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Clean Hydrogen Partnership

Hydrogen/methane release at a gas booster of a pipeline

Event

Event ID
1085
Quality
Description

The incident involves a gas booster provided by a manufacturer. This device is used in the experimental platform of the project to raise the pressure in pipelines from 60 to 80 barg (from 6 to 8 MPa), allowing the gas to flow in a close loop. After 5 weeks of operation, a critical gas leakage through the vent port was detected.

At the moment of the incident, the compressor was working with a mixture of hydrogen and methane (H2/CH4 blend 20/80 %v/%v). The booster was sent to the manufacturer for inspection and reparation. Severe damage in the seals of the vent port was found. Besides, the gas barrels were scratched. Both seals and gas barrels had to be replaced.

The reason for this failure is unclear and the manufacturer cannot provide a real solution. The booster must have been able to perform 2,000,000 cycles without premature deterioration of the seals, but failed after 500,000 cycles.

No consequences on people or property. Minor damage of environment because of release of greenhouse gases (methane)

Event Initiating system
Classification of the physical effects
Unignited Hydrogen Release
Nature of the consequences
leak no ignition
Macro-region
Europe
Country
Spain
Date
Component involved
compressor / booster / pump (seal)
Failure mode
rupture, no ignition
Initiating cause
material degradation (generic)
Root CAUSE analysis

The INITIATING cause of the release was the was the severe damage of the seals of the vent port, which occurred during operation.
The manufacturer could not provide a root cause of the damage.
The operator concluded that a manufacturing defect seems the most logical explanation for the failure. They also suspect that the manufacturer is reluctant to admit it, because the spare parts used after the reparation were the same as those originally installed.

Root causes
Date entry in HIAD
01/07/2024

Facility

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

booster

Process temperature range [C]
ambient temperature (-50°C to +50°C)
Process pressure range [MPa]
medium pressure (2 to 10 MPa)
Location type
Open
Location
unknown
Operational condition
Pre-event occurrences

The device was new and had not been used previously. The event occurred during a planned operation (the first experimental campaign).

Emergency & Consequences

Number of fatalities
0
Number of injured persons
0
Post-event summary

No consequences, no damage. 0.5 kg of H2 and 15.7 kg of CH4 released

Lesson Learnt

Corrective Measures

As first corrective action, the seals and the gas barrels were replaced by the manufacturer.

The facility operator is considering changing the booster manufacturer, for the following reasons:
(1) It appeared that the booster is not suitable for working with hydrogen / methane blends, especially in closed setups, because they are not tight enough.
(2) Manufacturer after-sale service was not reliable. Also, they did not provide sufficient information on the cause of failure.
(3) The communication with the manufacturer is in general difficult, slow and requests are often ignored.
(4) Manufacturer factory is in the UK, and since the BREXIT supplies are stopped at the custom too long, which makes finding quick solutions even more difficult.

A general conclusion could be that problems related to suppliers - projects relationship can generate safety issues.

In-depth data

Release type
gas mixture
Involved substances (% vol)
H2 20%
CH4 80%
Released amount (kg)
0.5
Release temperature [°C]
25
Release pressure [MPa]
8
Probable IGNITION SOURCE

References

Sources categories
Investigation report
Reference & weblink

Provided to JRC by the operator of the facility (confidential)