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
- Sources categories
- PHMSA