanker
How was it involved?
Manual Venting
Initiating cause
Over-Pressurisation (Boil-Off)
Root causes
Unknown (No additional details provided)
Root CAUSE analysis
The INITIATING CAUSE of the event was the increase of the internal pressure of the LH2 tank.

The report does not give insights on root causes. It could have been caused ((1) by over-pressurisation (overload) during filling at the base terminal, or (2) by a reduction of the thermal insulation capacity of the tank walls. It could also (3) have been integral part of the foreseen safety measures to be undertaken to counterbalance boil-off during a long travel.

Therefore, ROOT CAUSE is unknown.

Facility

Application
Hydrogen Transport And Distribution
Sub-application
LH2 tanker
Hydrogen supply chain stage
Hydrogen Transport (No additional details provided)
All components affected
LH2 tank overpressure
Location type
Open
Operational condition

Emergency & Consequences

Number of injured persons
0
Number of fatalities
0
Environmental damage
0
Currency
US$
Property loss (onsite)
25
Property loss (offsite)
0
Post-event summary
A negligible amount of hydrogen was released, with a loos of only 25 US dollars

Event Nature

Release type
gas
Involved substances (% vol)
H2 100%
Released amount
negligible
Actual pressure (MPa)
0.22
Design pressure (MPa)
0.14
Presumed ignition source
No ignition

References

Reference & weblink

Report I-1993081243 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