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Clean Hydrogen Partnership

Release of chemical substances (including hydrogen) from a chemicals production plant

Event

Event ID
924
Quality
Description
The event was initiated by the burst of a rupture disc on a reactor during a hydrogenation process. The hydrogenation reaction occurs under pressure in a tank containing 3,000 l of a mixture of ethanol (a flammable and toxic solvent), red hair dye, a catalyst (palladium on carbon) and hydrogen.
As a result of the disc rupture and the following tank decompression, part of the tank content was expelled and landed on the roof of the building.

The emergency action consisted in stopping the supply of hydrogen and to purge the tank with nitrogen.

The internal investigation showed that the disc’s maximum operating pressure was 2.83 bar, rather than assumed 3.7 bar. The hydrogenation process operates at pressures up to 2.9 bar.

Following a reference change, the rupture disc supplier did not validate the characteristics of the new model sold to the operator, who had not been informed of the reference change.

A possible additional contribution to the event could have been the 10-year inspection of the seal and the graphite performed a month earlier, which may have weakened the disc.
Event Initiating system
Classification of the physical effects
Unignited Hydrogen Release
Nature of the consequences
Leak No Ignition (No additional details provided)
Macro-region
Europe
Country
France
Date
Main component involved?
Prd (Burst Disc)
How was it involved?
Premature Activation
Initiating cause
Wrong Component
Root causes
Root CAUSE analysis
The INITIATING cause was the premature burst of the rupture disc under nominal working pressure condition.

The root cause was the delivery by the contractor of a disc with different characteristics, without informing the plant operator.

A contributing cause could be the absence of an independent control of components by the operator.

Facility

Application
Chemical Industry
Sub-application
Inorganic chemicals products
Hydrogen supply chain stage
All components affected
burst disc
Location type
Confined
Location description
Industrial Area
Operational condition
Pre-event occurrences
A maintenance intervention performed one month before the event may have damaged or weakened the disc.

Emergency & Consequences

Number of injured persons
0
Number of fatalities
0
Post-event summary
411 kg ethanol et 23 kg of reaction products are dispersed mainly to the ground, part of the ethanol is dispersed in the atmosphere.

Lesson Learnt

Lesson Learnt

Despite the corrective measures implemented, it remains unclear how these could guarantee avoiding the recurrence of the same accident, in absence of an internal procedure aiming at regularly checking subcontractors deliveries.
Corrective Measures

According to the ARIA report (see references), following the accident, the operator reviewed the reactor qualification documents, including the max. operative pressure of the rupture discs. All the discs in place on other reactors were checked and the discs below specifications were replaced.
The maintenance personnel were made aware of the importance of the proper assembly of rupture discs on the reactors.

Event Nature

Release type
Gas-liquid mixture
Involved substances (% vol)
H2,
C2H6O,
dye
Actual pressure (MPa)
0.29
Design pressure (MPa)
0.29
Presumed ignition source
No ignition

References

Reference & weblink

Event description in the French database ARIA<br />
https://www.aria.developpement-durable.gouv.fr/accident/47182/<br />
(accessed September 2020)

JRC assessment