Skip to main content
Clean Hydrogen Partnership

Release of a light hydrocarbon gas mixture in a chemical product plant

Event

Event ID
101
Quality
Description
During the start-up operation (phase) of a cryogenic unit, a separator exploded, releasing ethane, ethylene, methane and hydrogen. The bursting of a tank was caused by a 1600 mm long incipient crack which had been formed at the inside of the tank along a weld line (a ferritic basis metal had been welded with an austenitic weld metal).
The hydrogen induced incipient crack (cracking) was caused by the alternating load during start-up and shut-down phases in the course of the operating time.
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
Germany
Date
Main component involved?
Heat Exchanger (Cold Box)
How was it involved?
Rupture & Formation Of A Flammable H2-Hc-Air Mixture
Root causes
Root CAUSE analysis
The INITIATING CAUSE was hydrogen induced cracking originated by the geometric form variation and the resulting plastic deformation in the area of a longitudinal seam weld. This incipient cracking was favoured by the high tensile (strength) austenitic CrNiMnW weld metal with its particularly accentuated martensitic composite (mixed) zone (area) along the transition between weld metal and basis metal and was also favoured by its physical characteristics which differ strongly from the basis metal.

Possible ROOT CAUSES could two contributions: (i) a wrong execution of the welding (wrong choice of materials, inadequate themral management), aand a a lack of inspection / maintenance.

Facility

Application
Petrochemical Industry
Sub-application
distillation / gas separation
Hydrogen supply chain stage
All components affected
cryogenic unit, separator, weld
Location type
Open
Location description
Industrial Area
Operational condition
Pre-event occurrences
At the moment of the release, the plant was in in the start-up phase of a cryogenic unit.
Description of the facility/unit/process/substances
DESCRIPTION OF THE PROCESS
A cryogenic separator in a refinery has the role to separeate heavier components (like propane, butane, and natural gas liquids - NGLs) to liquefy while lighter ones (like methane or hydrogen) remain gaseous,based on the difference between their boiling points. The process involves compressing, and cooling the gas, then flashing (a sudden pressure drop) to create liquid/vapor phases, followed by fractionation in columns where each component is boiled off sequentially.

Emergency & Consequences

Number of injured persons
0
Number of fatalities
0
Currency
Euros
Property loss (onsite)
1500000
Post-event summary
Large material damages (losses) due to the destruction of plant parts, estimated as approx. 1.5 million ECU. No persons were injured.
The neighbourhood was strongly disturbed by the noise caused by the bursting of the tank and the consequent flaring activities.
Emergency action
The actions are not reported. Time of the fire also unknown.
Since this was a case of immediate release and ignition, It is very probable that the fire was left extinguish, possibly by cooling the tubes, before starting to intervene to recover the vehicles.

Event Nature

Release type
gas mixture
Involved substances (% vol)
C2H6
C2H4
CH4
H2
Presumed ignition source
Not reported

References

Reference & weblink

Event description in the European database eMARS<br />
https://emars.jrc.ec.europa.eu/en/eMARS/accident/view/2f7bf3bd-14f6-f0e… />
(accessed October 2020)<br />

Event description in the French database ARIA<br />
https://www.aria.developpement-durable.gouv.fr/accident/14666/<br />
(accessed October 2020)<br />

JRC assessment