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Clean Hydrogen Partnership

Release and ignition when starting operation of a new hydrogen line

Event

Event ID
154
Quality
Description

The event occurred on a hydrogen pipeline supplying a refinery. The location was at the fence to the refinery, when putting in operation a new section of the pipeline.
Operators had begun work to purge a new hydrogen 6" line into service. The required pre-work had been completed, and one operator was at the valve station preparing to slowly let hydrogen into the line, from an adjacent 8" line, which was already in service.
The second operator was at the valve station vent, to monitor purge gas flow and purity. The second operator mistakenly thought that the purge had already started and thought that there was insufficient purge flow at the vent. He decided to open the isolation valve to the pressurized 8" line at his end. By opening the valve, he caused a high-volume flow of hydrogen through the adjacent vent pipe, which ignited.
The second operator received burns to his hands and face. A company truck was destroyed, and other vehicles were damaged.

Event Initiating system
Classification of the physical effects
Hydrogen Release and Ignition
Nature of the consequences
Macro-region
North America
Country
United States
Date
Component involved
pipeline (generic)
Failure mode
erroneous release & ignition
Initiating cause
wrong operation
Root CAUSE analysis

INITIATING CAUSE is the erroneous injection of hydrogen high flow into the vent pipe.
The ROOT CAUSE relates to the wrong execution of a procedure, and probably also to lack of clarity of it. Moreover, failing in recognising the hazards related to actions performed by two workers who were depending on mutual understanding, caused the lack of automatic measures preventing misunderstanding and perceptive assumptions.

Root causes
Date entry in HIAD
01/06/2024

Facility

Application
Hydrogen transport and distribution
Sub-application
pipeline
Hydrogen supply chain stage
All components affected

pipeline, vent

Process temperature range [C]
ambient temperature (-50°C to +50°C)
Process pressure range [MPa]
medium to high pressure (10 to 50 MPa)
Location type
Open
Location
industrial area
Operational condition
Pre-event occurrences

The operation which brought to the incident consisted in preparing a new pipeline for its first operation.

Emergency & Consequences

Number of fatalities
0
Number of injured persons
1
Currency
US$
Property loss (onsite)
110.000
Post-event summary

An employee received burns to hands and face.
A company truck was destroyed and 10 other vehicles were damaged.

Emergency action

no evacuation. The area was declared safe after 1/2 hour

Lesson Learnt

Lesson Learnt

In this accident, two employees at different location were supposed to execute a series of operations depending of each-others. It went wrong because of the assumption of one of the two, on the actions taken by the other.
The incident has been attributed to a failure to follow the procedure. However, this error could have been minimise by:
(1) Ensuring the availability of proper communication means.
(2) Introduce automatic safeguards, so that the one employee could not process at a next step without cling the previous step.

In-depth data

Release type
gas
Involved substances (% vol)
H2 100%
Release temperature [°C]
25
Release pressure [MPa]
10
Probable IGNITION SOURCE
Explosion type

References

Sources categories
PHMSA
Reference & weblink

US Pipeline and Hazardous Materials Safety Administration PHMSA:
https://www.phmsa.dot.gov/data-and-statistics/pipeline/distribution-tra…
(accessed September 2024)