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Clean Hydrogen Partnership

Explosion of a chlorine distillate tank of a chemical plant

Event

Event ID
864
Quality
Description
The pressure vessel in a chlorine separation system exploded after the corrosion of the steel process equipment allowed chlorine and hydrogen to mix and form a volatile mixture.
The chlorine receiving tank ruptured violently into five pieces (three large ones and two smaller) causing considerable damage to nearby equipment. The appearance of the pieces confirmed that a the tank had failed by a rapid brittle fracture. The large size of the pieces and the degree of external damage implied a vapour-phase explosion rather than a more energetic liquid-explosion. No organic material traces were detected so that hydrogen became the only possible responsible of explosion.
A possible source was found in the corrosion of the steel packing below the feed point of the distillation column. It was not possible to identify a credible ignition source as in most previous chlorine-hydrogen explosions.
Event Initiating system
Classification of the physical effects
Hydrogen Release and Ignition
Nature of the consequences
Macro-region
North America
Country
United States
Date
Main component involved?
Chemical Storage Tank
How was it involved?
Internal Explosion (H2-Air Mixture)
Initiating cause
Accidental Hydrogen Formation
Root causes
Root CAUSE analysis
The INITATING CAUSE was the generation and ignition of an explosive atmosphere in the chlorine tank.

The composition of this explosive atmosphere could only be guessed. From the analysis of the explosion debris, a vapour phase explosion appeared more plausible than a liquid one.
By exclusion, the culprit could be found in the generation of hydrogen from corrosion of steel. if this was the case, lack of inspection could be the ROOT CAUSE.

Facility

Application
Chemical Industry
Sub-application
Chlorine production
Hydrogen supply chain stage
All components affected
chlorine tank, chlorine distillation column
Location type
Unknown
Location description
Industrial Area
Operational condition

Emergency & Consequences

Number of injured persons
0
Number of fatalities
0

Event Nature

Release type
gas mixture
Involved substances (% vol)
H2,
Cl2
Presumed ignition source
Not reported

References

Reference & weblink

Loss Prevention, Vol.7 (1973), pp. 104-107. American Institute of Chemical Engineers (AIChE) .

JRC assessment