Event
- Event ID
- 902
- Quality
- Description
A hot oil line (8-inch) in the hydrodesulphurisation unit failed due to fatigue cracking. Hot oil at 50 bar and 343°C sprayed across the roadway into the hydrogen units where ignition occurred. The pipe break was a guillotine -type, probably in the heat affected zone at 2 inches from a welding. The intense fire around the pipe rack in the hydrogen plant caused a hydrogen line (16-inch) to rupture, adding a second blow torch to the fire. In successive order, more pipes ruptured with explosions. After six-and-a-half hours, the fire was extinguished. Damage was extensive. The three hydrogen units and the four HDS units were heavily damaged or destroyed.
- Event Initiating system
- Classification of the physical effects
- Hydrogen Release and Ignition
- Nature of the consequences
- fire followed by an explosion
- Macro-region
- South America
- Country
- Venezuela
- Date
- Component involved
- pipe (generic)
- Failure mode
- rupture
- Initiating cause
- Conventional fire
- Root CAUSE analysis
The INITIATING CAUSE is fatigue cracking of the oil pipeline, which caused the failure of a hydrogen pipe. Sources refer to probable fatigue cracking, possibly hydrogen assisted. Before the loss, the line which failed was judged as having excessive vibration. Failure of managing out-of-specification fatigue phenomena may be the root cause, or at least a contributing cause.
- Root causes
- Date entry in HIAD
- 01/01/2018
Facility
- Application
- Petrochemical industry
- Sub-application
- Hydrodesulphurisation process
- Hydrogen supply chain stage
- All components affected
Desulphurisation reactor
- Process temperature range [C]
- High temperature (100°C to 500°C)
- Process pressure range [MPa]
- medium pressure (2 to 10 MPa)
- Location type
- Open
- Location
- industrial area
- Operational condition
- Pre-event occurrences
9 years earlier vibrations had been noted on the gas line which failed. The structure had been stiffened by means of gussets. An hypothesis is that this intervention had amplified/accelerated the fatigue phenomena which was caused the break of the line., together with blistering due to hydrogen attack.
Emergency & Consequences
- Number of fatalities
- 0
- Number of injured persons
- 0
- Currency
- US$
- Property loss (onsite)
- 75.000.000.000
- Post-event summary
Damage was extensive. The three hydrogen plants and the four HDS units were heavily damaged or destroyed. Other source report M$89(Excluding Production loss.)
- Emergency action
The fire lasted 6h30
In-depth data
- Release type
- gas mixture
- Involved substances (% vol)
- oilH2
- Release temperature [°C]
- 343
- Probable IGNITION SOURCE
- Flame type
References
- Sources categories
- ARIA
- Reference & weblink
Description of the event in the database ARIA https://www.aria.developpement-durable.gouv.fr/accident/7315/ (accessed September 2020)
MARSH report, 100 largest losses in the hydrocarbon industry, 27th edition 2022 https://www.marsh.com/cz/en/industries/energy-and-power/insights/100-largest-losses.html (accessed January 2024)
A. Goel, Refinery Reliability Through Advanced NDT Methodologies, Proc. National Seminar on Non-Destructive Evaluation Dec. 7 - 9, 2006, Hyderabad http://citeseerx.ist.psu.edu/viewdoc/download?doi=10.1.1.216.4819&rep=rep1&type=pdf (accessed September 2020)