Event
- Event ID
- 113
- Quality
- Description
- A liquid hydrogen tanker was en route on the highway when the driver noticed a vapour plume in the rear-view mirror. The driver exited the highway and stopped at the first available safe location.
Upon inspection of the cargo, the driver noticed that the pressure in the inner vessel of the double-walled tank had risen above 3.45 barg (50 psig), causing the opening of the safety relief valve.
Later, a thorough inspection revealed a leak in the annular space vacuum relief plate, leading to a loss of vacuum. That failure increased the heat transfer to the cryogenic hydrogen, consequently increasing vaporisation. - Event Initiating system
- Classification of the physical effects
- Unignited Hydrogen Release
- Nature of the consequences
- Macro-region
- North America
- Country
- United States
- Date
- Main component involved?
- Prd (Valve)
- How was it involved?
- Correct Activation
- Initiating cause
- Over-Pressurisation (Thermal Insulation Degradation)
- Root causes
- Root CAUSE analysis
- The INITIATING CAUSE was a loss of vacuum of he insulation shell of the liquid hydrogen tank. The Pressure Relief Device (PRD) worked as expected.
Facility
- Application
- Hydrogen Transport And Distribution
- Sub-application
- LH2 tanker
- Hydrogen supply chain stage
- Hydrogen Transport (No additional details provided)
- All components affected
- PRD
- Location type
- Open
- Operational condition
Emergency & Consequences
- Number of injured persons
- 0
- Number of fatalities
- 0
- Environmental damage
- 0
- Property loss (onsite)
- 0
- Property loss (offsite)
- 0
- Post-event summary
- This is a near miss. The PRD functioned as expected, releasing the hydrogen vapour in overpressure
- Emergency action
- It took 4 hours to bring the fire under control, When the fire was extinguished 2 of the 4 gas circulator systems and 2 of the 4 main heat exchanger systems were knocked out and 2 RHR systems in the reactor basements were disabled by flooding.
Lesson Learnt
- Lesson Learnt
This is an example of a successful mitigation of a mechanical failure. On a liquid hydrogen tank, the function of the Pressure Relief Device (PRD) is to release hydrogen vapour, when the tank internal pressure increase due to the evaporation of liquid hydrogen. The reduction of the insulation capacity of the tank accelerated the evaporation rate and the PRD released more vapour. In this way, the internal pressure of the tank remained below the maximal allowed value.
Event Nature
- Release type
- gas
- Involved substances (% vol)
- H2 100%
- Actual pressure (MPa)
- 0.345
- Design pressure (MPa)
- 0.345
- Presumed ignition source
- No ignition
References
- Reference & weblink
Event incident ID I-1996071466 of the PHMSA database (Pipeline and Hazardous Materials Safety Administration, 1996),<br />
https://portal.phmsa.dot.gov/analytics/saw.dll?Portalpages<br />
(accessed September 2024)A. Jimenez, C. Groth,<br />
Hazards associated with pressure relief devices in hydrogen systems, <br />
Journal of Loss Prevention in the Process Industries<br />
91 (2024), 105380, https://doi.org/10.1016/j.jlp.2024.105380
JRC assessment
- Sources categories
- PHMSA