Skip to main content
Clean Hydrogen Partnership

Fire in the desulphurisation unit of a refinery

Event

Event ID
114
Quality
Description
The accident occurred in the de-sulphurisation unit, and specifically on a pipeline at 50 bar, for the recycling of the hydrogen (containing hydrogen sulphide impurities). The pipe failed due to corrosion and the released hydrogen which ignited. The unit was containing 4000 kg of hydrogen, but it is not known if all of it was released.
The unit was stopped, de-pressurised and put under nitrogen.
Following the accidents, all other pipeline were controlled looking for anomalies.
Event Initiating system
Classification of the physical effects
Hydrogen Release and Ignition
Nature of the consequences
Macro-region
Europe
Country
Germany
Date
Main component involved?
Pipe
How was it involved?
Rupture & Formation Of A Flammable H2-Air Mixture
Initiating cause
Material Degradation (Internal Corrosion / Erosion)
Root causes
Root CAUSE analysis
The INITIATING cause was the failure of a hydrogen pipe due to corrosion. The accident investigation discovered that the part of the 100 mm diameter pipe which failed had a residual thickness of 2 instead of the nominal 6.3 mm.

The ARIA report (see references) does not mention any root cause, but judging by the deep corrosion, a lack of adequate inspection/maintenance can be postulated.

Facility

Application
Petrochemical Industry
Sub-application
Hydrodesulphurisation process
Hydrogen supply chain stage
All components affected
hydrogen recycling pipeline
Location type
Open
Location description
Industrial Area
Operational condition
Pre-event occurrences
Due to inner corrosion of a 100mm (DIN 100) pipe the wall thickness was reduced from 6.3 mm to 2 mm.

Emergency & Consequences

Number of injured persons
1
Number of fatalities
0
Environmental damage
0
Currency
Euro
Property loss (onsite)
2000000
Property loss (offsite)
1500
Post-event summary
1 injury, no fatality. The injury was due to the fact that an employee who had just left the plant was startled by the bang of the explosion and suffered a sprained ligament in a sudden movement.

The material damage were estimated around 3 millions et 3 000 DM (ZEMA reports 2 Meuros + offside loss due to vehicle pollution in the employee parking lot).
Emergency action
Unknown, probably none.

Lesson Learnt

Lesson Learnt
. Nevertheless, the fact that the pipe failed due to internal corrosion indicate a lack of fit-for-purpose inspection, able to detect material degradation on limited sections.
Corrective Measures

Following the accidents, all other pipeline were controlled looking for anomalies. Nothing is known on measures aiming at preventing the occurrence of similar cases in the future.

The sources do not report the

Event Nature

Release type
gas
Involved substances (% vol)
H2,
H2S (impurities)
Released amount
4000
Actual pressure (MPa)
5
Design pressure (MPa)
5
Presumed ignition source
Not reported

References

Reference & weblink

Event from German database ZEMA<br />
https://www.infosis.uba.de/index.php/de/site/2854/zema/index/3170.html<… />
(accessed December 2024)

Event description in the French database ARIA<br />
https://www.aria.developpement-durable.gouv.fr/accident/10347/<br />
(accessed October 2020)<br />

JRC assessment