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Gas flow incident causes screen pot fall and methane leak

What happened - icon

What happened?

While changing over triethylene glycol (TEG) circulation pumps at a gas processing facility, a reverse flow of gas occurred through the standby pump recycle line, dislodging a 12kg (26lbs) screen pot from the top of the column. This resulted in:

  1. The screen pot falling to the ground from a height of about 10m (33 feet), coming to rest approximately 3m (10 feet) from where an operator was standing.
  2. A Tier 2 loss of containment of methane gas from the reflux condenser column. Gas continued to vent through the top of the column for several minutes until operators remotely shutdown the TEG unit, isolating and depressurising it.
Screen pot on top of reflux condenser column
What happened - icon

Why did it happen?

Uncontrolled reverse flow of high pressure methane gas from top of TEG contactor to still column.

TEG skid was operating with a screen pot that was sitting loose since it was constructed.

12kg (26lbs) screen pot on the ground
What happened - icon

What did they learn?

Ensure transient / abnormal operations that are considered routine operations are reviewed during process hazard analysis (PHA) studies to manage loss of containment risks to as low as reasonably practicable (ALARP).

Review maintenance documentation during the management of work process, and the pre-start safety review process prior to recommissioning /restarting assets.

Rehearsing operator frontline responses is key to enabling safe behaviours during process emergencies.

A robust management of change process during projects is a critical control to ensure newly introduced hazards are identified and risks are managed to ALARP post-design stage.

Common line check valve on lean TEG piping – absent internals
What happened - icon

Ask yourself or your crew

Do you have columns with screen pots at your worksite? Have you checked that screen pots are securely fastened?

Are you involved in conducting process hazard analysis (PHA) studies? Do you identify and review transient operations when conducting PHAs?

Do you review maintenance documentation in the pre-start safety review process prior to recommissioning / restarting assets?

Do you conduct regular emergency drills at your workplace to confirm your readiness to respond safely to a process emergency?

TEG pump 2 discharge check valve – incorrectly reinstated during maintenance work
  • What happened?

    While changing over triethylene glycol (TEG) circulation pumps at a gas processing facility, a reverse flow of gas occurred through the standby pump recycle line, dislodging a 12kg (26lbs) screen pot from the top of the column. This resulted in:

    1. The screen pot falling to the ground from a height of about 10m (33 feet), coming to rest approximately 3m (10 feet) from where an operator was standing.
    2. A Tier 2 loss of containment of methane gas from the reflux condenser column. Gas continued to vent through the top of the column for several minutes until operators remotely shutdown the TEG unit, isolating and depressurising it.
    Screen pot on top of reflux condenser column
  • Why did it happen?

    Uncontrolled reverse flow of high pressure methane gas from top of TEG contactor to still column.

    TEG skid was operating with a screen pot that was sitting loose since it was constructed.

    12kg (26lbs) screen pot on the ground
  • What did they learn?

    Ensure transient / abnormal operations that are considered routine operations are reviewed during process hazard analysis (PHA) studies to manage loss of containment risks to as low as reasonably practicable (ALARP).

    Review maintenance documentation during the management of work process, and the pre-start safety review process prior to recommissioning /restarting assets.

    Rehearsing operator frontline responses is key to enabling safe behaviours during process emergencies.

    A robust management of change process during projects is a critical control to ensure newly introduced hazards are identified and risks are managed to ALARP post-design stage.

    Common line check valve on lean TEG piping – absent internals
  • Ask yourself or your crew

    Do you have columns with screen pots at your worksite? Have you checked that screen pots are securely fastened?

    Are you involved in conducting process hazard analysis (PHA) studies? Do you identify and review transient operations when conducting PHAs?

    Do you review maintenance documentation in the pre-start safety review process prior to recommissioning / restarting assets?

    Do you conduct regular emergency drills at your workplace to confirm your readiness to respond safely to a process emergency?

    TEG pump 2 discharge check valve – incorrectly reinstated during maintenance work
Published on 21/10/24 510 Views

During a pump changeover at a gas processing facility, a reverse gas flow dislodged a 12kg (26lbs) screen pot, which fell 10m (33 feet) and landed 3m (10 feet) from an operator. This incident also caused a Tier 2 methane gas leak, which was controlled after operators shut down and depressurised the unit.

Original material courtesy of Safer Together (Australia)

To access the PDF and PowerPoint versions, please visit https://www.safertogether.com.au/resources/sharing-library/maintaining-process-equipment-loss-of-containment-leb-toolbox