Event
- Event ID
- 1059
- Quality
- Description
- Early in the morning of (3:00 AM), the personnel on one of the companies on site reported a potential pipeline leak just south of the valve station. The potential leak was discovered due to bubbling water in the ditch. No visible hydrocarbon sheen was noted, indicating a probable non-hydrocarbon gas leak. Later in the morning, the personnel tested their area gas pipelines and determined that their company was not the source of the leak.
Later on the same day, another company tested their pipelines and determined that their hydrogen pipeline was the source of the leak. The line was de-pressurised and this caused the bubbling in the ditch to subside and eventually stop at noon.
The SCADA (Supervisory Control and Data Acquisition) system was functional and operating under normal conditions at the time of the incident. The pipeline pressure drop due to the failure was so small that it did not indicate on the control room SCADA screen at the pressure point adjacent to the leak area.
The leak resulted in 1.7 mmscf (ca. 4 t) of hydrogen was released to atmosphere, and the re-routing of the affected section lasted more than 6 months, the repair was expected after one year. - 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?
- Pipeline
- How was it involved?
- Leak & Formation Of A Flammable H2-Air Mixture
- Initiating cause
- Material Degradation (External Corrosion)
- Root causes
- Root CAUSE analysis
- The pipeline section was in water. The loss of containment has been attributed to internal corrosion of pipeline materials.
The difficulty in accessing the location of the release could hint to a shortcoming of the design of the pipeline or to an error in the installation.
Facility
- Application
- Hydrogen Transport And Distribution
- Sub-application
- Pipeline
- Hydrogen supply chain stage
- Hydrogen Transport (No additional details provided)
- All components affected
- underground pipepine
- Location type
- Underground
- Operational condition
- Description of the facility/unit/process/substances
- DESCRIPTION OF THE FACILITY
The pipeline had been produced and installed in 1993, was made of carbon steel API 5L X42, with an epoxy coating.
Pipeline diameter = 10 inch (0.254 m), wall thickness = 0.25 in (6.4 mm)
It was at 5 metre depth.
Emergency & Consequences
- Number of injured persons
- 0
- Number of fatalities
- 0
- Environmental damage
- 0
- Currency
- US$
- Property loss (onsite)
- 2104000
- Post-event summary
- No consequence for persons or environment. Maintenance costs incurred due to the partial replacement of the line.
Event Nature
- Release type
- gas
- Involved substances (% vol)
- H2 100%
- Released amount
- 4000 kg
- Actual pressure (MPa)
- 1.8
- Design pressure (MPa)
- 2.7
- Presumed ignition source
- No ignition
References
- Reference & weblink
US Pipeline and Hazardous Materials Safety Administration PHMSA: <br />
https://www.phmsa.dot.gov/safety-reports/pipeline-failure-investigation…
JRC assessment
- Sources categories
- PHMSA