Risk Assessment of large Hydrocarbon Storage tanks G. Unnikrishnan, - - PowerPoint PPT Presentation

risk assessment of large hydrocarbon storage tanks
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Risk Assessment of large Hydrocarbon Storage tanks G. Unnikrishnan, - - PowerPoint PPT Presentation

Risk Assessment of large Hydrocarbon Storage tanks G. Unnikrishnan, Kuwait Oil Company What QRAs can tell Incident/failure Location Specific frequencies Individual Risk Identification Risk transects Measures Of incident of Risk scenarios


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Risk Assessment of large Hydrocarbon Storage tanks

  • G. Unnikrishnan, Kuwait Oil Company
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What QRAs can tell

Identification Of incident scenarios Incident/failure frequencies Consequences Impacts Measures

  • f Risk
  • Location Specific

Individual Risk

  • Risk transects
  • Frequency –

Fatalities (FN Curve)

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Risk Contours Risk transect

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Variations in predicted frequencies of defined levels of fatalities ranging between 2 and 4 orders of magnitude by different analysts.

FN Curve

ASSURANCE Project: Benchmarking exercises for QRA methods

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  • Buncefield. UK: 10 Dec 2005:

Property damage, Environmental impact

Will QRAs would have predicted this ?

San Juan. Puerto Rico: 23 October 2009: Property damage, Environmental impact

  • Jaipur. India: 29

October 2009: 13

  • Fatalities. Property

damage, Environmental impact

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There should be a clear understanding of major accident risks and the safety critical equipment and systems designed to control them. There should be systems and a culture in place to detect signals of failure in safety critical equipment and to respond to them quickly and effectively. Time and resources for process safety should be made available. There should be effective auditing systems in place which test the quality of management systems and ensure that these systems are actually being used on the ground and are effective. At the core of managing a major hazard business should be clear and positive process safety leadership with top management involvement and competence to ensure that major hazard risks are being properly managed.

  • Buncefield. Why it happened
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 Systematic assessment of Safety Integrity Level requirements  Protecting against loss of containment using high integrity systems  Engineering against escalation of loss of primary containment  Engineering against escalation of loss of secondary and tertiary containment  Operating with high reliability organizations  Delivering high performance through culture and leadership

  • Buncefield. Recommendations (20)
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  • Jaipur. Why it happened

 The Loss of containment in terms of time & quantity was never considered a credible event and accordingly not taken into hazard identification.  Basic operating procedures for hammer blind opening was not followed.  Accident could have been managed if safety measures provided in control room were not made defunct.  Backup for emergency shutdown from Control room not available.  There was delay in emergency response for long period.

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  • Jaipur. Recommendations (118)

 Engineering related  Operation related  Procurement related  Training related  Policy related

  • Use of Remote Operated Valve
  • Tank dike valves –position indicators in Control room
  • High reliability High level alarm
  • Automation of Tank Farms in terms of hardware and

software

  • Written emergency procedures & training
  • Maintaining Shift manning levels at all times
  • Installation of CCTVs
  • Installation of Hydrocarbon Gas detectors
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What can be done ? Bow Tie Diagram and concept of Barriers

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Existing methods : Fault Tree Event Tree

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Bow Tie Diagram: Combination of Fault Tree & Event tree

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Initiating event probabilities Barrier Failure probabilities Hazardous event probability Barrier Failure probabilities Consequence probabilities

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Thank you Thank you

Q & A Q & A