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Clean Hydrogen Partnership

Hydrogen fire at a chemical plant

Event

Event ID
919
Quality
Description

The fire broke out in the acid etching tank of the ferric chloride manufacturing unit of a SEVESO-classified chemical plant. In this tank, the attack reaction of the iron metal with hydrochloric acid in solution is carried out, which results in ferrous chloride and hydrogen. The hydrogen generated is swept away by a large supply air fan to maintain the gaseous sky of the tank below the LFL.

A few days after the accident, the operator opened and analysed the tank to determine the origin of the fire.
According to the ARIA report, the start of the fire was caused by a slow combustion of hydrogen, initiated during the loading of metal. Despite the air circulation, hydrogen accumulated at the bottom of the tank due to its overfilling. The fire then spread outside the tank through the roof opening caused by the degradation of the hydrogen detector and by melting the blast doors. The fire was then alimented by the plastic components of the equipment and the surrounding piping, as well as by the oil from the hydraulic pistons of the roof door of the tank.
Event Initiating system
Classification of the physical effects
Hydrogen Release and Ignition
Nature of the consequences
Fire (No additional details provided)
Macro-region
Europe
Country
France
Date
Root causes
Root CAUSE analysis
The INITIATING cause was the overloading of the tank, which allowed accumulation of hydrogen despite the air circulation system.

Considering the corrective actions described in the ARIA report, the root cause was probably inadequate safety design and operation.

Facility

Application
Chemical Industry
Sub-application
Inorganic chemicals products
Hydrogen supply chain stage
All components affected
reaction tank, production of iron chloride (FeCl2)
Location type
Semiconfined
Location description
Industrial Area
Operational condition
Description of the facility/unit/process/substances
DESCRIPTION OF THE PROCESS
The stoichiometric reaction at the basis of the process is: Fe + 2 HCl → FeCl2 + H2

Emergency & Consequences

Number of injured persons
0
Number of fatalities
0
Post-event summary
No injuries. The unit restarted 6 months after the accident.
Damage to the tank upper parts, hydrogen detector and doors

Lesson Learnt

Lesson Learnt

The accident suggests that the operative procedure related to the loading of the materials and the preventive measures (hydrogen detection) were inadequate.

Corrective Measures

According to the ARIA report (see references), the operator updates the risk analysis of this unit and reinforces controls on the level of scrap metal in the tank and analyses of hydrochloric acid.
It also added safety features on the low air sweep rate and high temperature in the tank and lowers the alarm threshold of the hydrogen analyser.

Event Nature

Release type
gas
Involved substances (% vol)
H2 100%
Presumed ignition source
Not reported
Flame type
Other

References

Reference & weblink

Event description in the French database ARIA<br />
https://www.aria.developpement-durable.gouv.fr/accident/49915/<br />
(accessed September 2020)

JRC assessment