Skip to content

Union Carbide Corp. Nitrogen Asphyxiation Incident

Overview

On March 27, 1998, two workers at Union Carbide Corporation’s Taft/Star Manufacturing Plant in Hahnville, Louisiana, were overcome by nitrogen gas while performing a black light inspection at an open end of a 48-inch-wide horizontal pipe. One Union Carbide worker was killed and an independent contractor was seriously injured due to nitrogen asphyxiation. The incident occurred during a turnaround in the plant’s Taft Oxide I Unit, where nitrogen was being used to purge process equipment.

Incident Snapshot

Field Value
Facility / Company Union Carbide Corporation
Location Hahnville, LA
Incident Date 03/27/1998
Investigation Status The final summary report on this investigation was approved on February 23, 1999.
Accident Type Confined Space / Asphyxiation
Final Report Release Date 02/23/1999

What Happened

  • The 48-inch pipe was open because chemical-processing equipment had been shut down and opened for major maintenance.
  • Nitrogen was being injected into the process equipment primarily to protect new catalyst in reactors from exposure to moisture.
  • The nitrogen was also flowing through some of the piping systems connected to the reactors.
  • The nitrogen was venting from one side of the open pipe where it had formerly been connected to an oxygen feed mixer.
  • No warning sign was posted on the pipe opening identifying it as a confined space or warning that the pipe contained potentially hazardous nitrogen.
  • The two workers had placed a sheet of black plastic over the end of the pipe to provide shade to make it easier to conduct the black light test during daylight.
  • While working just outside the pipe opening and inside of the black plastic sheet, the two workers were overcome by nitrogen.
  • The evening before the incident, Worker A directed Operations Technicians to add the nitrogen to the piping because the catalyst had been changed.
  • Because nitrogen would retard rust formation in the piping connected to the reactors, two valves were opened to allow the flow of nitrogen into the process piping.
  • On the day of the incident, Workers A and B performed a black light inspection and cleaning of the two flange surfaces on the open 48-inch pipe, beginning with the south flange.
  • The black plastic sheet was fastened over the pipe flange because there was a strong breeze that day.
  • The inspection and cleaning of the south pipe flange began at approximately 10:45 am and was completed at about 11:35 am.
  • There was no incident because the nitrogen was not venting through the south pipe opening.
  • Next, the workers and the contractors placed a plastic sheet in the same fashion on the north pipe flange while Workers A and B conducted an inspection and cleaning.
  • Because this part of the pipe was being purged with nitrogen, it contained a high level of nitrogen.
  • The temporary plastic enclosure trapped a high concentration of the nitrogen, which continued to vent out of the north pipe.
  • Contractors, who were on the other side of the black plastic sheet, reported talking with Workers A and B.
  • The last communication with Workers A and B took place just after noon.
  • At approximately 12:20 pm, a contractor noticed blood on one of the worker’s hands when he looked through a gap in the plastic sheet.
  • He alerted his foreman.
  • The foreman called to the two workers behind the sheet and, getting no reply, removed the sheet.
  • Worker B was found in front of the pipe, unconscious and slumped over with his head lying inside the open pipe.
  • Worker A was found seated beside the pipe opening, dazed and leaning against the side of the pipe.
  • The plant emergency response team arrived and removed the two men from the Unit while administering cardiopulmonary resuscitation to Worker B.
  • The two workers were transported by ambulance to St. Charles Parish Hospital.
  • Worker B was dead on arrival.
  • Worker A was admitted to the hospital in critical condition and given oxygen therapy over the next several days.
  • He was released after five days in the hospital.

Facility and Process Context

  • The plant, which produces chemicals for industry, is located about 30 miles west of New Orleans and employs approximately 1,130 people.
  • The incident occurred in the plant’s Taft Oxide I Unit.
  • The Unit primarily produces ethylene oxide, ethylene glycol, and glycol ethers.
  • The Unit uses ethylene and methane as feed gases to produce ethylene oxide.
  • Ethylene and methane are mixed with oxygen and then put in contact with a catalyst located in the reactors.
  • A scrubber removes the product while carbon dioxide gas is also removed.
  • The incident occurred at the fifth level of the structure, approximately 60 feet above the ground.
  • At the time of the incident, the Unit had been in a turnaround status for about six weeks.
  • Worker A was retained as an independent contractor and was in charge of daily operations in the reaction area during the turnaround.
  • Worker A had retired from Union Carbide after 32 years of service, primarily at the plant.
  • Worker B was a Union Carbide employee who had 23 years of service at the plant.
  • Worker B was a Maintenance Skilled Operations Team Technician in the Unit.
  • Worker B was under the general direction of Worker A at the time of the incident.

Consequences

  • Fatalities: 1
  • Injuries: 1
  • Environmental Release: Not specified
  • Facility Damage: Not specified
  • Operational Impact: The Unit had been in a turnaround status for about six weeks.

Key Findings

Immediate Causes

  • Nitrogen and confined space hazard warnings were inadequate.
  • Personnel were unable to detect hazardous levels of nitrogen because this gas cannot be detected by human senses.
  • The men were asphyxiated by nitrogen.
  • The plastic sheet created a dangerous enclosure where nitrogen gas could accumulate, displacing oxygen and causing asphyxiation.

Contributing Factors

  • The temporary plastic enclosure trapped a high concentration of the nitrogen.
  • The open pipe was an unrecognized secondary hazard in the oxygen feed mixer cleaning activity.
  • There was no evaluation of the impact of the catalyst change activity and nitrogen purge on the seemingly unrelated oxygen feed mixer cleaning activity.
  • The plant’s safety program did not adequately address the control of hazards associated with the creation of temporary enclosures around chemical plant equipment.
  • Temporary enclosures that had an easy means of exit were generally not covered by the safety requirements of the plant’s confined space entry policy.
  • No signs were posted at the pipe opening to warn workers and contractors that it was a confined space or that it contained nitrogen.
  • Worker A probably did not realize that nitrogen was venting from the pipe even though the evening before he had directed that nitrogen be injected into the piping system.
  • He may have not remembered that nitrogen was in the pipe because the nitrogen was injected at a distant location, 150 feet and several stories in elevation away from the site of the incident.
  • The workers were not aware that they were being exposed to dangerous levels of nitrogen.
  • High concentrations of nitrogen are dangerous because personnel may not recognize physical or mental symptoms resulting from over-exposure.
  • The two workers involved in the incident were unable to recognize that they were in trouble.
  • They did not try to leave the hazardous work area even though there was an easy means of escape.
  • Contractors were located nearby, but the two workers did not ask for help.
  • Inadequate confined-space warnings and entry procedures.
  • Temporary enclosures like the one in this case were not generally covered by the plant’s confined space procedures.
  • No permit was issued prior to the workers’ entry into the enclosure.
  • No precautions were taken to protect the men from the risk of asphyxiation.
  • Operators did not evaluate the risks caused by the nitrogen purge to the workers downstream.
  • Hazards at the open pipe end were not recognized.
  • The open pipe end itself presented a hazard.
  • Humans cannot detect excess levels of nitrogen because the gas is invisible, odorless, and tasteless.

Organizational and Systemic Factors

  • Prior to the incident, the plant’s safety program did not adequately address the control of hazards associated with the creation of temporary enclosures around chemical plant equipment.
  • Management should have performed this type of evaluation when it planned to inject nitrogen into the 48-inch pipe and out of the north end of the pipe.
  • Management personnel said it was unnecessary to clean the flanges because the oxygen feed mixer had been cleaned and an enriched oxygen atmosphere would not contact the flanges.
  • Management did not expect the specific job of a black light inspection to be performed.
  • There were other workers in the area who needed to be protected from the potential nitrogen hazard.
  • The plant had a confined space entry program and a chemical safety-training program. Nonetheless, one very experienced worker died and another was seriously injured because these workers were not aware that they were being exposed to dangerous levels of nitrogen.
  • Although the Union Carbide plant did have procedures for entering confined spaces, CSB found that these procedures did not generally cover temporary enclosures like the one in this case.
  • After the accident, managers said they did not know that the workers were going to perform a black light inspection of the pipe, which led to the creation of a temporary enclosure.

Failed Safeguards or Barrier Breakdowns

  • No warning sign was posted on the pipe opening identifying it as a confined space or warning that the pipe contained potentially hazardous nitrogen.
  • The plant’s safety program did not adequately address the control of hazards associated with the creation of temporary enclosures around chemical plant equipment.
  • Temporary enclosures that had an easy means of exit were generally not covered by the safety requirements of the plant’s confined space entry policy.
  • There was no evaluation of the impact of the catalyst change activity and nitrogen purge on the seemingly unrelated oxygen feed mixer cleaning activity.
  • Recognition of the nitrogen hazard could have identified the need to post a nitrogen warning sign at the pipe opening where the incident took place.
  • Personnel were not aware of the hazard of the nitrogen flowing out of the open pipe that they were working on.
  • The workers were not aware that they were being exposed to dangerous levels of nitrogen.
  • Inadequate confined-space warnings.
  • Entry procedures.
  • No permit was issued prior to the workers’ entry into the enclosure.
  • No precautions were taken to protect the men from the risk of asphyxiation.
  • Operators did not evaluate the risks caused by the nitrogen purge to the workers downstream.
  • Hazards at the open pipe end were not recognized.
  • Warning signs at the pipe opening were not posted.
  • The gas was not odorized.

Recommendations

  1. 98-05-I-LA-R1 | Recipient: Union Carbide Taft Plant | Status: Not specified | Post signs containing the warning “Danger, Confined Space: Do Not Enter Without Authorization” or similar wording at potential entryways when tanks, vessels, pipes, or other similar chemical industry equipment are opened. When nitrogen is added to a confined space, post an additional sign that warns personnel of the potential nitrogen hazard.
  2. 98-05-I-LA-R2 | Recipient: Union Carbide Taft Plant | Status: Not specified | Ensure that the plant safety program addresses the control of hazards created by erecting temporary enclosures around equipment that may trap a dangerous atmosphere in the enclosure if the equipment leaks or vents hazardous material.
  3. 98-05-I-LA-R3 | Recipient: National Institute for Occupational Safety and Health | Status: Not specified | Conduct a study concerning the appropriateness and feasibility of odorizing nitrogen in order to warn personnel of the presence of nitrogen when it is used in confined spaces.
  4. 98-05-I-LA-R4 | Recipient: Occupational Safety and Health Administration | Status: Not specified | Issue a safety alert that addresses the hazards and provides safety guidelines for the use of temporary enclosures that are erected around equipment containing hazardous substances.
  5. 98-05-I-LA-R5 | Recipient: Center for Chemical Process Safety | Status: Not specified | Communicate the findings of this report to your membership.
  6. 98-05-I-LA-R6 | Recipient: Compressed Gas Association | Status: Not specified | Communicate the findings of this report to your membership.

Key Engineering Lessons

  • Temporary enclosures around opened process equipment can trap hazardous atmospheres if the equipment leaks or vents hazardous material.
  • A black plastic sheet used for work convenience can create a dangerous enclosure when placed over an opening connected to a nitrogen purge.
  • Open pipe ends and downstream work areas must be evaluated for hazards created by upstream purge or maintenance activities.
  • Warning signs at opened tanks, vessels, pipes, or similar equipment are needed when a confined space or nitrogen hazard may be present.
  • Nitrogen used in confined spaces is especially hazardous because it is invisible, odorless, tasteless, and cannot be detected by human senses.

Source Notes

  • Priority 1 final report used as primary authority; supporting document used only to supplement where consistent.
  • Conflicting or less specific wording from lower-priority source was not used when the final report provided clearer terminology.
  • All facts were taken only from the provided source extracts; no external information was added.

Similar Incidents

Incidents sharing the same equipment, root causes, or hazard types.

Same Equipment

Same Root Cause

Same Hazard


Could this happen in your plant?

Find similar incidents in the CSB database:

By equipment: Pipeline Ruptures, Leaks, and Fires · Reactor Explosions and Runaway Reactions · Valve Failures in Process Plant Incidents

By hazard type: Asphyxiation · Toxic Release · Chemical Release

By industry: Chemical Manufacturing Incidents