Event
- Event ID
- 161
- Quality
- Description
- The event occurred at the in the distillate hydrotreater unit of a refinery. This unit removed sulphur from a hydrocarbon feedstock by hydogenating it with hydrogen. A 12-inch overhead pipe ruptured with a loud noise and released flammable gaseous hydrocarbonsat a temperature high enough to cause spontaneous ignition.
The pipe normally operated at a pressure of approximately 600 pounds per square inch (approximately 40 bar). No personnel were present in the unit when the pipe rupture occurred.
The local fire brigade extinguished the ensuing fire two hours later. No employees or emergency responders were injured. Air monitoring at the perimeter of the refinery did not detect elevated concentrations of any hazardous chemicals.
The fire damage was confined to other equipment in an area of to an approximately 10 square meter. Two fan-type heat exchangers were destroyed by the fire along with an approximately 50-foot section of piping; electrical conduit was also damaged by radiant heat. No blast damage was observed. - Event Initiating system
- Classification of the physical effects
- Hydrogen Release and Ignition
- Nature of the consequences
- Fire (No additional details provided)
- Macro-region
- North America
- Country
- United States
- Date
- Main component involved?
- Pipe
- How was it involved?
- Rupture & Formation Of A Flammable H2-Air Mixture
- Initiating cause
- Material Degradation (Internal Corrosion / Erosion)
- Root causes
- Root CAUSE analysis
- The cause of the pipe rupture could not be determined. Nevertheless, the investigation noted there have been a number of past instances of corrosion-related failures in refinery hydrotreater units.
Facility
- Application
- Petrochemical Industry
- Sub-application
- hydrotreater
- Hydrogen supply chain stage
- All components affected
- gas recycle line
- Location type
- Unknown
- Location description
- Industrial Area
- Operational condition
- Pre-event occurrences
- the investigation reported that there have been a number of past instances of corrosion-related failures in refinery hydrotreater units.
Emergency & Consequences
- Number of injured persons
- 0
- Number of fatalities
- 0
- Environmental damage
- 0
- Post-event summary
- The fire damage was confined to other equipment in an area of to an approximately 10 square meter. Two fan-type heat exchangers were destroyed by the fire along with an approximately 50-foot section of piping; electrical conduit was also damaged by radiant heat. No blast damage was observed.
Air monitoring at the perimeter of the refinery did not detect elevated concentrations of any hazardous chemicals. - Emergency action
- A very detailed Emergency Response record is given in the HAZMAT report in the references.
Lesson Learnt
- Lesson Learnt
In general, it is important to carefully guarantee the integrity of piping that contains hazardous substances through rigorous inspection and testing, and to adapt them with increasing ageing of the components.
Event Nature
- Release type
- Liquid
- Involved substances (% vol)
- H2 100%
- Actual pressure (MPa)
- 4
- Presumed ignition source
- Not reported
References
- Reference & weblink
HeraldGuide news of 21 May 2006:<br />
https://www.heraldguide.com/news/investigation-of-valero-explosion-comp… />
(accesed January 2024)
JRC assessment
- Sources categories
- News