Event
- Event ID
- 156
- Quality
- Description
- A LH2 trailer was delivering at a customer’s site. Just after having terminated the transfer to the stationary tank approximately 13000 gallons (3500 kg) of liquid hydrogen, the pressure relief valve on the trailer activated at a tank pressure of approximately 120 psig (8.4 bar). The tanker was rated for 150 psig (9.7 bar). The venting hydrogen ignited.
The two tanks were still connected with the transfer hose. The driver immediately isolated the trailer and the customer storage tank and then called 911. The local fire department put in place an extensive emergency area, by evacuating residents and shutting down traffics. - Event Initiating system
- Classification of the physical effects
- Unignited Hydrogen Release
- Nature of the consequences
- Fire (No additional details provided)
- Macro-region
- North America
- Country
- United States
- Date
- Main component involved?
- Prd (Valve)
- How was it involved?
- Premature Activation
- Initiating cause
- Unknown
- Root causes
- Root CAUSE analysis
- The INITIAL CAUSE was the premature opening of the pressure relief valve.
ROOT CAUSE is unknown. It would require a detailed investigation on the cause of material failure.
Facility
- Application
- Hydrogen Transport And Distribution
- Sub-application
- LH2 tanker
- Hydrogen supply chain stage
- Hydrogen Transfer (No additional details provided)
- All components affected
- PRD
- Location type
- Open
- Location description
- Industrial Area
- Operational condition
- Pre-event occurrences
- The tanker had just terminated the transfer of LH2 to the customer's stationary tank.
- Description of the facility/unit/process/substances
- [Note of HIAD event validator: the PHMSA individual report has a wrong value of 126,000 cubic feet of LH2 delivered, but the correct value appears in the column dedicated to tank capacity]
Emergency & Consequences
- Number of injured persons
- 0
- Number of fatalities
- 0
- Environmental damage
- 0
- Currency
- US$
- Property loss (onsite)
- 2000
- Property loss (offsite)
- 0
- Post-event summary
- Over 300 local residents were evacuated, but no one was injured.
Approximately 30 kg of hydrogen were vented to the atmosphere. - Emergency action
- Both internal and external emergency operations of the refinery and outside services were very effective, and fires in both tanks and the dike were put out without any additional damage to other equipment in the tank farm.
Foam was used on the on the roof and surface cooling systems enabled protection of the tanks nearby.
Lesson Learnt
- Lesson Learnt
Premature activation of pressure relief devices is a regular cause of hydrogen release. It is usual due to ageing of the devices material, which could have several causes: wrong choice of the design materials, lack of inspection/maintenance, error in replacing sub-components, by not using the ones certified/specified.
Event Nature
- Release type
- gas
- Involved substances (% vol)
- H2 100%
- Released amount
- 20
- Actual pressure (MPa)
- 0.84
- Design pressure (MPa)
- 0.97
- Presumed ignition source
- Not reported
References
- Reference & weblink
Incident I-2000050966 of the US Pipeline and Hazardous Materials Safety Administration PHMSA: <br />
https://portal.phmsa.dot.gov/analytics/saw.dll?Portalpages&PortalPath=%… />
(accessed September 2024)Event description extracted from the UK database ICHEME in PDF<br />
ICHEME database is no longer available for purchase, but data can be download as PDF for free.<br />
https://www.icheme.org/knowledge/safety-centre/resources/accident-data/… />
(accessed October 2020)<br />Event nr 17608 of the French database ARIA<br />
https://www.aria.developpement-durable.gouv.fr/accident/17608/<br />
(accessed December 2025)
JRC assessment
- Sources categories
- PHMSA