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Clean Hydrogen Partnership

Fire in a refinery

Event

Event ID
979
Quality
Description

A 1-metre high flame developed on a pipe at the inlet of the hydrodesulphurisation unit of a refinery. The fire was caused by the leak of the pipe content, consisting of hydrogen and diesel.

The fire was spotted visually and was located 25 m above the ground. The personnel was evacuated. The operator did not extinguish the flame to avoid the risk to generate a hydrogen cloud.
The unit was gradually shut down with decompression to a site flare. The gas contained in the unit, feeding the leak, was progressively replaced by nitrogen. A preventive foam mat was put in place under the reactor to protect against a possible ground pool fire.

Event Initiating system
Classification of the physical effects
Hydrogen Release and Ignition
Nature of the consequences
fire
Macro-region
Europe
Country
France
Date
Component involved
flange (gasket)
Failure mode
rupture & ignition
Initiating cause
material degradation (over-stress)
Root CAUSE analysis

The INITIATING CAUSE was a leak on a bolted flange, and specifically the sealing gasket.
During the work of replacing the flanges, the operator observed the good flatness of the flanges but a deformation of the gasket. This deformation could have occurred due to the over-tightening of the flange during the last maintenance shutdown.
Moreover, at the time of the event, the desulphurisation unit was arriving at the end of the production cycle. A replacement of the catalyst had been planned at 1 month after the event. According to the operator, the loss of catalytic activity at the end of the cycle was compensated by an increase in the reaction temperature. This temperature increase, combined with the over-tightening of the flange, would be the cause of the leak.
Therefore, the ROOT CAUSE could be attributed to installation error, and/or to a human error. A possible shortcoming of the procedural instructions cannot be excluded.

Root causes
Date entry in HIAD
01/01/2024

Facility

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

hydrodesulphurisation unit, pipe

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

At the time of the event, the desulfurisation unit was at the end of its cycle with a replacement of the catalyst initially planned 1 month after the event.
Due to the normal losses in catalytic activity at the end of the cycle, the reaction temperature was usually increased i nespect to the prescribed value att the star tof the cycle.

Emergency & Consequences

Number of fatalities
0
Number of injured persons
0
Emergency action

The personnel was evacuated and a emergency operation room was installed.
The operator did not extinguish the flame in order not to generate a hydrogen cloud, which is highly explosive.
The unit was gradually shut down with decompression to a site flare. The gas contained in the unit, feeding the leak, was progressively replaced by nitrogen. A preventive foam mat was put in place under the reactor to protect against a possible ground pool fire

Lesson Learnt

Corrective Measures

After the fire, new bolts were used on the flange that leaked, and a controlled and incremental tightening of the assembly was executed throughout the restart of the unit.

In-depth data

Release type
Gas-liquid mixture
Involved substances (% vol)
H2,
diesel
Probable IGNITION SOURCE
Flame type

References

Sources categories
ARIA
Reference & weblink

Event description no. 53363 in the French database ARIA
https://www.aria.developpement-durable.gouv.fr/accident/53363_en/?lang=…
(accessed October 2021)