Event
- Event ID
- 885
- Quality
- Description
- A release of compressed hydrogen and subsequent fire occurred during the transportation of a CGH2 trailer by means of a truck tractor. The tube trailer module contained 25 fully wrapped carbon filler reinforced aluminium-lined tubes, 24 of which were fully loaded with 240 kilograms of compressed hydrogen.
The pressure relief devices actuated on 12 of the tubes and released about 120 kilograms of hydrogen that was likely consumed in the fire.
The Fire Department estimated about 1,400 to 2,000 people were evacuated from the adjacent business district and a nearby residential area. Equipment damages were estimated at $175,000.
The National Transportation Safety Board (NTSB) investigated the event and concluded that the probable cause were
(i) the requalification technician’s installation of an incorrectly rated pressure relief device in cylinder No. 14, which actuated during normal transportation and released high-pressure hydrogen,
(ii) The tube trailer module assembly contractor’s failure to sufficiently tighten compression fittings on the pressure relief device vent lines that disassembled under the pressure of escaping gas allowing a fire to develop inside the module and impinge on adjacent cylinders.
(iii) Contributing to the incident was a lack of a requirement for requalification inspectors to verify the pressure relief device pressure rating and to inspect for vent line assembly securement. - Event Initiating system
- Classification of the physical effects
- Hydrogen Release and Ignition
- Nature of the consequences
- Fire (No additional details provided)
- Macro-region
- North America
- Country
- United States
- Date
- Main component involved?
- Tprd
- How was it involved?
- Premature Activation
- Initiating cause
- Wrong Component
- Root causes
- Root CAUSE analysis
- INITIATING cause of the event was the opening of a incorrectly rated pressure relief device, which actuated during normal transportation and released high-pressure hydrogen.
ROOT CAUSE was probably the requalification technician’s installation of the incorrectly device and the tube trailer module assembly contractor’s failure to sufficiently tighten compression fittings.
CONTRIBUTING CAUSE was a lack of a requirement for requalification inspectors.
Facility
- Application
- Hydrogen Transport And Distribution
- Sub-application
- CGH2 tube trailer
- Hydrogen supply chain stage
- Hydrogen Transport (No additional details provided)
- All components affected
- compressed hydrogen tube trailer, 24 tubes, each 240 kg H2
- Location type
- Open
- Operational condition
- Pre-event occurrences
- After delivering a similar tube trailer module that morning, the driver picked up the incident tube trailer module from the hydrogen filling station and conducted a pre-trip inspection. The driver connected the module to the filling stanchion and found that although the cylinders were pressurized to 7,855 psig (temperature-corrected loading pressure, 540 bar), the pressure had reduced to 7,300 psig with cooling (503 bar). The driver concluded the module was already full and then proceeded with his trip to deliver it to a FCEV refuelling station.
- Description of the facility/unit/process/substances
- TECHNCIAL SPECIFICATIONS OF TtHE TUBES AND MODULE
The CT-250 tube trailer module consisted of 25 horizontal neck-mounted Type 3 model carbon fibre composite cylinders arranged in a 5 x 5 array.
Each cylinder had a nominal capacity of contained 10 kg with a hydrogen capacity of 250 kg for the entire module.
The tubes were certified according to the permit DOT-SP 14576, with these design criteria and operational requirements:
Service pressure limited to 7,500 psig at 70℉ (517 bar at 20C) .
Test pressure of 12,500 psig (862 bar).
Minimum cylinder burst pressure = 25,500 psig (1758 bar), or a safety factor of 3.4.
Cylinder service life = 15 years. The tube trailer cylinders had been in service for 5 years, thus they had 10 years of remaining authorized service life.
Each cylinder requalified once every 5 years using a hydraulic or pneumatic pressure proof test.
Cylinders manifolded in accordance with the requirements of Title 49 Code of Federal Regulations (CFR) 173.301(g).
The gas cylinders were equipped with PRDs at each end, giving a total of 50 PRDs installed on the module. They were CG-5 type devices, i.e. consisting in a combination of rupture disk and fusible plug.
Emergency & Consequences
- Number of injured persons
- 0
- Number of fatalities
- 0
- Currency
- US$
- Property loss (onsite)
- 175000
- Post-event summary
- The Fire Department estimated about 1,400 to 2,000 people were evacuated from the adjacent business district and a nearby residential area.
Equipment damages were estimated at $175,000. - Official legal action
- The NTSB has made safety recommendations to the Pipeline and Hazardous Materials Safety Administration; the US Department of Energy, Pacific Northwest National Laboratory; and the Compressed Gas Association.
Lesson Learnt
- Lesson Learnt
Findings of the NTSB investigation:
1. Greater first responder training and awareness about hydrogen tube trailer modules transported within their jurisdiction could have helped the first responders to initially respond to this incident more effectively, efficiently, and safely.
2. Although there is ample generic hazard information for compressed hydrogen and vehicle fuel systems, the available guidance lacks critical hazard recognition and firefighting information specific to fuel cell electric vehicle fuelling infrastructure and containers currently used for the bulk transportation of compressed hydrogen.
3. The generic guidance for flammable gases contained in the US Emergency Response Guidebook, Guide 115, does not adequately describe unique hazards associated with compressed hydrogen or best response actions for public safety personnel.
4. None of the incident tube trailer cylinders lost mechanical integrity, and they did not contribute to the cause or perpetuation of the incident.
5. The hydrogen release most likely initiated because a pressure relief device with the wrong pressure rating was installed on cylinder No. 14 and actuated under normal working pressure loads.
6. The hydrogen ignited during the forced separation of the cylinder No. 14 pressure relief device assembly from the cylinder.
7. Although the other cylinder pressure relief devices in the tube trailer module were actuated because of fire exposure, the cylinder No. 14 pressure relief device actuated before the fire began.
8. Had the requalification personnel inspected each vent line compression fitting for tightness, the propagation of the fire to the adjacent hydrogen cylinders may have been avoided.
9. The vent line compression fittings that disassembled during venting were not properly installed at the time the tube trailer module was fabricated and should have been noticed and repaired during the requalification inspection.
10. The lack of a Pipeline and Hazardous Materials Safety Administration special permit and regulatory requirements for verifying that pressure relief devices used on cylinders actuate at the correct pressure and venting equipment has been properly assembled and secured increases the risk of uncontrolled fires on flammable gas tube trailers.
11. The lack of vent system design requirements that consider factors such as the force of venting gas and construction material may leave vent systems for cylinders and tube trailers vulnerable to unexpected failure during an incident.
12. The lack of noticeable marking or other visual indicators, unique design features, and unique model numbering to readily identify pressure relief devices intended for different applications, made them easy to confuse and did not avert the requalification technician from installing four wrong pressure relief devices on the incident tube trailer module.
Event Nature
- Release type
- gas
- Involved substances (% vol)
- H2 100%
- Released amount
- 120
- Actual pressure (MPa)
- 51.7
- Design pressure (MPa)
- 50.3
- Presumed ignition source
- Not reported
- Ignition delay
- 0
- Flame type
- Jet flame
References
- Reference & weblink
NTSB report on Diamond Bar HZM1902:<br />
https://www.ntsb.gov/investigations/Pages/HMD18FR001.aspx<br />
(accessed Dec 2022)<br />
`Incident E-2018030180 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
- NTSB