QRA Method for Land-Use Planning around on-Shore Oil and Gas Facilities
- Type: Conference Presentation
- Conference Type:
AIChE Spring Meeting and Global Congress on Process Safety
- Presentation Date:
March 15, 2011
- Skill Level:
The project was carried out by NOGEPA (Netherlands Oil and Gas Exploitation and Production Association) and RIVM (Dutch National Institute for Public Health and the Environment) and was supervised by the ministries of VROM (Housing, Spatial Planning and Environment) and EZ (Economic Affairs).
In The Netherlands legislation is in place that obliges facilities that handle or store large amounts of hazardous substances to perform a quantitative risk analysis for land-use planning purposes [i]. This involves chemical industries, rail marshalling yards, pesticide storages and LPG fueling stations. It is intended to include on-shore oil and gas facilities, such as production sites and gas treatment sites, in this legislation in 2011. As a result, the current methodology, known as the ?Reference Manual for Bevi Risk Assessments'[ii] (hereafter ?QRA manual'), must be extended with a methodology for on-shore oil and gas facilities. This updated QRA manual will be published in Q1 2012.
In The Netherlands, off-side risk is expressed with two indicators: individual risk (IR) and societal risk (SR). IR is used to determine a zone where the presence of structures such as nearby industries, houses and schools is undesirable or unacceptable. SR is used to determine whether the remaining risk level, related to the acceptable structures in the inner zone and to all structures outside the inner zone, is tolerable.
The use of QRA outcomes for public decision making for current and future land use requires a methodology that is transparent and robust. The stakeholders must be able to verify the method and therefore only generally accessible data can be used for the derivation of release frequencies and for consequence calculations. The outcomes of the QRA should not depend on subjective choices of risk analysts or differences in software models. Therefore, the method to carry out a QRA is prescribed by legislation, including the prescribed use of the software tool Safeti-NLâ. In order to achieve coherence, the QRA method for oil and gas facilities should follow the method for general chemical industries where possible.
Scenario identification and frequency analysis
Only a limited number of activities takes place at the facilities under consideration (see Table 1). Most activities are deemed relevant for the risk assessment. Only the fuel gas system, the venting system and the drainage system do not have to be included in the QRA.
Table 1 Relevance of various activities for the risk outside the facility
Activity / component
Well related activities: drilling, completion, production, injection andmaintenance
One or more wells with tubings and casings, topped with a christmas tree with several valves and a blowout preventer.
well blowout (tubing blowout)
leak from the well
Treatment related activities: oil / gas separation, drying, cleaning, heating, cooling, compression
cessel type and finger (pipe) type slug catchers
adsorbers and scrubbers
full bore rupture of a finger (pipe)
leak from a finger (pipe)
catastrophic rupture of a vessel/heat exchanger/compressor
leak from a vessel/heat exchanger/compressor
atmospheric storage tanks
catastrophic rupture of a vessel
major continuous release from a vessel (entire contents in 600 s)
small leak from a vessel
tank trucks, tank wagons, ships, loading arms
full bore rupture of a pipeline/loading arm
leak from a pipeline/loading arm
catastrophic rupture of a truck/wagon
large/small leak from truck/wagon
major release from a ship after collision
minor release from a ship after collision
Fuel gas system
small dimension pipes and vessels
Not deemed relevant for off-site risk because the dimensions are generally very small.
Not deemed relevant for off-site risk as a result of safe design.
pipes and containment systems
Not deemed relevant as an accident scenario because quantities of hazardous substances should be small.
As mentioned, coherence with the current method for general chemical industries was a prerequisite. Therefore, most attention was paid to activities and equipment types that are specific for the gas and oil facilities. Table 2 gives an oversight of the equipment types for which scenarios and frequencies have been either newly defined or copied from the existing framework.
Table 2 Source of scenario identification and frequency estimation
Source of scenario identification and frequency estimation
Newly defined scenarios and frequencies using SINTEF/Scandpower data.
Updated frequencies using Dutch accident data.
Updated frequencies using a variety of data.
Finger type slug catchers
Modification of scenarios and frequencies for pressure vessels and pipelines in the QRA guideline.
Pressurized and atmospheric storage tanks, adsorbers, scrubbers, a.s.o.
Copied from the existing QRA guideline.
Tank trucks / wagons / ships
Copied from the existing QRA guideline.
Copied from the existing QRA guideline.
For well related activities two release scenarios are defined, namely a well blow-out and a leak from the well. A well blow-out is defined as a release from a well that is not stopped by the blowout preventor and has a release rate similar to a tubing blowout. A leak is defined as a release from a hole with a diameter equivalent to 10% of the diameter of the production tubing. The SINTEF database as reported by Scandpower [iii] was the main source for the derivation of frequencies. This database distinguishes between various types of well activities (drilling, completion, production, various types of maintenance).
For pipelines two release scenarios are defined, namely a full bore rupture of the pipeline and a leak with an equivalent diameter of 10% of the internal diameter of the pipe. The frequencies for pressurized gas pipelines were updated because the frequencies currently used for general chemical industries were not considered to be appropriate. This claim was confirmed by recent work, in which the UK Health and Safety Executive (HSE) and the French INERIS were also involved [iv]. This has resulted in an update of the frequencies to be used.
For compressors two release scenarios are currently defined, namely the catastrophic rupture of the compressor and a leak with an equivalent diameter of 10% of the internal diameter of the feed line. As with the pipelines, the current frequencies used in the QRA manual were not considered to be appropriate for the high integrity compressors that are used for natural gas production and distribution. As a result, a literature and database investigation was carried out under supervision of RIVM and the frequencies were updated [v].
The release scenarios and frequencies for slug catchers were investigated in 2008. The conclusion was that no reliable data for major accidents with slug catchers could be found in literature or databases. As a result of the lack of data, it was decided to use Dutch data for the failure of pressurized vessels with minor modifications.
All other data were taken from the QRA guideline [ii].
The exact frequencies for each distinguished release scenario will be reported in the extended paper.
As prescribed by current Dutch legislation, consequences need to be calculated with Safeti-NLâ from DNV. This is a modification of the widely used DNV product Phast Riskâ. In order to verify the reliability of the outcomes, the results obtained with Safeti-NL were compared with results from the more specific, confidential, software tools FREDâ (oil and gas) and PIPESAFEâ (gas). In general, the observed differences in consequence distances were between 10 and 20%. For extraordinary cases, the differences may be 40%. The outcomes of FREDâ and PIPESAFEâ can however not be used, as they are not publicly available.
A method was defined to calculate the off-site risk resulting from activities at oil and gas facilities such as production sites and oil and gas treatment sites. Where necessary, the scenario identification and frequency estimation were updated. Consequence calculations can only be improved if confidential models be made publicly available.
[i] Dutch external safety degree (in Dutch: Besluit externe veiligheid inrichtingen). Dutch ministry of Housing, Spatial Planning and the Environment (VROM). First issue 2004, current issue 2009.
[ii] Reference Manual Bevi Risk Assessments, version 3.2. RIVM. 2009.
[iii] Blowout and Well Release Frequencies ? Based on SINTEF Offshore Blowout Database 2007. 90.005.003/2008/R3. Scandpower commissioned by StatoilHydro, HSE and Shell. 2008.
[iv] Failure frequencies of on-site natural gas pipelines. André Van vliet, Leendert Gooijer and Gerald Laheij. To be presented at the 45th Loss Prevention Symposium in Chicago, USA. 2011.
[v] Failure frequencies for high integrity natural gas compressors. RIVM. To be published 4Q 2010.
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