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Clean Hydrogen Partnership

leak from a dispenser of a mobile HRS

Event

Event ID
1208
Quality
Description

The accident occurred at a mobile hydrogen station during a fuelling test for a fuel cell vehicle. The day before, the gas detector in the dispenser detected a leak and the equipment was shut down. With a mobile detector and a helium leak test, the leak was found coming from the emergency shutdown valve of the dispenser. The valve manufacturer replaced the O-ring. The day after during a fuelling test, a leak was detected again. The leakage point was and found on the lower part of the emergency disconnect coupler on the fuelling nozzle side of the fuelling hose was leaking.

Event Initiating system
Classification of the physical effects
Unignited Hydrogen Release
Nature of the consequences
leak no ignition
Macro-region
Asia
Country
Japan
Date
Component involved
dispenser (gasket)
Failure mode
rupture, no ignition
Initiating cause
material degradation (generic)
Root CAUSE analysis

The INITIATING CAUSE was a small release of hydrogen from a damaged O-ring.

The ROOT CAUSE could not be identified with certainty and was believed to be one of the following:
1. The O-ring of the coupling valve was damaged during the previous work of dismantling and remounting of the emergency valve.
2. The sealing of the coupling was poor and during fuelling the application of a force on the coupling could have caused the movement and the damage of the O-ring.

Root causes
Date entry in HIAD
30/09/2025

Facility

Application
Hydrogen refuelling station
Sub-application
HRS 70 MPa
Hydrogen supply chain stage
All components affected

emergency valve, dispenser

Process temperature range [C]
ambient temperature (-50°C to +50°C)
Process pressure range [MPa]
high pressure (above 50 MPa)
Location type
Confined
Location
unknown
Operational condition
Pre-event occurrences

10 days before, a safety inspection was terminated and the operation restarted 3 days after.
10 vehicles had already been refuelled, when the first leak was detected during the refuelling of the 4th FCV of the day.

Description of the facility/unit/process/substances

DESCRIPTION OF THE FACILITY
High-Pressure Gas Production Capacity: 12,366 m3/day
Normal Operating Pressure: 70.0 MPa
Normal Operating Temperature: -40 to 40°C

The location is classified as CONFINED, because the leaking valve was installed in an enclosed section of the dispenser.

Emergency & Consequences

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

No personal injury, no property damage.
Only a very small release of hydrogen.

Emergency action

1. September 25: Completed inspection
2. September 28: Start of operation
3. October 5: During hydrogen fueling to the 4th vehicle (10th since the start of operation) (Temperature: -37°C, Pressure: 63 MPa), the hydrogen gas leak detection alarm device inside the dispenser activated. After detecting the leak, the hydrogen inside the piping was automatically depressurized and released from the vent. The leakage point was investigated using a portable hydrogen gas detector, but it was not identified. (This is a separate hydrogen leakage accident from the one mentioned above.)
4. October 6: Under the supervision of the equipment manufacturer, the leakage point was thoroughly investigated, and it was confirmed that the shut-off valve inside the dispenser was leaking.
5. October 6: The O-ring of the shut-off valve inside the dispenser was replaced, and during the hydrogen fueling test to a fuel cell vehicle (Temperature: -37°C, Pressure: 55 MPa), the hydrogen gas leak detection alarm device inside the dispenser activated. The leakage point was investigated using a portable hydrogen gas detector, and it was confirmed that the lower part of the emergency disconnect coupler on the fueling nozzle side of the fueling hose was leaking.

Lesson Learnt

Lesson Learnt

This event is classified as incident because of the hydrogen release and the resources spent in improving the situation; however, considering that the safety system functioned as designed and that the leak was very small, system it is borderline with a near-miss classification.
The KHK report indicated that only at the lowest temperature of -40°C, the leak rate exceeded \the max allowed rate (2.1 10-5 Pa m3/s, instead of a max of 1.0 10-5 Pa m3/s).

The following general conclusion van be drown (modified in respect to the original KHK report):
(1) Leak testing is essential to detect any leaks before fuelling. However, as demonstrated by a similar incident (see HIAD_1207), they are not always effective in detecting loss of confinement if the conditions under tests differ too much from those experienced during refuelling. Leaking rate measured at room temperature were according to specification, while at -40 C resulted above maximum allowed.
(2) It is necessary to consider the whole assembly of the emergency disconnect coupler, the hose and fuelling nozzle, and the external force acting on them, to prevent that any force not considered in the design from being applied to the emergency disconnect coupler.
(3) An effective seal management is crucial in high-pressure gas equipment. This implies the correct choice and management of O-rings, with sealing power also at lower temperature and in a wide range of dynamic pressure. Moreover, correct control and care of the seal surface is important during the installation and replacement.

Corrective Measures

The facility has taken the following countermeasures to prevent a recurrence of the accident:
1. Changed the manufacturer of the emergency disconnect coupler and high-pressure hose.
2. The manufacturer created a checklist to prevent damage to the O-ring during assembly.
3. The manufacturer introduced a new helium leak test at 96.3 MPa and -40°C before product shipment.

In-depth data

Release type
gas
Involved substances (% vol)
H2 100%
Released amount (kg)
0
Release temperature [°C]
25
Release pressure [MPa]
82
Probable IGNITION SOURCE

References

Sources categories
KHK
Reference & weblink

KHK accidentl database, incident 2015-363:
https://www.khk.or.jp/public_information/incident_investigation/hpg_inc…
(accessed august 2024)

Translated version in English (by GPT@JRC)