Skip to main content
Clean Hydrogen Partnership

Release and fire from a hydrogen pipeline

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