Synthesis Gas Pipeline Rupture Causes Hydrogen Explosion and Jet Fire
A 24" pipe carrying synthesis gas (Hydrogen = 43.5%, Nitrogen = 14.08%, Methane = 0.2%, Carbon Dioxide = 12.3%, Water = 29.3% by volume) ruptured. About 60 kg of hydrogen contained in the gas initially released formed an unconfined vapor cloud and exploded. The explosion was audible up to 2.5 km from the factory and it caused considerable alarm to the residents. Lengths of pipe on either sides of the rupture were displaced as a result of the depressurization. An 8 m length pipe downstream rotated upon itself of about 380 while a 12 m length pipe upstream rotated of about 90. This 12 m section damaged the pipes on an adjacent pipe-rack rupturing the vent header from the desulfurizer unit and causing the release of approximately 600 kg of methane. The hydrogen released from the upstream section of the 24" pipe subsequently burned as a jet-fire about 70 m long. The released methane initially burned as a cloud (60 m long) and then as a jet-fire from the ruptured vent header. On hearing the explosion and by the indications from the plant instrumentation of a major leak, the plant operator shut-off the supply of natural gas to the plant and shut-down the individual units. After about 5 minutes the fire extinguished. A small amount of ammonia vapors which had been released from a fitting on a vapor return line (damaged by the 12 m section pipe) dispersed harmlessly
Event Date
December 23, 1987
Record Quality Indicator
Region / Country
Event Initiating System
Classification of the Physical Effects
Nature of the Consequences
Cause Comments
Metallurgical examination of the 24" pipe showed that a fatigue failure occurred, induced by thermal cycling. Examination of the fracture faces of the ruptured seam weld showed a significant amount of fatigue cracking initiating at the bore of the pipe along a length of about 3 meters of the weld downstream the water injection point. At the upstream end, the rupture propagated circumferentially around the pipe as a shear failure. At the other end, the rupture arrested at a circumferential weld and then propagated as a circumferential tear in the pipe material. The spray pattern from the nozzle was such that water at 80C was intermittently hitting the inner surface of the pipe and quickly cooling the surface. The process gas stream at a temperature of 230C quickly heated up the pipe wall again only for it to be quickly cooled by water impingement at the start of the next cycle. This phenomenon which affected a number of areas in the pipe wall downstream of the water injection nozzle caused a number of small fatigue cracks which ultimately developed so that the material near the longitudinal weld failed. Subsequent examination of the spray nozzle showed that this may have been distorted for some time prior to the accident causing preferential impingement possibly enhancing the failure mechanism although it is not concluded that this distortion was the main cause of the failure. There was a two year history of previous leaks in welds further downstream on this section of pipe which it is now recognized were due to the same cause. At the time the company wrongly diagnosed the cause as external stress corrosion cracking.
Facility Information
Application Type
Application
Specific Application Supply Chain Stage
Components Involved
pipe, pipe-rack, carbon dioxide absorber, CO shift converter
Storage/Process Medium
Location Type
Location description
Industrial Area
Operational Condition
Pre-event Summary
At a petrochemical industry for the Ammonia/Urea production synthesis gas is carried from the CO shift converter to the carbon dioxide absorber of the ammonia synthesis unit via a 24" stainless steel piping. Water is injected into the gas to cool it from 230 to 179 degrees Celsius at 28 bar.
Lessons Learned
Lessons Learned
Unknown
Event Nature
Emergency Action
Unknown
Release Type
Release Substance
Release Amount (kg)
600.00
Detonation
No
Deflagration
No
High Pressure Explosion
No
High Voltage Explosion
No
Flame Type
Source Category
References
References
From public part of MARS database