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Clean Hydrogen Partnership

Leakage from a valve in a heavy-oil hydro-desulphurisation unit

Event

Event ID
637
Quality
Description

The incident occurred during the start-up after a routine repair of the refinery's heavy oil hydrodesulphurisation system. A valve at the inlet pipe of a high-temperature and high-pressure separation tank ruptured, resulting in oil and gas spillage.
The valve was part of a pressure gauge instrument. It failed at the welding, due to hydrogen and hydrogen sulphide attack. Its weld material had an excessively hardness due to insufficient heat treatment after welding.

This conclusion was based on the findings of the post-incident investigation:
(i) The fracture was approximately in the middle of the butt weld between the valve body and the sealing.
(ii) On the inner circumference of the fracture surface, a small weld bevel remained, indicating incomplete penetration of the weld.
(iii) The hardness at the weld fracture was high.
(iv) Both the base metal and the welded metals were normal and in accordance with the specified standards.
(v) From a microstructural point of view, both the welded metal and the welding heat-affected zone of the damaged part were showing hardened structures such as those observed at the time of quenching. It points out at an insufficient post-welding heat treatment. There were no signs of decarburization with hydrogen.
(vi) Observations by scanning electron microscope revealed a pseudo-sheared fracture surface, characteristic of delayed fracture by hydrogen.

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
valve (weld)
Failure mode
rupture, no ignition
Initiating cause
material degradation (internal corrosion / erosion)
Root CAUSE analysis

The INITIATING CASUE was the failure of a welding between a pipe and a pressure gauge.
The ROOT CAUSE was shortcoming in the manufacturing of the weld.

Root causes
Date entry in HIAD
05/06/2027

Facility

Application
Petrochemical industry
Sub-application
Hydrodesulphurisation process
Hydrogen supply chain stage
All components affected

valve

Process temperature range [C]
High temperature (100°C to 500°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 unit was restarting after a routine repair.

Emergency & Consequences

Number of fatalities
0
Number of injured persons
3
Emergency action

After the leak, the device was immediately stopped with an emergency preocedure.
in two minutes, the decompression operation started and the system wnet down to atmospgeric pressure i n20 minutes, after which purging with nitrogen was started.

Lesson Learnt

Lesson Learnt

The incident highlights the complexity and the possible pitfalls of the relationship between suppliers of components and the plant operators.
From the point of the valve manufacturer (the supplier), this incident was the results of a manufacturing error, the failure to execute a weld respecting the specification. It could be as well be attributed to lack of quality control.
From the point of the user (the plant operator) the incident could be classified as a case of ‘force majeure’, because the user choose the supplier and specified the quality/application standard, but was not able to assess the quality of the weld and the compliances to the standard.

In-depth data

Release type
Gas-liquid mixture
Involved substances (% vol)
H2
heavy gas oil
Probable IGNITION SOURCE

References

Sources categories
JST
Reference & weblink

JST failures database (google translation):
https://www.shippai.org/fkd/include/fkd_showCase.php?id=CC0000164&text1…
(accessed Dec 2024)

Picture from the JST Failure Knowledge Database report CC0000164 reporting the location of the leak (google translation)

High Pressure Gas Accident Cases Database of the KHK (High Pressure Gas Safety Association):
https://www.khk.or.jp/public_information/incident_investigation/hpg_inc…
(accessed May 2025)