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Clean Hydrogen Partnership

Over-pressurisation of a LH2 tanker

Event

Event ID
527
Quality
Description
A liquid hydrogen tanker was travelling back to the base after having made an earlier delivery. At the end of the delivery, the pressure in the tanker had been reduced to 75 psig using the vent stack installed at the customer unit.
During a routine stop to conduct a check of the tires and of the tank pressure, the drivers noted that the pressure had risen to 138 psig (9.5 barg), in excess of the anticipated pressure rise for a hydrogen tanker. To prevent any unexpected venting of hydrogen gas, they exited the highway and stopped at an abandoned gas station. There the drivers ("blew down") reduced manually the tank pressure to 75 psig (5.2 barg) and restarted the travel. When the tanker had travelled for approximately 6 hr, the pressure had climbed back to 120 psig (8.3 barg). It is not mentioned in the report, but it is probable that the drivers decided to repeat the blow down procedure before arriving at the home terminal (probably at additional 3 hr driving).
The trailer was removed from service because of the deterioration of the vacuum of the thermal insulation shell.
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 (Thermal Insulation Degradation)
Root causes
Root CAUSE analysis
The INITIAL CAUSE was over-pressurisation of the LH2 tank, which caused an intevention of the drivers to reduce pressure.
The ROOT CAUSE was the degradation of the thermal insulation capacity of the tank.

Facility

Application
Hydrogen Transport And Distribution
Sub-application
LH2 tanker
Hydrogen supply chain stage
Hydrogen Transport (No additional details provided)
All components affected
vacuum thermal insulation
Location type
Open
Operational condition
Pre-event occurrences
The tanker was almost empty, after delivery.

Emergency & Consequences

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

Event Nature

Release type
gas
Involved substances (% vol)
H2 100%
Actual pressure (MPa)
1.05
Design pressure (MPa)
0.62
Presumed ignition source
No ignition

References

Reference & weblink

Incident I-1997080401 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