REQUIREMENTS FOR VALIDATION OF MATHEMATICAL MODELS IN SAFETY CASES

Similar documents
Comparison of Large-Scale Vented Deflagration Tests to CFD Simulations for Partially Congested Enclosures

Determination of the Design Load for Structural Safety Assessment against Gas Explosion in Offshore Topside

EXPLOSION RELIEF PROTECTION FOR INDUSTRIAL PLANT OF INTERMEDIATE STRENGTH

USE OF THE EXCEEDANCE CURVE APPROACH IN OCCUPIED BUILDING RISK ASSESSMENT

CFD Based Approach for VCE Risk Assessment

Internal Explosion Methodologies

Fire loading and Structural Response

MODELLING OF FUME EXTRACTORS C. R.

Fire and Safety for Offshore drilling and production Ajey Walavalkar ANSYS Inc.

Abstract. Geometry Obstructions Ventilation Wind conditions

Hydrogen and fuel cell stationary applications: key findings of modelling and experimental work in the HYPER project

Injector Dynamics Assumptions and their Impact on Predicting Cavitation and Performance

Engineering Models for Vented Lean Hydrogen Deflagrations

VENTED CONFINED EXPLOSIONS INVOLVING METHANE/HYDROGEN MIXTURES

Improvement in Release Frequencies for Quantitative Risk Assessment

DIGITAL SOLUTIONS TRAINING CATALOGUE. QRA and CFD simulation. Phast, Safeti and KFX SAFER, SMARTER, GREENER

Experimental determination of deflagration explosion characteristics of methane air mixture and their verification by advanced numerical simulation

THE EXTERNAL EXPLOSION CHARACTERISTICS OF VENTED DUST EXPLOSIONS.

SHAPA TECHNICAL PAPER 10 (Revised) SIZING OF EXPLOSION RELIEF VENTS DAVID BURN FIKE UK LTD

Experimental Study of Hydrogen Release Accidents in a Vehicle Garage

EXPERIMENTAL STUDY ON HYDROGEN EXPLOSIONS IN A FULL-SCALE HYDROGEN FILLING STATION MODEL

Identification and Screening of Scenarios for LOPA. Ken First Dow Chemical Company Midland, MI

Prediction of gas explosion overpressure interacting with structures for blast-resistant design

Gerald D. Anderson. Education Technical Specialist

NUMERICAL INVESTIGATION OF THE FLOW BEHAVIOUR IN A MODERN TRAFFIC TUNNEL IN CASE OF FIRE INCIDENT

PRAGMATIC ASSESSMENT OF EXPLOSION RISKS TO THE CONTROL ROOM BUILDING OF A VINYL CHLORIDE PLANT

SIMULATIONS OF HYDROGEN RELEASES FROM A STORAGE TANKS: DISPERSION AND CONSEQUENCES OF IGNITION

Study on Intensity of Blast Wave Generated from Vessel Bursting by Gas Explosion

Ignition modelling Are our approaches aligned?

AIRFLOW GENERATION IN A TUNNEL USING A SACCARDO VENTILATION SYSTEM AGAINST THE BUOYANCY EFFECT PRODUCED BY A FIRE

Quantitative Risk Analysis for Explosion Safety of Oil and Gas Facilities

The Influence Of Vessel Volume And Equivalence Ratio In Vented Gas Explosions

Simulations of hydrogen releases from high pressure storage systems

Module 03 Accident modeling, risk assessment and management Lecture 04 Explosions

Computational Fluid Dynamics

Ermenek Dam and HEPP: Spillway Test & 3D Numeric-Hydraulic Analysis of Jet Collision

BACKGROUND. Subsequently, British Gas carried out a series of full-scale experiments, releasing natural gas at high pressure into horizontal

Dynamic Modelling of Control Valves

Simulation and modelling of water spray in the 3D explosion simulation program FLACS. Elin Kristin Dale

I.CHEM.E. SYMPOSIUM SERIES NO. 97 BUOYANCY-DRIVEN NATURAL VENTILATION OP ENCLOSED SPACES

EXPLOSION VENTING OF BUCKET ELEVATORS

Aberdeen Significant Error Review ITE Independent Report. Eur Ing Keith Vugler CEng FInstMC

Damage Assessment Following Accidents - Official Discussion

MODELING OF HYDROGEN EXPLOSION ON A PRESSURE SWING ADSORPTION FACILITY

PSM TRAINING COURSES. Courses can be conducted in multi-languages

"Although a good start with a good project, others are as much a hostage of the "human factor".

FIRE PROTECTION. In fact, hydraulic modeling allows for infinite what if scenarios including:

ACCUMULATION OF HYDROGEN RELEASED INTO A VENTED ENCLOSURE - EXPERIMENTAL RESULTS

DETERMINATION OF SAFETY REQUIREMENTS FOR SAFETY- RELATED PROTECTION AND CONTROL SYSTEMS - IEC 61508

Investigation of Cargo Tank Vent Fires on the GP3 FPSO, Part 2: Analysis of Vapour Dispersion

Development of Accidental Collapse Limit State Criteria for Offshore Structures

Misuse of Combustible Gas Meters

Computational Analysis of Oil Spill in Shallow Water due to Wave and Tidal Motion Madhu Agrawal Durai Dakshinamoorthy

The «practical elimination» approach for pressurized water reactors

PERCEPTIVE ROBOT MOVING IN 3D WORLD. D.E- Okhotsimsky, A.K. Platonov USSR

Specific Accreditation Criteria Calibration ISO IEC Annex. Mass and related quantities

TG GUIDELINES CONCERNING CALIBRATION INTERVALS AND RECALIBRATION

American Chemical Society (ACS) 246th ACS National Meeting Indianapolis, Indiana September 9, 2013

Kiefner & Associates, Inc.

MODELLING OF POOL FIRE AND INJURY PREDICTION CONSIDERING DIFFERENT WIND SPEEDS AND DIRECTIONS IN OFFSHORE PLATFORM

POWER Quantifying Correction Curve Uncertainty Through Empirical Methods

Critical Systems Validation

Study of Passing Ship Effects along a Bank by Delft3D-FLOW and XBeach1

Free Surface Flow Simulation with ACUSIM in the Water Industry

ROUNDABOUT CAPACITY: THE UK EMPIRICAL METHODOLOGY

INHERENTLY SAFER DESIGN CASE STUDY OF RAPID BLOW DOWN ON OFFSHORE PLATFORM

ITTC Recommended Procedures Testing and Extrapolation Methods Loads and Responses, Seakeeping Experiments on Rarely Occurring Events

Vented confined explosions involving methane/hydrogen mixtures

QUANTIFYING THE TOLERABILITY OF POTENTIAL IGNITION SOURCES FROM UNCERTIFIED MECHANICAL EQUIPMENT INSTALLED IN HAZARDOUS AREAS

Key words: gas explosion, turbulence, scaling, burning velocity INTRODUCTION

Traffic circles. February 9, 2009

Improving Accuracy of Frequency Estimation of Major Vapor Cloud Explosions for Evaluating Control Room Location through Quantitative Risk Assessment

Blast Damage Consideratons for Horizontal Pressure Vessel and Potential for Domino Effects

Effect of Diameter on the Aerodynamics of Sepaktakraw Balls, A Computational Study

Explosion venting of bucket elevators

Flow transients in multiphase pipelines

AutoReaGas - A CFD-Tool for gaz explosion hazard analysis

HYDROGEN RISK ANALYSIS FOR A GENERIC NUCLEAR CONTAINMENT VENTILATION SYSTEM

General Accreditation Guidance. User checks and maintenance of laboratory balances

Justification of Risk Reduction through In-Service Inspection / REDUCE

Modelling Hazardous Consequences of a Shale Gas Well Blowout

A METHOD FOR ASSESSING THE CONSEQUENCES OF SMALL LEAKS IN ENCLOSURES

ICHEME SYMPOSIUM SERIES NO. 139 THE HAZARDS POSED BY LARGE-SCALE POOL FIRES IN OFFSHORE PLATFORMS

Learning from Dangerous Occurrences in the Chemical Industries

Evaluation of Northwest Citizen Science Initiative (NWCSI) March 7,2015 Report Summary

RYA British Youth Sailing Safety Policy

Numerical Simulation of Wave Loads on Static Offshore Structures

INTERIM ADVICE NOTE 171/12. Risk Based Principal Inspection Intervals

Direct Numerical Simulation on Hydrogen Fuel Jetting from High Pressure Tank

Advanced Training for DP Operators

Offshore Oil and Gas Platforms for Deep Waters

Experimental Characterization and Modeling of Helium Dispersion in a ¼-Scale Two-Car Residential Garage

Control of surge and pitch motions of a rectangular floating body using internal sloshing phenomena. Minho Ha and *Cheolung Cheong 1)

ICHEME SYMPOSIUM SERIES NO. 144

Session One: A Practical Approach to Managing Safety Critical Equipment and Systems in Process Plants

Novel Approaches to Venting

Practical Modelling & Hazard Assessment of LPG & LNG Spills

Responding to Natural Gas Pipeline Emergencies

Accident/Incident Reporting and Investigation Procedures

Review and Assessment of Engineering Factors

Transcription:

REQUIREMENTS FOR VALIDATION OF MATHEMATICAL MODELS IN SAFETY CASES R F Evans Principal Specialist Inspector, Health & Safety Executive Offshore Safety Division, Bootle Merseyside. The Offshore Installations (Safety Case) Regulations 1992 require operators (or owners) of offshore installations to prepare a Safety Case that shows, among other things, that risks from a major accident have been reduced as far as is reasonably practicable. Such a hazard is that of a gas explosion. To show that effective measures have been taken to prevent or mitigate the consequences of a major accident it is first necessary to identify the sources of the hazard and then determine their consequences. This requires the prediction of the effects of gas explosions. Several mathematical models are available and used for this purpose. This paper describes some of these models and their inherent uncertainties. It explains the need to validate the models, the methods used to effect such validation and difficulties met in trying to validate models for use on offshore installations. INTRODUCTION On 6 July 1988 an explosion on the Piper Alpha platform started a chain of events that led to the destruction of the platform and the loss of 167 lives. This prompted a public inquiry under Lord Cullen 1 who, as a result of his findings, recommended sweeping changes to the way health and safety were administered in the North Sea. One of his recommendations was the introduction of legislation requiring the operators (or owners) of offshore installations to prepare a Safety Case showing, among other things, that risks from a major accident had been reduced as far as is reasonably practicable. This recommendation was implemented in the form of the Offshore Installations (Safety Case) Regulations 1992 An obvious major accident hazard is that of a gas explosion. Before it can be shown that effective measures have been taken to prevent or mitigate the consequences of such a major accident it is necessary to identify the sources of the hazard and then determine their consequences. This requires the prediction by mathematical models or otherwise of the effects of gas explosions. There has long been an interest in predicting the effects of gas explosions, and mitigating their consequences. Much research has been carried out in this field, starting with the work of Cubbage and Simmonds 2 in the 1950s and continuing to this day. Recently a review of the applicability of the predictive methods to gas explosions in offshore modules has been carried by British Gas on behalf of the Department of Energy 3. A review of prediction methods has also been carried out by the Steel Construction Institute (SCI) 4 as part of a joint industry project on blast and Crown Copyright 263

fire engineering for topsides structures and they have subsequently published guidance based on their findings 5. Although it is comparatively easy to predict the effects of an explosion in a confined and relatively uncongested space such as an oven it is much more difficult to do so for a large and congested space such as a module on a typical offshore installation and there are still many areas of uncertainty. This paper is concerned with the particular problems met when trying to predict the blast loadings of a gas explosion in a typical offshore module. It does not deal with how plant or the structure of the module will respond to these loadings. EXPLOSION MODELS To model a gas explosion it is necessary to know the extent and composition of the gas cloud. This can be achieved by identifying leak sources and modelling the leak and dispersion. Mathematical techniques are available for such modelling but often the conservative assumption is made that the module is filled with a stoichiometric mixture of gas and air. Owing to their highly congested nature, offshore modules do not lend themselves to simple methods for calculating blast loadings. Whereas unconfined hydrocarbon gas clouds do not generally cause large explosion pressure impulses, where the gas flow generated by an explosion passes through an obstacle array the turbulence generated can cause the flame front to accelerate leadibng to very large pressure impulses. Turbulence can also be generated by the momentum of a jet of escaping fluid. Several methods have been developed for simulating these effects. These include small-scale simulations, using a gas mixture with enhanced reactivity to compensate for the reduced scale, and mathematical modelling. The former offer interesting possibilities but still rely on mathematical scaling arguments. This paper, therefore, concentrates on mathematical modelling techniques. Mathematical models for predicting the behaviour of gas explosions fall into 3 categories: 1 Empirical: these simple models extrapolate to the real problem from a set of small-scale experimental data in a range of geometries, usually idealised. The relative importance of the variables measured in the experiments is then assumed to hold for the real conditions of interest. At best these models can only give rough answers since without some fundamental modelling of the combustion and turbulence processes there is no reliable way of predicting what will happen at larger scales, in different geometries and for different fuels from those studied in the underlying experiments. 2 Phenomenological: these models use a set of equations to describe the bulk behaviour of the explosion/ taking account of the dominant physical processes. The models are calibrated against experimental data, both on individual physical 264

processes (eg turbulent burning velocities) and from idealised or realistic module geometries. Because they are based on a model of the physics of combustion processes, they can be used to extrapolate from experimental data more safely than can empirical models (if the model is good enough) and, because only a few simple equations have to be solved, they do not require a great deal of computing power. However owing to the simplifying assumptions made, and because the models are based only on the dominant physical processes, there may be some doubts about the reliability of these models in predicting behaviour beyond the range of experimental data unless the extrapolation can be supported by a demonstration that different physical effects do not become dominant. 3 Numerical: these models are usually based on computational fluid dynamics. The field in which the explosion occurs is divided by a grid and the behaviour in each cell within the grid calculated in turn. This type of model demands a great deal of computing power and, to enable it to run on even a very powerful computer, requires the use of a coarse grid (about lm 3 ) and, to take account of turbulence effects of a smaller scale than the grid size, sub-grid turbulence models are employed. Thus simplifying assumptions have to be made although to a lesser extent than with the phenomenological models. As with phenomenological models it is necessary for these models to be calibrated and validated against experimental data. Table 1. is a list of models typical of those used to predict blast loadings in offshore modules. EXPERIMENTAL DATA As already discussed even the most sophisticated models have uncertainties in them. These uncertainties become greater when the models are used to extrapolate beyond the range of the experimental data against which they were calibrated, particularly because the simplifying assumptions made may not hold true at the larger scale. There is a large body of experimental data which has been generated by organisations working in this field against which models can be calibrated. However not all models will necessarily have been calibrated against the same set of data and none of them have been calibrated against full-scale experimental data because of the sheer size of typical offshore modules. Hitherto no experimental data have been obtained on rigs of greater than about one fifth linear scale. VALIDATION Models can be validated against existing data other than those against which they were calibrated and, as stated above, these data exist. Models can also be validated by a model comparision 265

exercise. However no full scale experiments have been carried out yet and when extrapolating beyond the range of existing experimental data there will be large uncertainties because there may be some assumptions common to all the models that do not hold true at the larger scale. To rectify this situation there are plans to carry out tests at full scale. There is a joint industry project managed by the Steel Construction Institute to build a 3000m 3 model of a typical offshore module and carry out a series of tests in it to obtain data that it will then be possible to use to validate models at full scale. It is unlikely that the results from full-scale experiments will be available for some time yet. In the meantime it has to be recognised that there is a high degree of uncertainty in all the models and this should be taken into account in applying them. When uncertainties in passing to different geometries at full-scale are taken into account one may well suppose that the error could be in the order of a factor of two or more. The models will not necessarily produce conservative results. When using a physical or mathematical model for predicting blast loadings for the purposes of a Safety Case the degree of validation expected will depend on the extent to which the Case relies on the predictions. For example the assumption that an explosion would cause major damage would be acceptable if the frequency of such events were shown to be both tolerable and as low as is reasonably practicable: this would not require any validated predictions. In other cases the degree of certainty sought in the predictions should increase with the frequency of the events leading up to an explosion and the size of the risk from the explosions in relation to the total risk. In any case it will be necessary to take account of the uncertainties in any risk assessment based on the predictions. The SCI Interim Guidance Note 5 advises that with the current state of knowledge it would not be prudent to rely on any single predictive method where the predicted values of explosion pressures are of critical consequence. APPLICATIONS Although all models have a high degree of uncertainty they are nonetheless of practical value. Apart from their application in risk assessments they can be used to show how passive inherent features of design such as layout and venting paths influence the effect of explosions. They can also show where improvements need to be made such as the provision of vents and the construction of blast walls or measures taken to reduce the probability of unacceptably severe explosions. They may well be better at showing the relative effect of such changes than in predicting absolute values. 266

CONCLUSIONS 1 There is a large body of data based on experiments on the effects of explosions in models of offshore modules. 2 Although these experiments have been carried out over a wide range of scales none have been carried out on rigs of greater than about one fifth scale. It has therefore not been possible to validate these models at full scale. 3 Confidence in these models could be improved by validating them against data from a wide range of sources, by carrying out a benchmark exercise and by carrying out experiments in a full-scale rig. 4 In the meantime the models can be put to good use in risk assessments provided that allowance is made for the inherent uncertainties. They can also be used in comparative studies of the influence that passive design features such as plant layout have on explosions. Models may be better at showing the relative effect of changing such features than in predicting absolute values. REFERENCES 1 The HON. LORD CULLEN, The Public Inquiry into the Piper Alpha Disaster. HMSO London, November 1990. 2 Cubbage, P.A., Simmonds, W.A. An Investigation of Explosion Reliefs for Industrial Drying Ovens - I Top Reliefs in Box Ovens, Trans. Inst. Gas Engrs., 105, p470, 1950. 3 OTH 89 312 Review of the Applicability of Predictive Methods to Gas Explosions in Offshore Modules. Prepared by British Gas for the Department of Energy. 4 OTH 92 591 (BL1) Gas/Vapour build-up on offshore structures. OTI 92 592 (BL2) Confined vented explosions. OTH 92 593 (BL3) Explosions in highly congested volumes. OTI 92 594 (BL4) The prediction of the pressure loading on structures resulting from an explosion. OTI 92 595 (BL5) Possible ways of mitigating explosions on offshore structures. 5 Interim Guidance Notes for the Design and Protection of Topside Structures against Explosion and Fire. Published by the Steel Construction Institute. 267

Table 1.. Typical Models used to Predict Blast Loadings in Offshore Modules 268