1984 union oil romeoville petroleum refinery disaster

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1984 Romeoville petroleum refinery disaster From Wikipedia, the free encyclopedia Jump to: navigation , search On July 23, 1984, an explosion followed by a fire took place at a Union Oil petroleum refinery in Romeoville, Illinois , outside Chicago , killing 17 people and causing major property damage. [1] This vessel was an amine absorber tower used to strip hydrogen sulfide from a process stream of propane and butane. The vessel was 18.8 metres (62 ft) tall, 2.6 metres (8.5 ft) in diameter, and made from 25 millimetres (0.98 in) thick plates of type ASTM A516 Grade 70 steel. The explosive force had been able to propel the upper 14 metres (46 ft) of the vessel a distance of 1 kilometre (0.62 mi) from its original location, while the base remained at the center of the fire that followed after the explosion. Testing of the vessel segments began with non-destructive testing methods. i) Magnetic particle inspection revealed large number of cracks confined mainly to the inner surfaces along the welds between Courses 1 and 2 of the vessel and between Courses 2 and 3. ii) Ultrasonic measurements then detected clear indications of separation of laminate to layers confined to Course 1. iii) Thickness measurements, made with a micrometer , showed that Courses 1 and 2 had wall thickness well within the allowances for pressure vessels. So these tests showed that all initial and replacement components satisfied the industry standard specifications. The cause of failure did not become clear until metallographic results were combined with stress corrosion cracking and hydrogen embrittlement tests, followed by a fracture mechanics analysis. It appeared that

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Root causes of failure and potential failure due to badd weld repair

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1984 Romeoville petroleum refinery disasterFrom Wikipedia, the free encyclopediaJump to: navigation, search

On July 23, 1984, an explosion followed by a fire took place at a Union Oil petroleum refinery in Romeoville, Illinois, outside Chicago, killing 17 people and causing major property damage.[1] This vessel was an amine absorber tower used to strip hydrogen sulfide from a process stream of propane and butane. The vessel was 18.8 metres (62ft) tall, 2.6 metres (8.5ft) in diameter, and made from 25 millimetres (0.98in) thick plates of type ASTM A516 Grade 70 steel. The explosive force had been able to propel the upper 14 metres (46ft) of the vessel a distance of 1 kilometre (0.62mi) from its original location, while the base remained at the center of the fire that followed after the explosion. Testing of the vessel segments began with non-destructive testing methods.i) Magnetic particle inspection revealed large number of cracks confined mainly to the inner surfaces along the welds between Courses 1 and 2 of the vessel and between Courses 2 and 3.ii) Ultrasonic measurements then detected clear indications of separation of laminate to layers confined to Course 1.iii) Thickness measurements, made with a micrometer, showed that Courses 1 and 2 had wall thickness well within the allowances for pressure vessels.So these tests showed that all initial and replacement components satisfied the industry standard specifications. The cause of failure did not become clear until metallographic results were combined with stress corrosion cracking and hydrogen embrittlement tests, followed by a fracture mechanics analysis. It appeared that an already existing crack had extended through more than 90% of the wall thickness and was about 800mm in length. Further, it was determined that hydrogen embrittlement had reduced the fracture resistance of the steel by more than half. The vessel had been put into service in 1970 and had undergone several repairs and modifications before the July 1984 incident. The vessel was fractured along a path that was weakened by extensive cracking adjacent to a repair weld joining a replacement section to the original vessel. These pre-existing cracks initiated in areas of hard microstructure known to be susceptible to hydrogen stress cracking. This hard microstructure formed during the repair welding of the replacement section. The cracks grew through the vessel wall as a result of hydrogen pressure cracking. When the depth of the largest of these pre-existing cracks exceeded 90% to 95% of the wall thickness, the remaining thin ligament of steel in the cracked section ruptured and leakage occurred. This crack caused a complete fracture of the vessel circumference at the operating stress level of only 35 MPa (roughly 10% of the rated strength of the steel) because the toughness of the vessel steel had been reduced by hydrogen embrittlement.

Welding Cracks Caused Union Oil Blast Fatal To 17November 02, 1985|By Dave Schneidman.Cracks in an industrial pressure tank caused the explosion and fire that killed 17 people and caused $100 million in damage last year at the Union Oil Refinery in Romeoville, says a report issued Friday by the state fire marshal. The report, prepared by Packer Engineering Associates, found that a network of cracks formed in the brittle metal surrounding a weld that was made on the pressure tank in 1974, when a section of the tank was replaced.``Eventually that network of cracks joined to form a huge 9-foot crack on the inside of the vessel,`` said Deputy Fire Marshal Tom Ortciger. ``Pressure blew that 9-foot crack open like a zipper`` and blasted the 30-ton vessel 3,400 feet into the air with 1.5 million pounds of thrust.

The 55-foot tank left in its wake a huge cloud of highly flammable propane and butane gas that immediately burst into flame, Ortciger said.The cracks in the tank that caused the explosion were traced to faulty welding work, but the report did not issue any reprimands.``The purpose of the investigation was not to assess blame, but rather to determine cause,`` Ortciger said, pointing out that the fire marshal`s office has recommended changes in inspection procedures for such tanks.After the explosion, Union Oil was cited by state and federal agencies for ineffective inspections of equipment on the site. The firm has denied the charges.The explosion, which occurred July 23, 1984, was in a part of the plant where a raw material was processed into propane, propylene, butylene and butane.The tank was installed at the refinery in 1969, according to the report prepared by Packer, a consulting firm and laboratory retained by the office of the fire marshal to study the blast. The tank was designed to remove hydrogen sulfide from propane and butane gas, a common procedure for gas sold commercially because hydrogen sulfide gives off a strong ``rotten egg`` stench.Problems with the tank were noticed early in its use, the report says. In addition to the 1974 weld, a liner was installed in 1976 in the lower portion of the vessel to control hydrogen corrosion.But Ortciger said it was the 1974 welding that caused the network of cracks. He explained that if metal to be welded is not properly preheated, or is heated after the weld, the surrounding metal becomes brittle. ``Such brittle metal is well known to be susceptible to cracking in a hydrogen-rich environment,`` Ortciger said.Even before the Packer report was issued, Ortciger said, the office of the state fire marshal suspected that weld cracks caused the blast.On Sept. 4, Ortciger said, the fire marshal`s Board of Boiler and Pressure Vessel Rules updated its inspection guidelines covering such pressure vessels in an effort to avoid another explosion.

Previously, each company using pressure tanks had to have a staff of inspectors certified by the fire marshal`s office on hand to approve work on the vessels and was required to inspect them periodically.Because of the Union Oil blast, the rules were modified so that the inspectors make up a separate department within a company`s structure.``The inspectors cannot be part of the company`s financial management team or of their engineering division,`` Ortciger said, ``and thus will not be subjected to any pressure from peers.``Also, Packer has prepared a ``technical information bulletin`` to be distributed to companies throughout the state and describing techniques for applying welds to the vessels.