Prescriptive and risk based SIL allocation methods used together



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Prescriptive and risk based SIL allocation methods used together Handling of potential inconsistencies between NOG GL 070 and LOPA Håkon Dahl-Olsen Senior Consultant, Trondheim Working together for a safer world

Outline Key questions to the industry as a whole Experience with combining Guideline 070 with LOPA Have we established a best practice? Effects of choices Photo: flickr.com phil_g under a Creative Commons licence

Key questions Why do we want to combine the Norwegian Oil and Gas Association s Guideline 070 with risk analysis for establishing required saferty integrity levels? How do we select which functions will be given a SIL rating based on the guideline, and which functions will be subject to a semi-quantitative risk assessment? Using risk based approaches requires stronger risk owner engagement in the SIL allocation process. What can the consulting firm not do by itself? How do we assess the consequences of an undesirable events? Why is it important to select consistent risk acceptance criteria when using LOPA for SIL allocation?

Experience with combining the Norwegian Oil and Gas Association s Guideline 070 and LOPA in Lloyd s Register Consulting

Experience base More than 3 different operators on the Norwegian Continental Shelf Fixed and floating installations Large and small projects Engineering contractors from different regions in the world

What can Guideline 070 give us? Time savings Conservative safety results Covers conventional functions ref ISO 10418 Covers global SIFs

What can Guideline 070 not give us?

Does Guideline 070 suggest how to proceed?

(Why) do we want to combine the Norwegian Oil and Gas Association s Guideline 070 with risk analysis for establishing required saferty integrity levels?

SIF described in NOG GL 070? YES NO Is SIF protecting agains events with environmental or asset integrity impact? NO YES Are NOG GL 070 assumptions fulfilled with regard to demand rate, etc.? NOG GL 070 to be applied YES NO LOPA

Do we get consistent results when combining GL 070 and LOPA? Safety Becomes reference for important SIL Guideline 070 Financials Often leads to high SIL! Consequence? Environment Engineers are typically clueless! Consequence? Different from LOPA results? What is the acceptable frequency? What is acceptable frequency?

Acceptable mitigated event frequencies controlling factor! Typically a LOPA can reproduce expected SILs from GL 070 Requires meaningful numbers to be entered! E.g. overpressure in inlet separator Safety, environment or asset protection dominating? What are the acceptance criteria? In example we only consider safety to compare with GL 070!

Overpressure in inlet separator Initating event Blocked outlet Start-up malop. Choke collapse f IPL1 Alarm IPL2 PSV IPL3 F&G Event probabilt y modifier Ignition prob. 0.1 0.1 0.01 0.01 1 0.1 10-7 Mitigated event frequenc y 24 1 0.01 0.01 0.1 0.1 2.4 x 10-5 24 1 0.01 0.01 0.01 0.1 2.4 x 10-6 Acceptance criteria: 10-6 events per per year [overpressure leading to gas release with fire/explosion, multiple fatalities] Redisdual risk: 3.77 x 10-2 Conclusion: SIL 2 (rounding to integrity level above)

Consequence assessment and choice of categories for severity assessment

Ownership of risk Operator Exposed to risk Knowledge of consequences of all categories Varying degree of method competence Engineering Moderate exposure to risk (financial) Knowledge of consequences to safety and assets Varying degree of method competence Consulting firm Very limited exposure to risk Knowledge of consequences to safety Strong method competence

Effect of poorly chosen consequence categories Typical effect: loss of production for a short time is protected with higher integrity than multiple fatalities Environmental concerns are either exaggerated or neglected Engineers cannot assess ecological conseqeunces in workshops Need acceptance criteria engineers can relate to

Financial risk assessing consequences Asset replacement and repairs are limited in cost Production downtime worth millions per day If grouped in one category fixed asset cost is rarely dominating

Present value retained Value of downtime is lost? For a long field-life, cost of capital eats up the value in terms of present worth With 10% discount factor, a cash flow deferred by 20 years retains only 15% 100 % 80 % 60 % For short field life, complete loss of present value is too conservative 40 % For short field life, asset repair CAPEX may be dominating 20 % 0 % 0 10 20 30 40 50 Years before oil is recovered

Including time value of money? Impractical and difficult in workshop Consequence in terms of practical descriptions better To be adapted to the actual field, project and the operator s chosen risk profile Can only be done by operator! Consulting firm can help suggest categories in cooperation with operator!

Suggested practice Add both direct asset cost and production value as separate acceptance criteria Consider degree of undesiredness up against safety criteria to avoid valuing money over people Note that too conservative acceptance criteria on financial risk will typically yield high SIL requirements on water systems! Cat. Safety Fixed Assets Productio n downtime A Multiple fatalities Not used Not used B Single fatality > 100 mill. > 1 year C D E Lost time incident First aid injury (minor) Injury not requiring first aid 20 100 mill. 2 months 1 year 2 20 mill 14 days 2 months < 2 mill. < 14 days Example only categories not from actual project numbers are not meant to be used in real risk assessments

Can somebody please think about the animals? Environmental consequences are difficult to assess Engineers do typically not have this type of competence Consequences often expressed as severe damage to environment with more than 10 years of recovery time Even more difficult than time-value of money!

Acceptance criteria for environment oil releases Accidents that affect environment are typically due to loss of containment It is possible to estimate the amount of hydrocarbons lost Oil more problematic than gas What about climate gases? Photo: Wikimedia commons (Exxon Valdez)

Acceptance criteria for the environment gas releases Local ecosystem effects much smaller than oil Tend to be completely disregarded as not harmful to environment Methane is a potent greenhouse gas 20 times the effect of CO 2 Methane accounted for ~9% of human contributed greenhouse gas emssions in the United States in 2011 (Source: epa.gov) Category Oil release Gas release A > 500.000 bbl Not used B 100.000 500.000 bbl C 20.000 100.000 bbl D 1000 20.000 bbl > 12500 tons HC gas 2500 12500 tons HC gas 250 2500 tons HC gas E < 1000 bbl < 250 tons HC gas Suggested type of categorization for environmental impact. Numbers that engineers can relate to. Note: not intended for actual use.

Inconsistencies Unnecessary high financial SILs give extra maintenance cost and work typically on safe systems Erodes trust in safety mangement Portrays company as money before poeple likely in dissonance with visions and stated goals

What can the consulting firm not do? Who do we assess consequences of undesirable events? Why is it important to select consistent acceptance criteria?

Summary How Risk Pitfall Based on pre-defined criteria Data dossier must be established as firm basis Operator owns risk Consulting firm cannot set RAC Inconsistent RAC erodes trust in safety management May lead to lack of attention to follow-up in operations

Håkon Dahl-Olsen Team Manager / Senior Consultant Trondheim T +47 942 79 049 E hakon.dahl-olsen@lr.org Lloyd s Register Consulting www.lr.org/consulting Working together for a safer world Lloyd s Register and variants of it are trading names of Lloyd s Register Group Limited, its subsidiaries and affiliates. Copyright Lloyd s Register Consulting. 2013. A member of the Lloyd s Register group.