Event
- Event ID
- 223
- Quality
- Description
The event occurred in the ammonia production unit.
A minor leak had been detected in a flange on the piping of the ammonia synthesis loop (operating at 250 bar). The company called a specialized external contractor to perform an on-stream repair of the valve. This solution was chosen because of the limited extents of the leakage and the economic costs and efforts associated to a shut-down of a very complex system.The on-stream repair consisted in: (1) fabrication of a special bracket in two parts adapted to the dimensions of the flange of the valve, and (2) injection of filling material in the bracket around the flange (the material had to be injected at a pressure higher than the operating pressure inside the pipe). During the repair some stud bolts broke causing the escape of a jet of a gaseous mixture of unknown amount of hydrogen and nitrogen at 250 bars. The escaping mixture exploded, killing 2 workers and damaging the valves and the piping.
- Event Initiating system
- Classification of the physical effects
- Hydrogen Release and Ignition
- Nature of the consequences
- Macro-region
- Europe
- Country
- France
- Date
- Component involved
- flange (bolts)
- Failure mode
- rupture & ignition
- Initiating cause
- wrong installation
- Root CAUSE analysis
INITIATING cause was the failure of a flange followed by the release of a nitrogen-hydrogen mixture.
The investigation revealed that two causes have probably contributed to the accident:
(1): the flange stud-bolts of the valve have been replaced by others made of a material not equivalent to the one originally specified;
(2): the maintenance company performing the repair have not taken into account the overpressure on the stud-bolts due to the injection of the filling material in the bracket.
Therefore the root cause could be identified in the lack of a proper risk assessment of the repairing operation.
- Root causes
- Date entry in HIAD
- 28/02/2009
Facility
- Application
- Chemical industry
- Sub-application
- Fertilisers production
- Hydrogen supply chain stage
- All components affected
flange, bolt, ammonia synthesis loop, valve, bracket
- Process temperature range [C]
- High temperature (100°C to 500°C)
- Process pressure range [MPa]
- medium to high pressure (10 to 50 MPa)
- Location type
- Unknown
- Location
- industrial area
- Operational condition
- Pre-event occurrences
Following the detection of a small leak repairing works had been subcontracted, to be performed while the plant continued its operation.
Emergency & Consequences
- Number of fatalities
- 2
- Number of injured persons
- 0
- Emergency action
After the explosion, the ammonia production unit was shut-down.
No off-site emergency measures were necessary.
Lesson Learnt
- Corrective Measures
After the accident, the following measures were established:
- compilation of written maintenance procedures with emphasis on safety issues;
- establishment of the sequence of operations to be followed during repair of such valves.
In-depth data
- Release type
- gas mixture
- Involved substances (% vol)
- H2 75%
N2 25% - Release pressure [MPa]
- 25
- Probable IGNITION SOURCE
- Explosion type
References
- Sources categories
- eMARS
- Reference & weblink
Event description in European database eMARS
https://emars.jrc.ec.europa.eu/en/emars/accident/view/81b0a851-01f8-620…
(accessed September 2020)Event no. 170 in the French database ARIA
https://www.aria.developpement-durable.gouv.fr/accident/176/
(accessed October 2020)