Natech Accident
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Type
Natech Accident
Date
2010/07/14
Status
Published

Units Involved

  1. Name
    Polystyrene production unit
    Type
    Process: Reactor
    Description
    This upper-tier Seveso site includes two polystyrene production units that comprise three continuously running production lines.

    The workshop was continuously producing 2 types of polystyrene:
    1. 'crystal' (2 production lines - DC1 and DC2) and
    2. 'shock' (1 production line - DC3).

    The production of 'expandable' polystyrene was performed in batch mode in 6 non-synchronised reactors:
    - 2 at the beginning of the cycle;
    - 2 at the intermediate stage; and
    - 2 at the end of the cycle.

Event Sequences

  1. Name
    Heating and explosion of styrene product
    Unit
    1. Polystyrene production unit
    Description
    Due to the storm, a lightning caused a power outage at the Ineos Nova company, which disrupted the control system that monitored the temperature of styrene tanks. The styrene contained in one of the nine tanks began to rise in temperature and pressure. The loss of power triggered a thermal runaway on one of the production lines, which caused a rupture disc to burst, leading in turn to a discharge of 10 tonnes of polystyrene and another 3 tonnes of styrene into the atmosphere.
    Substances Involved
    1. Name
      Polystyrene
      CAS No
      9003-53-6
      Involved Quantity
      10 ton
    2. Name
      Styrene
      CAS No
      100-42-5
      Involved Quantity
      3 ton
      Description
      Styrene is organic compound of the petroleum chemistry, which is used for the production of polystyrene. Styrene is found at liquid state under ambient temperature and it is a harmful product in high doses.
    Initiating EventCritical EventMajor Event
    Lifeline: Loss of electrical power / short circuit
    Due to the storm, a lightning caused a power outage at the Ineos Nova company, which disrupted the control system that monitored the temperature of styrene tanks.
    Contributing Factors
    Equipment: Runaway reaction:
    Being unable to either stir or cool without electric power, a runaway reaction begun that led to a rise of temperature and pressure in the unit.
    Measure: Back-up power: Unavailable
    Only three out of four back-up power generators were available. One power generator was not working at that time. Another power generator was knocked down by the storm (at 10:43 pm). The two remaining generators proved insufficient to cope with the installation's power demand, which triggered the safety mode of the electrical power supply (at 10:46 pm) as a preventive measure due to loss of utility service.
    Substance: Over-heating
    The styrene contained in one of the nine tanks began to rise in temperature.
    Substance: Over-pressurization
    The styrene contained in one of the nine tanks also began to rise in pressure.
    Release: Gas, vapour, mist, or smoke release to air
    A rupture disc was installed as a critical safety item to mitigate the effects of a runaway reaction during both the start-up phase and steady-state operations. However, the thermal runaway on one of the production lines (reactor 1/DC2) caused the rupture disc to burst (at 5.8 bar), leading in turn to a discharge of 10 tonnes of polystyrene and another 3 tonnes of styrene into the atmosphere.
    Dispersion: Substance in air
    Products dispersed in the air and reached nearby homes.

Weather Conditions

Precipitation
Rain

Emergency Response

Response Planning Activities
- In order to minimise the impacts of micro-outages (due to electrical storms), the plant operator typically switched the power supply onto the four back-up electric power generating sets.

- In case of loss of electricity, the safety mode of the electrical power supply is triggered as a preventive measure.
Response Teams and Equipment Involved
  • On-site systems (e.g. sprinkler, water cannon)
  • On-site hazmat team
  • Local fire fighting team
  • Regional / national fire fighting teams
Response to the Natech Event
Around fifty firefighters from Pas-de-Calais but also from the North were called to support the staff from the factory.
No evacuation or confinement plan for local residents was deemed necessary.

- The power supply was switched to the three available back-up electric power generating sets (at 10:20 pm).
- The two remaining generators proved insufficient to cope with the installation's power demand, which triggered the safety mode of the electrical power supply as a preventive measure due to loss of utility service (at 10:46 pm).
- The on-call maintenance electrician was called, as he was the only person actually certified to switch the power supply back onto the electricity grid (at 10:53 pm).
- The internal alarm was sounded, which in turn activated a crisis management unit and notified both on-call team and external first responders (at 11:01 pm).
- Pressure rose in one of the polymerisation reactors at the continuously-running station (first DC1 reactor, at 11:05 pm).
- In accordance with the plant's emergency procedure, gyro monitors were turned on, so as to contain vapours that may have been vented from reactor 1/DC2 line (at 11:15 pm).
- The site was connected to the grid network, though the units started up following a short lapse (at 11:18 pm).
- At 11:20, the disc of reactor 1 (DC2) burst at 5.8 bar, leading in turn to a discharge of 10 tonnes of polystyrene and another 3 tonnes of styrene into the atmosphere.
- A peripheral water curtain was activated to control the vapours (at 11:40).
- Both reactors from the workshop at the beginning of the polymerisation process were emptied into an emergency pit as a precautionary measure.
-The state of alert was lifted at 2 am.

Consequences

On-site People At Risk
27
Off-site Injured
1
Human Health Impacts
No casualties were reported.

Following the request from the site, firefighters performed air quality checks, which were found to comply with standards (according to director of human resources of the company).
Economic Impacts
An emergency order was issued and the units were allowed to restart on 19 July.
The consequences of this accident remained confined to operating loses tied to installation shutdown.
Built-up Areas Impacted
Residential areas (e.g. housings, hotels)
Community Disruption
Residents, not warned to evacuate the area, noticed a strong odour and respiratory discomfort.

Remedial Activities

Decontamination Activities
Styrene concentrations around the pit and in 4 neighbouring municipalities had returned to zero at 12:25 am.
Remediation Activities
- A peripheral water curtain was activated to control the vapours.
- Both reactors from the workshop at the beginning of the polymerisation process were emptied into an emergency pit as a precautionary measure.

Lessons Learned

Lessons Learned on Equipment
- The reactor's runaway response was due to the loss of utility services. Critical utilities that prevent the occurrence of runaway reactions must be ensured even during the impact of a natural hazard either by increasing the robustness of the utilities or by increasing redundancy.

- The design of the reactor had incorporated the possibility of runaway during steady-state operations. Following the accident, the focus was shifted on the runaway response during the start-up phases.

- The objective of the risk management measure was revised in order to limit disc rupture to thermal runaways during start-up, which entailed redesigning the disc. Once this modification had been completed, the process could be considered as intrinsically safe while operating in a steady state.

- The efficiency of the gyro monitors, along with the degree of polymerization (small quantity of released Styrene) and the confinement of the aqueous discharges within a basin, all helped limit the consequences to operating losses for the installation.
Lessons Learned on Organisational Aspects
- Since the technician had not completed the manoeuvre to contain pressure surge, the emergency vent on the CMP unit's line 2 reactors had not opened early on during the incident, as indicated in the procedure. Preparedness for staff should be improved on procedures to mitigate/prevent accidents due to runaway reactions.

-Lack of communication to the public.
Lessons Learned on Mitigation Measures
A protocol change regarding power supply management was carried out, involving:
- the principle of constant redundancy (even during thunderstorm events);
- verification of the availability and operability of critical safety item, CSI, (tied to a thermal runaway) should utilities be down;
- efficient lightning protection.
Lessons Learned on Emergency Response Aspects
1. Immediate measures
- modification to the emergency shutdown procedure on the continuous line (open vent valve, and start-up of gyro monitors upon initiation of the emergency shutdown procedure);
- change of protocol regarding power supply during thunderstorms.

2. Medium-term measures
- technical-economic study to ensure continuous line operations under safer conditions;
- a risk analysis focusing on lightning.
ID: 17, Created: Bogdan DORNEANU, 2013-08-05 11:15:48 – Last Updated: Kyriaki GKOKTSI, 2023-11-20 08:57:30

Attachments

NoDescriptionFile Size
1.ARIA 38617 96.88KB
2.Dudzinski, 2012 768.80KB