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Clean Hydrogen Partnership

Fire in a refinery

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