Event
- Event ID
- 50
- Quality
- Description
The incident occurred at a heat exchanger involving gas-product mixture. The source does not specify the process, with as main component a furnace, probably a hydrodesulphurisation reactor. Due to a leak in the pipe, the mixture was released and formed a vapour cloud. Following ignition, a fire developed at the leaking point.
The plant fire brigade was alerted and laid a foam carpet over the entire area. The furnace system, the as circulation compressor and the injection pump were switched off in an emergency. The emergency expansion valve was opened and nitrogen was fed into the circuit.
No injuries, only equipment damage.- Event Initiating system
- Classification of the physical effects
- Hydrogen Release and Ignition
- Nature of the consequences
- Macro-region
- Europe
- Country
- Germany
- Date
- Component involved
- heat exchanger (pipe)
- Failure mode
- leak & ignition
- Initiating cause
- material degradation (generic)
- Root CAUSE analysis
A material failure was suspected to as INITIATING CAUSE of the leak. Nothing is known on the operative aspects of the event.
- Root causes
- Unknown
- Date entry in HIAD
- 28/02/2009
Facility
- Application
- Petrochemical industry
- Sub-application
- Hydrodesulphurisation process
- Hydrogen supply chain stage
- All components affected
pipe, heat exchangeer
- Process temperature range [C]
- High temperature (100°C to 500°C)
- Location type
- Unknown
- Location
- industrial area
- Operational condition
Emergency & Consequences
- Number of fatalities
- 0
- Number of injured persons
- 0
- Currency
- Euro
- Property loss (onsite)
- 500.000
- Post-event summary
There were no personal injuries. The property damage due to partial destruction of equipment as a result of the fire amounted to 500,000 euros. There was no environmental damage.
- Emergency action
The plant fire brigade was alerted and laid a foam carpet over the entire area. As safety measures, the furnace system, the as circulation compressor and the injection pump were switched off in an emergency. The emergency expansion valve was opened and nitrogen was fed into the circuit. No intervention outside the plant was required.
Lesson Learnt
- Corrective Measures
A revision and expansion of the wall thickness measuring programs, to be able to detect on time critical loos of resistance and percent loss of confinement.
In-depth data
- Release type
- gas mixture
- Involved substances (% vol)
- H2S 10 kg
H2 100 kg
Hydrocarbons 1200 kg - Probable IGNITION SOURCE
- Explosion type
References
- Sources categories
- ZEMA
- Reference & weblink
Event from German database ZEMA
https://www.infosis.uba.de/index.php/de/site/12981/zema/index/2869.html
(accessed December 2023)