Fire on a Heat Exchanger at Refinery
In a petrochemical plant, visual inspection detects fumes under the heat insulation of a heat exchanger operating under hydrogen pressure. The first intervention team was mobilized and the unit stopped for depressurization and cooling. A risk analysis was conducted before erecting a scaffold, decalcifying the exchanger and inspecting it under safe conditions. After having defined the fire protection and fire prevention strategy, the operator decided to put the unit back under pressure. During this rise in pressure, a resumption of fire on the flange justified the triggering of the emergency pln. The intervention team managed the fire. No injuries or impacts outside the site are to be deplored. At the time of the accident, the plant was shut down due to a staff strike. The unit, usually operated under a mixture of butane and hydrogen, according to the supplier's recommendations, was filled with hydrogen only.
Event Date
May 30, 2003
Record Quality Indicator
Region / Country
Event Initiating System
Classification of the Physical Effects
Nature of the Consequences
Causes
Cause Comments
A leaking seal on a flange is the cause of the accident.
Facility Information
Application Type
Application
Specific Application Supply Chain Stage
Components Involved
heat exchanger operating under hydrogen pressure
Storage/Process Medium
Location Type
Location description
Industrial Area
Pre-event Summary
At the time of the accident, the plant was shut down due to a staff strike. The unit, usually operated under a mixture of butane and hydrogen, was filled with hydrogen only according to supplier's recommendations.
Lessons Learned
Lessons Learned
The action plan put in place to reduce the probability of re-occurrence of the accident comprises:1. the study of the possibility of cooling and re-pressurizing the heat exchanger under helium or nitrogen, 2. preventive replacement of all connections under hydrogen 3. regular technical inspection.
Event Nature
Emergency Action
16:00 Fumes detected during a visual inspection. First intervention team is mobilized, the unit is stopped for depressurization and cooling. Risk analysis performed, safety inspection executed,. A fire protection and fire prevention strategy defined and operation restarted by pressurising the system. 21:30 the emergency plan is put in place due to the restart of the fireThe intervention team manages the fire.
Release Type
Release Substance
Hydrogen Release Concentration (%)
100.00
Detonation
No
Deflagration
No
High Pressure Explosion
No
High Voltage Explosion
No
Source Category
References
References
ARIA data base
event no. 26429