Advancements in the prediction of blast damage due to vapour cloud explosions. Hans Boot

Size: px
Start display at page:

Download "Advancements in the prediction of blast damage due to vapour cloud explosions. Hans Boot"

Transcription

1 Advancements in the prediction of blast damage due to vapour cloud explosions

2 2 Contents Predicting VCE Damage zones? = the WHY Explosion modeling = the WHAT Using the GAME correlations = the HOW 1 Explosion regions : connecting dispersion to explosion models = the HOW 2 Calculation procedure = RESULT Conclusions

3 3 Technology evolves! New models have been published after the last version of Yellow book (1984,1995,2005) Government does not want changes: other risk distances!! Yet, new, improved insight models are being added to TNO consequence modelling tool e.g: 1. Dynamic BLEVE (Martinson & Marx) 2. Two Zone pool fire (Rew & Hulbert) 3. Statistical spray release (Dam) 4. GAME correlations (van de Berg & Mercx)

4 4 Vapour Cloud Explosions (VCE s) One of the most destructive accident scenarios on (petro)chemical sites Much effort in prevention, but.. what if it happens? Avoid domino effects! Use site layout guidelines/requirements for plant buildings Conscious choice for location operator rooms Constructions designed to withstand certain overpressure Evaluation requires knowledge of potential blast strength

5 5 VCE damage modelling Knowledge on potential damage requires: - Prediction of overpressure / impulse (blast strength) - Information about construction strength (vulnerability) Explosion models: 1. Numerical simulations 2. TNT equivalency 3. Blast curve methods Can a VCE affect the operator room?

6 6 Typical explosion models Numerical simulations (CFD based) Requires detailed 3D geometry Total site: multiple sources/receivers/ wind angle s: laborious & expensive TNT equivalency method Requires equivalency factor Primary aimed at solids: short duration high amplitude Blast Curve methods TNO Multi Energy : developed for VCE s Requires estimation Blast curve # + % confined explosive mass

7 7 Multi-Energy method Determination of Blast class (curve #) based on: Ignition strength: High, Low Obstruction: High, Low, None Parallel plane confinement: Yes, No / only ground surface Estimation of % confined mass of the cloud Blast strength category Ignition strength (High / Low) Obstruction (High / Low / None) Parallel plane (Confined / Unconfined) Class 1 H H C H H U 7 10 LFL footprint 3 L H C H L C H L U H N C L H U H N U L L C L L U L N C L N U 1 Only small part of cloud covers installations: is this 10%?? We need to estimate overlap LFL cloud AND congested area

8 8 GAME correlations Guidance on the Application of Multi Energy: a HSE-TNO project aimed at providing a quantitative relation to provide overpressure of VCE s Describes maximum overpressure as function of quantifiable parameters: P max = 0.84 (VBR * L p / D avg ) S L 2.7. D avg 0.7 (open 3D) P max = 3.38 (VBR * L p / D avg ) S L 2.7. D avg 0.7 With: P max = (Dimensionless) Maximum Overpressure VBR = Volume Blockage Ratio L p = Flame Path Length D avg = Average Diameter Obstacles S L = Laminar Burning Speed fuel (2D confinement)

9 9 GAME correlations Instead of estimating the Blast strength category (based on expert judgement), the maximum overpressure is calculated The GAME correlations were extensively validated!! TNO-ME method also provides dynamic pressure & pressure impulse curves The initial P max relates to starting point of curves: P max can be translated into a Representative curve #

10 10 Determining VCE damage zones Practical usage of GAME correlations P max => Blast Curve number representation Log interpolation: Peak overpressure, Dynamic pressure and Pressure Impulse vs. distance But what about the flame path length and confined explosive mass fraction? Overpressure [bar] Blast Curve 9 (Very strong deflagration) Blast Curve 10 (Detonation) GAME calculated; Distance from center mass of explosive cloud [m] Flame path L p and % Confined mass requires projection of flammable cloud on congestion area!

11 Area [m2] 11 Dispersion model connected to GAME A dispersion model is required to calculate Explosive mass in the cloud and Footprint of the LFL Cloud Dispersion models can report Mass in LFL cloud and Area of LFL cloud as F(time) Available dispersion models have been extended with reporting dynamic cloud = location, size and mass Explosive mass [kg] 9,000 8,500 8,000 7,500 7,000 6,500 6,000 5,500 5,000 4,500 4,000 3,500 3,000 2,500 2,000 1,500 1, Instantaneous release - Explosive mass vs. Time Instantaneous release - Area of the LFL cloud vs. Time Time [s] ,500 7,000 6,500 6,000 5,500 5,000 4,500 4,000 3,500 3,000 2,500 2,000 1,500 1,

12 12 Interaction of LFL cloud & congestion areas The GAME method requires to define congestion areas (with properties VBR and D avg ) The (moving) LFL cloud is projected upon congestion areas The overlap of LFL cloud and congestion area determines explosion strength: Overlap region = Explosion region LFL cloud as function (time) Max flame path length Cloud size determines explosive mass involved VBR and D taken from area: overpressure contours Overpressure contours resulting explosion in centre congested area Release point Congested area size determines mass involved VBR and D taken from area: overpressure contours

13 13 Calculation procedure 1. Define release location, Chemical, and Loss of Containment event (Instantaneous, Leak, Rupture) 2. Define environmental conditions (temperatures, wind speed, stability class, surface roughness) 3. Define potential congestion areas (polygon on the map with typical VBR and D properties) 4. Calculate source term/rate and conditions 5. Perform dispersion calculation (LFL mass, area and location as function time) 6. Calculate maximum expl. mass in LFL cloud overlap with congestion areas: (Confined explosive mass, Flame path length) 7. Calculate overpressure contours (corresponding to worst case confined mass, congestion area properties)

14 14 Example procedure Project LFL cloud on congestion area Explosion region (red contour) determines %confined and flame path length First assumption: explosion centre in centre of gravity explosion region

15 15 Remaining choice: explosion centre The explosion centre determines the damage range! The explosion centre: anywhere in the explosion region The explosion region: (almost) anywhere in congestion area Construct the overpressure contour (example 0.1 bar) around the full congestion area!

16 16 Limits for explosion centre Part of congestion areas can be out of reach of LFL concentrations The explosion centre location is limited to max LFL distance Construct the overpressure contour around the congestion area within LFL!

17 17 Conclusions OK: A practical, quick and thus highly feasible method has been developed to create overpressure contours for total site analysis OK: The usage of the GAME correlations avoids the need of expert judgment in selecting blast curves, providing a more transparent and traceable blast pressure calculation OK: The method described can now also be extended with damage calculations on receiving objects (using vulnerability criteria for buildings or constructions)

18 18 Conclusions To Do: The explosion region method can be extended with the concept of Critical Separation Distance Note: The GAME method requires detailed knowledge of site congestion areas with parameters VBR and D avg Note: not a real 3D modelling; does not involve height : LFL cloud and congestion areas are 2D projections. (Height area is used as max volume limit) Be aware: The empirical dispersion models don t account for cloud displacement (concentration deviations) due to large obstacles (requires real 3D modelling of surroundings: a CFD calculation for multiple wind directions) Method remains an estimation of reality we simply gained improved realism

19 19 Finally Thank you for your attention Any questions??

A SOFTWARE MODEL FOR ASSESSING FATALITY RISK FROM EXPLOSION HAZARDS USING THE MULTI ENERGY METHOD AND BAKER STREHLOW TANG APPROACH

A SOFTWARE MODEL FOR ASSESSING FATALITY RISK FROM EXPLOSION HAZARDS USING THE MULTI ENERGY METHOD AND BAKER STREHLOW TANG APPROACH A SOFTWARE MODEL FOR ASSESSING FATALITY RISK FROM EXPLOSION HAZARDS USING THE MULTI ENERGY METHOD AND BAKER STREHLOW TANG APPROACH Nic Cavanagh 1, Yongfu Xu 2 and David Worthington 3 1 Head of Safeti Product

More information

Using CFD in Platform Design

Using CFD in Platform Design Using CFD in Platform Design Eric Peterson, PhD. Principal Consultant Quantitative Risk Analyst Scandpower Inc., Houston,TX Hans Nordstand, Scandpower Inc., Houston, TX Sverre Nodland, Scandpower Inc.,

More information

APPLICATION OF QUALITATIVE AND QUANTITATIVE RISK ANALYSIS TECHNIQUES TO BUILDING SITING STUDIES

APPLICATION OF QUALITATIVE AND QUANTITATIVE RISK ANALYSIS TECHNIQUES TO BUILDING SITING STUDIES APPLICATION OF QUALITATIVE AND QUANTITATIVE RISK ANALYSIS TECHNIQUES TO BUILDING SITING STUDIES John B. Cornwell, Jeffrey D. Marx, and Wilbert W. Lee Presented At 1998 Process Plant Safety Symposium Houston,

More information

Consequence Analysis: Comparison of Methodologies under API Standard and Commercial Software

Consequence Analysis: Comparison of Methodologies under API Standard and Commercial Software 511 A publication of CHEMICAL ENGINEERING TRANSACTIONS VOL. 36, 2014 Guest Editors: Valerio Cozzani, Eddy de Rademaeker Copyright 2014, AIDIC Servizi S.r.l., ISBN 978-88-95608-27-3; ISSN 2283-9216 The

More information

Assessment of Hydrocarbon Explosion and Fire Risks. Professor Jeom Paik. The LRET Research Collegium Southampton, 11 July 2 September 2011

Assessment of Hydrocarbon Explosion and Fire Risks. Professor Jeom Paik. The LRET Research Collegium Southampton, 11 July 2 September 2011 Assessment of Hydrocarbon Explosion and Fire Risks by Professor Jeom Paik The LRET Research Collegium Southampton, 11 July 2 September 2011 1 Assessment of Hydrocarbon Explosion and Fire Risks in Offshore

More information

REVIEW OF METHODS FOR ESTIMATING THE OVERPRESSURE AND IMPULSE RESULTING FROM A HYDROGEN EXPLOSION IN A CONFINED/OBSTRUCTED VOLUME

REVIEW OF METHODS FOR ESTIMATING THE OVERPRESSURE AND IMPULSE RESULTING FROM A HYDROGEN EXPLOSION IN A CONFINED/OBSTRUCTED VOLUME REVIEW OF METHODS FOR ESTIMATING THE OVERPRESSURE AND IMPULSE RESULTING FROM A HYDROGEN EXPLOSION IN A CONFINED/OBSTRUCTED VOLUME Mélani, L. 1,2, Sochet, I. 1, Rocourt, X. 1 and Jallais, S. 2 1 ENSI de

More information

A PROGRESSIVE RISK ASSESSMENT PROCESS FOR A TYPICAL CHEMICAL COMPANY: HOW TO AVOID THE RUSH TO QRA

A PROGRESSIVE RISK ASSESSMENT PROCESS FOR A TYPICAL CHEMICAL COMPANY: HOW TO AVOID THE RUSH TO QRA A PROGRESSIVE ASSESSMENT PROCESS FOR A TYPICAL CHEMICAL COMPANY: HOW TO AVOID THE RUSH TO QRA R. Gowland European Process Safety Centre, U.K. The Seveso Directive and the Establishment operators own internal

More information

Explosion Hazards of Hydrogen-Air Mixtures. Professor John H.S. Lee McGill University, Montreal, Canada

Explosion Hazards of Hydrogen-Air Mixtures. Professor John H.S. Lee McGill University, Montreal, Canada Explosion Hazards of Hydrogen-Air Mixtures Professor John H.S. Lee McGill University, Montreal, Canada Hydrogen Safety Issues Wide spread use of hydrogen requires significant efforts to resolve safety

More information

A Response Surface Model to Predict Flammable Gas Cloud Volume in Offshore Modules. Tatiele Dalfior Ferreira Sávio Souza Venâncio Vianna

A Response Surface Model to Predict Flammable Gas Cloud Volume in Offshore Modules. Tatiele Dalfior Ferreira Sávio Souza Venâncio Vianna A Response Surface Model to Predict Flammable Gas Cloud Volume in Offshore Modules Tatiele Dalfior Ferreira Sávio Souza Venâncio Vianna PRESENTATION TOPICS Research Group Overview; Problem Description;

More information

The ADREA-HF CFD code An overview

The ADREA-HF CFD code An overview The ADREA-HF CFD code An overview Dr. A.G. Venetsanos Environmental Research Laboratory (EREL) National Centre for Scientific Research Demokritos, Greece venets@ipta.demokritos.gr Slide 2 Computational

More information

CHAPTER 4: OFFSITE CONSEQUENCE ANALYSIS

CHAPTER 4: OFFSITE CONSEQUENCE ANALYSIS CHAPTER 4: OFFSITE CONSEQUENCE ANALYSIS RMP OFFSITE CONSEQUENCE ANALYSIS GUIDANCE This chapter is intended for people who plan to do their own air dispersion modeling. If you plan to do your own modeling,

More information

QUANTITATIVE RISK ASSESSMENT - QRA FOR

QUANTITATIVE RISK ASSESSMENT - QRA FOR QUANTITATIVE RISK ASSESSMENT - QRA FOR TOWN GAS COMPANY PART - II Pressure Reduction and Odorant Station at Greater Cairo Jan 2006 Report # PS-GZT-TG 001 Rev.0 PS-GZT-TG-001 Revision (1) Jan 2006 Table

More information

GAS DISPERSION WITH OPENFOAM

GAS DISPERSION WITH OPENFOAM GAS DISPERSION WITH OPENFOAM Chris Dixon Major Hazards Management Centre of Expertise October 2012 1 DEFINITIONS AND CAUTIONARY NOTE Resources: Our use of the term resources in this announcement includes

More information

ALOHA. Example Scenarios. August 2013

ALOHA. Example Scenarios. August 2013 The CAMEO Software Suite ALOHA Example Scenarios August 2013 National Oceanic and Atmospheric Administration Office of Response and Restoration Emergency Response Division Seattle, Washington E N V IR

More information

A Triple Bottom Line approach to QRA

A Triple Bottom Line approach to QRA A publication of CHEMICAL ENGINEERING TRANSACTIONS VOL. 26, 2012 Guest Editors: Valerio Cozzani, Eddy De Rademaeker Copyright 2012, AIDIC Servizi S.r.l., ISBN 978-88-95608-17-4; ISSN 1974-9791 The Italian

More information

LNG SAFETY MYTHS and LEGENDS

LNG SAFETY MYTHS and LEGENDS LNG SAFETY MYTHS and LEGENDS Doug Quillen ChevronTexaco Corp. Natural Gas Technology Investment in a Healthy U.S. Energy Future May 14-15, 2002 Houston Introduction North America is Becoming the Focal

More information

VAPOUR CLOUD EXPLOSION RISK MANAGEMENT IN ONSHORE PLANT USING EXPLOSION EXCEEDANCE TECHNIQUES

VAPOUR CLOUD EXPLOSION RISK MANAGEMENT IN ONSHORE PLANT USING EXPLOSION EXCEEDANCE TECHNIQUES VAPOUR CLOUD EXPLOSION RISK MANAGEMENT IN ONSHORE PLANT USING EXPLOSION EXCEEDANCE TECHNIQUES G.A. Chamberlain and J.S. Puttock Shell Global Solutions UK 1 Cheshire Innovation Park, P.O. Box 1, Chester,

More information

Safety issues of hydrogen in vehicles Frano Barbir Energy Partners 1501 Northpoint Pkwy, #102 West Palm Beach, FL 33407, U.S.A.

Safety issues of hydrogen in vehicles Frano Barbir Energy Partners 1501 Northpoint Pkwy, #102 West Palm Beach, FL 33407, U.S.A. Safety issues of hydrogen in vehicles Frano Barbir Energy Partners 1501 Northpoint Pkwy, #102 West Palm Beach, FL 33407, U.S.A. Properties of hydrogen Hydrogen is an odorless, colorless gas. With molecular

More information

Is This Combustible Dust?

Is This Combustible Dust? 1 of 5 8/6/2012 1:16 PM Is This Combustible Dust? Thursday, 19 July 2012 Dust explosions and fires are serious hazards in the process industries that have lead to loss of life, injury to plant personnel

More information

Major Hazard Risk Assessment on Ammonia Storage at Jordan Phosphate Mines Company (JPMC) in Aqaba, Jordan

Major Hazard Risk Assessment on Ammonia Storage at Jordan Phosphate Mines Company (JPMC) in Aqaba, Jordan Major Hazard Risk Assessment on Ammonia Storage at Jordan Phosphate Mines Company (JPMC) in Aqaba, Jordan Jehan Haddad, Salah Abu Salah, Mohammad Mosa, Royal Scientific Society, Jordan Pablo Lerena, Swiss

More information

The Behaviour Of Vertical Jet Fires Under Sonic And Subsonic Regimes

The Behaviour Of Vertical Jet Fires Under Sonic And Subsonic Regimes The Behaviour Of Vertical Jet Fires Under Sonic And Subsonic Regimes Palacios A. and Casal J. Centre for Technological Risk Studies (CERTEC), Department of Chemical Engineering, Universitat Politècnica

More information

Information for HFO-1234yf Automotive Plant and Service Shop Implementation

Information for HFO-1234yf Automotive Plant and Service Shop Implementation Information for HFO-1234yf Automotive Plant and Service Shop Implementation Mary Koban, Automotive Sr Technical Engineer DuPont Fluoroproducts, Wilmington,DE 2 Agenda HFO-1234yf Properties Flammability

More information

Supporting document to NORSOK Standard C-004, Edition 2, May 2013, Section 5.4 Hot air flow

Supporting document to NORSOK Standard C-004, Edition 2, May 2013, Section 5.4 Hot air flow 1 of 9 Supporting document to NORSOK Standard C-004, Edition 2, May 2013, Section 5.4 Hot air flow A method utilizing Computational Fluid Dynamics (CFD) codes for determination of acceptable risk level

More information

Risk Assessment Data Directory. Report No. 434 7 March 2010. Consequence modelling

Risk Assessment Data Directory. Report No. 434 7 March 2010. Consequence modelling Risk Assessment Data Directory Report No. 434 7 March 2010 Consequence modelling I n t e r n a t i o n a l A s s o c i a t i o n o f O i l & G a s P r o d u c e r s P ublications Global experience The

More information

Calculation of Liquefied Natural Gas (LNG) Burning Rates

Calculation of Liquefied Natural Gas (LNG) Burning Rates Calculation of Liquefied Natural Gas (LNG) Burning Rates Carolina Herrera, R. Mentzer, M. Sam Mannan, and S. Waldram Mary Kay O Connor Process Safety Center Artie McFerrin Department of Chemical Engineering

More information

CFD Simulation of HSDI Engine Combustion Using VECTIS

CFD Simulation of HSDI Engine Combustion Using VECTIS CFD Simulation of HSDI Engine Combustion Using VECTIS G. Li, S.M. Sapsford Ricardo Consulting Engineer s Ltd., Shoreham-by-Sea, UK ABSTRACT As part of the VECTIS code validation programme, CFD simulations

More information

Do you speak SAFETY?

Do you speak SAFETY? Do you speak SAFETY? Convegno:Terminologie specialistiche e prodotti terminologici Orvieto 28-29 maggio 2010 1 Leadership in Safety: le sette aspettative 1. Creazione della Safety Vision 2. Costante focalizzazione

More information

VIII.1 Hydrogen Behavior and Quantitative Risk Assessment

VIII.1 Hydrogen Behavior and Quantitative Risk Assessment VIII.1 Hydrogen Behavior and Quantitative Risk Assessment Katrina Groth (Primary Contact), Ethan Hecht, Chris LaFleur, Alice Muna, John Reynolds (SAIC) Sandia National Laboratories (SNL) P.O. Box 5800

More information

QUANTITATIVE RISK ASSESSMENT FOR ACCIDENTS AT WORK IN THE CHEMICAL INDUSTRY AND THE SEVESO II DIRECTIVE

QUANTITATIVE RISK ASSESSMENT FOR ACCIDENTS AT WORK IN THE CHEMICAL INDUSTRY AND THE SEVESO II DIRECTIVE QUANTITATIVE RISK ASSESSMENT FOR ACCIDENTS AT WORK IN THE CHEMICAL INDUSTRY AND THE SEVESO II DIRECTIVE I. A. PAPAZOGLOU System Reliability and Industrial Safety Laboratory National Center for Scientific

More information

Derivation of Risk Areas Associated with High-Pressure Natural-Gas Pipelines Explosions Including Effects on Structural Components

Derivation of Risk Areas Associated with High-Pressure Natural-Gas Pipelines Explosions Including Effects on Structural Components 289 A publication of VOL. 36, 2014 CHEMICAL ENGINEERING TRANSACTIONS Guest Editors: Valerio Cozzani, Eddy de Rademaeker Copyright 2014, AIDIC Servizi S.r.l., ISBN 978-88-95608-27-3; ISSN 2283-9216 The

More information

COMBUSTIBLE DUST EXPLOSIONS

COMBUSTIBLE DUST EXPLOSIONS COMBUSTIBLE DUST EXPLOSIONS Most people would not think that dust made up of ordinary materials such as food could explode, but under certain circumstances it can. On 7 February 2008, a violent explosion

More information

Risk Analysis of Gas Explosions on Oil Platforms

Risk Analysis of Gas Explosions on Oil Platforms Risk Analysis of Gas Explosions on Oil Platforms Christian Linde Olsen Griffith University, Faculty of Engineering and Information Technology, Gold Coast Campus. Abstract Risk analysis of gas explosion

More information

Ontario Fire Code SECTION 5.13 DIP TANKS. Illustrated Commentary. Office of the Ontario Fire Marshal

Ontario Fire Code SECTION 5.13 DIP TANKS. Illustrated Commentary. Office of the Ontario Fire Marshal Ontario Fire Code SECTION 5.13 DIP TANKS Illustrated Commentary Office of the Ontario Fire Marshal Dip Tanks Illustrated Commentary 1 5.13.1. Location 5.13.1.1. Dip tank operations involving flammable

More information

FLACS TRAINING OVERVIEW

FLACS TRAINING OVERVIEW FLACS TRAINING OVERVIEW FLACS SOFTWARE FLACS Software is focusing on producing and distributing a complete and advanced, well validated and recognized software solution for CFD modeling in ventilation,

More information

Modelling of fire spread in car parks

Modelling of fire spread in car parks Modelling of fire spread in car parks Leander Noordijk TNO Centre for Fire Research, Delft, the Netherlands Tony Lemaire TNO Centre for Fire Research, Delft, the Netherlands Currently, design codes assume

More information

Characteristic overpressure impulse distance curves for vapour cloud explosions using the TNO Multi-Energy model

Characteristic overpressure impulse distance curves for vapour cloud explosions using the TNO Multi-Energy model Journal of Hazardous Materials A137 (2006) 734 741 Characteristic overpressure impulse distance curves for vapour cloud explosions using the TNO Multi-Energy model Fernando Díaz Alonso a,, Enrique González

More information

How To Run A Cdef Simulation

How To Run A Cdef Simulation Simple CFD Simulations and Visualisation using OpenFOAM and ParaView Sachiko Arvelius, PhD Purpose of this presentation To show my competence in CFD (Computational Fluid Dynamics) simulation and visualisation

More information

INITIAL ASSESSMENT OF THE IMPACT OF JET FLAME HAZARD FROM HYDROGEN CARS IN ROAD TUNNELS AND THE IMPLICATION ON HYDROGEN CAR DESIGN

INITIAL ASSESSMENT OF THE IMPACT OF JET FLAME HAZARD FROM HYDROGEN CARS IN ROAD TUNNELS AND THE IMPLICATION ON HYDROGEN CAR DESIGN INITIAL ASSESSMENT OF THE IMPACT OF JET FLAME HAZARD FROM HYDROGEN CARS IN ROAD TUNNELS AND THE IMPLICATION ON HYDROGEN CAR DESIGN Wu, Y Department of Chemical and Process Engineering, University of Sheffield,

More information

APPENDIX H7: POOL SPREAD AREAS FOR INSTANTANEOUS TANK FAILURE

APPENDIX H7: POOL SPREAD AREAS FOR INSTANTANEOUS TANK FAILURE APPENDIX H7: POOL SPREAD AREAS FOR INSTANTANEOUS TANK FAILURE H7.1 Introduction H7.1.1.1 The extent of flow of liquid from a instantaneous tank failure has been assessed based on the physical modelling

More information

Dimensional analysis is a method for reducing the number and complexity of experimental variables that affect a given physical phenomena.

Dimensional analysis is a method for reducing the number and complexity of experimental variables that affect a given physical phenomena. Dimensional Analysis and Similarity Dimensional analysis is very useful for planning, presentation, and interpretation of experimental data. As discussed previously, most practical fluid mechanics problems

More information

IGEM/UP/16 Communication 1756

IGEM/UP/16 Communication 1756 Communication 1756 Design for Natural Gas installations on industrial and commercial premises with respect to hazardous area classification and preparation of risk assessments Founded 1863 Royal Charter

More information

RISK ENGINEERING MANAGING RISK INTELLIGENTLY

RISK ENGINEERING MANAGING RISK INTELLIGENTLY RISK ENGINEERING MANAGING RISK INTELLIGENTLY OMAN RISK ENGINEERING SEMINAR 13 OCTOBER 2015 Adrian Louis BEng CEng MIChemE Risk Engineer Dubai - Marsh Emirates Agenda Introduction Risk Management Framework

More information

Annex H. Quantitative Risk Assessment Specialist Report

Annex H. Quantitative Risk Assessment Specialist Report Annex H Quantitative Risk Assessment Specialist Report Burgan Oil Cape Terminal Major Hazard Installation Risk Assessment for EIA v4.0 Ref: 0220778 MHI 0012 EXECUTIVE SUMMARY Burgan Oil Cape Terminal

More information

Onshore Explosion Studies Benefits of CFD-Modelling

Onshore Explosion Studies Benefits of CFD-Modelling 205 A publication of CHEMICAL ENGINEERING TRANSACTIONS VOL. 31, 2013 Guest Editors: Eddy De Rademaeker, Bruno Fabiano, Simberto Senni Buratti Copyright 2013, AIDIC Servizi S.r.l., ISBN 978-88-95608-22-8;

More information

Technical documentation and software quality assurance for project Eagle-ALOHA

Technical documentation and software quality assurance for project Eagle-ALOHA Technical documentation and software quality assurance for project Eagle-ALOHA A project to add fire and explosive capability to ALOHA FEBRUARY 2006 This report summarizes the technical details and quality

More information

Using the Linear Risk Integral (LRI) approach in pipeline QRA for a better application of risk mitigation measures

Using the Linear Risk Integral (LRI) approach in pipeline QRA for a better application of risk mitigation measures Using the Linear Risk Integral (LRI) approach in pipeline QRA for a better application of risk mitigation measures Urban Neunert, ILF Consulting Engineers, Germany Abstract Minimizing the risks resulting

More information

HSE information sheet. Fire and explosion hazards in offshore gas turbines. Offshore Information Sheet No. 10/2008

HSE information sheet. Fire and explosion hazards in offshore gas turbines. Offshore Information Sheet No. 10/2008 HSE information sheet Fire and explosion hazards in offshore gas turbines Offshore Information Sheet No. 10/2008 Contents Introduction.. 2 Background of gas turbine incidents in the UK offshore sector...2

More information

Austin Peay State University Department of Chemistry Chem 1111. The Use of the Spectrophotometer and Beer's Law

Austin Peay State University Department of Chemistry Chem 1111. The Use of the Spectrophotometer and Beer's Law Purpose To become familiar with using a spectrophotometer and gain an understanding of Beer s law and it s relationship to solution concentration. Introduction Scientists use many methods to determine

More information

CFD Computational Fluid Dynamics

CFD Computational Fluid Dynamics CFD Computational Fluid Dynamics Norconsult is both highly competent and has a broad experience in the 3D simulation of fluid flows. The section for Applied Fluid Dynamics utilises CFD in a multi-discipline

More information

Energy transformations

Energy transformations Energy transformations Objectives Describe examples of energy transformations. Demonstrate and apply the law of conservation of energy to a system involving a vertical spring and mass. Design and implement

More information

Methods of Avoiding Tank Bund Overtopping Using

Methods of Avoiding Tank Bund Overtopping Using Methods of Avoiding Tank Bund Overtopping Using Computational Fluid Dynamics Tool SreeRaj R Nair Senior Engineer, Aker Kvaerner Consultancy Services Aker Kvaerner, Ashmore House, Richardson Road, Stockton

More information

Aeroelastic Investigation of the Sandia 100m Blade Using Computational Fluid Dynamics

Aeroelastic Investigation of the Sandia 100m Blade Using Computational Fluid Dynamics Aeroelastic Investigation of the Sandia 100m Blade Using Computational Fluid Dynamics David Corson Altair Engineering, Inc. Todd Griffith Sandia National Laboratories Tom Ashwill (Retired) Sandia National

More information

Hazard and Risk Assessment

Hazard and Risk Assessment Appendix C Hazard and Risk Assessment C1 Preliminary Hazard Analysis C2 Kurnell Buncefield Review Appendix 1 Preliminary Hazard Analysis Caltex Refineries (NSW) Pty Ltd Proposed Kurnell Product Terminal

More information

RR630. Area classification for secondary releases from low pressure natural gas systems

RR630. Area classification for secondary releases from low pressure natural gas systems Health and Safety Executive Area classification for secondary releases from low pressure natural gas systems Prepared by the Health and Safety Laboratory for the Health and Safety Executive 2008 RR630

More information

Recommendations Regarding the Handling of Norit GL 50 in Flue Gas Clean up Systems

Recommendations Regarding the Handling of Norit GL 50 in Flue Gas Clean up Systems Technical Bulletin Gas & Air Recommendations Regarding the Handling of Norit GL 50 in Flue Gas Clean up Systems 1. Introduction Norit GL 50 is a powdered activated carbon widely used for the removal of

More information

AREA CLASSIFICATION OF NATURAL GAS INSTALLATIONS

AREA CLASSIFICATION OF NATURAL GAS INSTALLATIONS AREA CLASSIFICATION OF NATURAL GAS INSTALLATIONS R C Santon and M J Ivings Health and Safety Laboratory, Harpur Hill, Buxton, SK17 6PJ Whilst area classification has been applied in the past to high pressure

More information

NUMERICAL ANALYSIS OF THE EFFECTS OF WIND ON BUILDING STRUCTURES

NUMERICAL ANALYSIS OF THE EFFECTS OF WIND ON BUILDING STRUCTURES Vol. XX 2012 No. 4 28 34 J. ŠIMIČEK O. HUBOVÁ NUMERICAL ANALYSIS OF THE EFFECTS OF WIND ON BUILDING STRUCTURES Jozef ŠIMIČEK email: jozef.simicek@stuba.sk Research field: Statics and Dynamics Fluids mechanics

More information

New Revised European Norm on Dust Explosion Venting Protection Systems EN 14491

New Revised European Norm on Dust Explosion Venting Protection Systems EN 14491 A publication of CHEMICAL ENGINEERINGTRANSACTIONS VOL. 26, 2012 Guest Editors:ValerioCozzani, Eddy De Rademaeker Copyright 2012, AIDIC Servizi S.r.l., ISBN 978-88-95608-17-4; ISSN 1974-9791 The Italian

More information

JOINT CBA AND SIA GUIDANCE FOR THE STORAGE OF FLAMMABLE LIQUIDS IN SEALED PACKAGES IN SPECIFIED EXTERNAL STORAGE AREAS

JOINT CBA AND SIA GUIDANCE FOR THE STORAGE OF FLAMMABLE LIQUIDS IN SEALED PACKAGES IN SPECIFIED EXTERNAL STORAGE AREAS JOINT CBA AND SIA GUIDANCE FOR THE STORAGE OF FLAMMABLE LIQUIDS IN SEALED PACKAGES IN SPECIFIED EXTERNAL STORAGE AREAS 1 JOINT CBA AND SIA GUIDANCE FOR THE STORAGE OF FLAMMABLE LIQUIDS IN SEALED PACKAGES

More information

Population Vulnerability Assessment around a LPG Storage and Distribution Facility near Cochin using ALOHA And GIS

Population Vulnerability Assessment around a LPG Storage and Distribution Facility near Cochin using ALOHA And GIS International Journal of Engineering Science Invention ISSN (Online): 2319 6734, ISSN (Print): 2319 6726 Volume 4 Issue 6 June 2015 PP.23-31 Population Vulnerability Assessment around a LPG Storage and

More information

FLAMMABLE LIQUIDS COMPLIANCE NOTE

FLAMMABLE LIQUIDS COMPLIANCE NOTE Issued by: Heather Rice Page: 1 of 7 COMPLIANCE NOTE INTRODUCTION This document provides additional guidance to support the Arrangement on Flammable Liquids (Ref No. CYC/HS/A27) CONTENTS Section Topic

More information

Combustible Dust Booklet

Combustible Dust Booklet Introduction In general, over 70% of organic dusts are explosible if given an adequate ignition source and appropriate dust/air concentration. Unless the material is combustible and finely divided (generally

More information

Passive & Active Design

Passive & Active Design Passive & Active Design CIBSE Building Simulations Group Peter A. Brown CEng, MBA October 2010 Introduction Passive & Active Design Introduction What are the interactions between passive and active design?

More information

HEAT TRANSFER ANALYSIS IN A 3D SQUARE CHANNEL LAMINAR FLOW WITH USING BAFFLES 1 Vikram Bishnoi

HEAT TRANSFER ANALYSIS IN A 3D SQUARE CHANNEL LAMINAR FLOW WITH USING BAFFLES 1 Vikram Bishnoi HEAT TRANSFER ANALYSIS IN A 3D SQUARE CHANNEL LAMINAR FLOW WITH USING BAFFLES 1 Vikram Bishnoi 2 Rajesh Dudi 1 Scholar and 2 Assistant Professor,Department of Mechanical Engineering, OITM, Hisar (Haryana)

More information

Analysis of the UNH Data Center Using CFD Modeling

Analysis of the UNH Data Center Using CFD Modeling Applied Math Modeling White Paper Analysis of the UNH Data Center Using CFD Modeling By Jamie Bemis, Dana Etherington, and Mike Osienski, Department of Mechanical Engineering, University of New Hampshire,

More information

Nuclear Detonation Calculator

Nuclear Detonation Calculator Nuclear Detonation Calculator In last month s newsletter, February 2007, I discussed the Fallout Radiation Dose Calculator that was a new feature in the in the latest version of the PEAC-WMD software released

More information

EMERGENCY VESSELS BLOWDOWN SIMULATIONS

EMERGENCY VESSELS BLOWDOWN SIMULATIONS EMERGENCY VESSELS BLOWDOWN SIMULATIONS AGENDA INTRODUCTION TYPICAL FIRST STUDIES IN TOTAL UPSTREAM INTERNAL RULES BASED ON API METHODOLOGY STUDY RESULTS DEVELOPMENT WORK - COLLABORATION BETWEEN SIMSCI

More information

An experimental study of temperatures in cloud from release of flashing liquid CO 2 in 3m long channel

An experimental study of temperatures in cloud from release of flashing liquid CO 2 in 3m long channel INTERNATIONAL JOURNAL OF ENERGY AND ENVIRONMENT Volume 5, Issue 5, 214 pp.567-574 Journal homepage: www.ijee.ieefoundation.org An experimental study of temperatures in cloud from release of flashing liquid

More information

Risk Assessment Data Directory. Report No. 434 6.1 March 2010. Ignition probabilities

Risk Assessment Data Directory. Report No. 434 6.1 March 2010. Ignition probabilities Risk Assessment Data Directory Report No. 434 6.1 March 2010 Ignition probabilities I n t e r n a t i o n a l A s s o c i a t i o n o f O i l & G a s P r o d u c e r s P ublications Global experience The

More information

TOXIC AND FLAMMABLE GAS CLOUD DETECTORS LAYOUT OPTIMIZATION USING CFD

TOXIC AND FLAMMABLE GAS CLOUD DETECTORS LAYOUT OPTIMIZATION USING CFD Introduction to the case Gas detectors are commonly installed in process facilities to automatically alarm and trigger safety measures in response to hazardous leaks. Without effective leak detection,

More information

Work and Energy. Work = Force Distance. Work increases the energy of an object. Energy can be converted back to work.

Work and Energy. Work = Force Distance. Work increases the energy of an object. Energy can be converted back to work. Work and Energy Ch. 6 Work = Force Distance Work increases the energy of an object. Energy can be converted back to work. Therefore, energy and work have the same unit: Newton meter = Nm Energy per gram,

More information

Combustible Dust Ensuring Safety and Compliance. Brian Edwards, PE Conversion Technology Inc. ENVIRONMENTAL & SAFETY CONSULTING ENGINEERS

Combustible Dust Ensuring Safety and Compliance. Brian Edwards, PE Conversion Technology Inc. ENVIRONMENTAL & SAFETY CONSULTING ENGINEERS Combustible Dust Ensuring Safety and Compliance Prepared for: REGION IV VPPPA Presented by: Brian Edwards, PE Conversion Technology Inc. ENVIRONMENTAL & SAFETY CONSULTING ENGINEERS 1 Scope of Discussion

More information

ESReDA Working Group on Fire Risk Analysis

ESReDA Working Group on Fire Risk Analysis Rev. 0 - SEPTEMBER 2009 ESReDA Working Group on Fire Risk Analysis Fire Risk Analysis Process and Oil & Gas Industries Standard and Regulations, State of the Art & Methodologies D'Appolonia Contribution

More information

Hazardous Substance Class Definitions & Labels

Hazardous Substance Class Definitions & Labels Hazardous Substance Class Definitions & Labels In the IMDG Code, substances are divided into 9 classes. A substance with multiple hazards has one 'Primary Class' and one or more 'Subsidiary Risks'. Some

More information

Fire, Explosion and Risk Assessment Topic Guidance Issue 1

Fire, Explosion and Risk Assessment Topic Guidance Issue 1 Hazard Installations Directorate Offshore Division Fire, Explosion and Risk Assessment Topic Guidance Issue 1 Revision sheet Issue Description Date 1 First issue February 2003 Overview of Topic Guidance

More information

Explosion of a gasoline vapour cloud formed in a hydrocarbon loaded effluents storage tank 10 December 1999 Arquata Scrivia Italy

Explosion of a gasoline vapour cloud formed in a hydrocarbon loaded effluents storage tank 10 December 1999 Arquata Scrivia Italy Explosion of a gasoline vapour cloud formed in a hydrocarbon loaded effluents storage tank 10 December 1999 Arquata Scrivia Italy UVCE Storage tank Hydrocarbons Steam coil Corrosion Steam Instrumentation

More information

Seismic Risk Assessment Procedures for a System consisting of Distributed Facilities -Part three- Insurance Portfolio Analysis

Seismic Risk Assessment Procedures for a System consisting of Distributed Facilities -Part three- Insurance Portfolio Analysis Seismic Risk Assessment Procedures for a System consisting of Distributed Facilities -Part three- Insurance Portfolio Analysis M. Achiwa & M. Sato Yasuda Risk Engineering Co., Ltd., Tokyo, Japan M. Mizutani

More information

FAC 2.1: Data Center Cooling Simulation. Jacob Harris, Application Engineer Yue Ma, Senior Product Manager

FAC 2.1: Data Center Cooling Simulation. Jacob Harris, Application Engineer Yue Ma, Senior Product Manager FAC 2.1: Data Center Cooling Simulation Jacob Harris, Application Engineer Yue Ma, Senior Product Manager FAC 2.1: Data Center Cooling Simulation Computational Fluid Dynamics (CFD) can be used to numerically

More information

QUANTITATIVE RISK ASSESSMENT AND MODELING: FIRE RISKS OF CNG-POWERED BUSES

QUANTITATIVE RISK ASSESSMENT AND MODELING: FIRE RISKS OF CNG-POWERED BUSES QUANTITATIVE RISK ASSESSMENT AND MODELING: FIRE RISKS OF CNG-POWERED BUSES Mohammad Modarres Minta Martin Professor of Engineering Director, Reliability Engineering Program Department of Mechanical Engineering

More information

(1) 2 TEST SETUP. Table 1 Summary of models used for calculating roughness parameters Model Published z 0 / H d/h

(1) 2 TEST SETUP. Table 1 Summary of models used for calculating roughness parameters Model Published z 0 / H d/h Estimation of Surface Roughness using CFD Simulation Daniel Abdi a, Girma T. Bitsuamlak b a Research Assistant, Department of Civil and Environmental Engineering, FIU, Miami, FL, USA, dabdi001@fiu.edu

More information

Eksplosjonsrisiko, værbeskyttelse og optimalisering av design

Eksplosjonsrisiko, værbeskyttelse og optimalisering av design OIL & GAS Eksplosjonsrisiko, værbeskyttelse og optimalisering av design HMS utfordringer i Nordområdene Arbeidsseminar 4 Asmund Huser 20 May 2014 1 DNV GL 2013 20 May 2014 SAFER, SMARTER, GREENER Content

More information

Belgian Stress tests specifications Applicable to all nuclear plants, excluding power reactors 22 June 2011

Belgian Stress tests specifications Applicable to all nuclear plants, excluding power reactors 22 June 2011 Belgian Stress tests specifications Applicable to all nuclear plants, excluding power reactors 22 June 2011 Introduction Considering the accident at the Fukushima nuclear power plant in Japan, the European

More information

WEEKLY SAFETY MEETING All Euramax Subsidiaries COMBUSTIBLE DUST. Safety Meeting Contents. Meeting Notice. Leaders Guide.

WEEKLY SAFETY MEETING All Euramax Subsidiaries COMBUSTIBLE DUST. Safety Meeting Contents. Meeting Notice. Leaders Guide. Safety Meeting Contents Meeting Notice Leaders Guide Employee Handout Employee Quiz Meeting Sign-In Sheet Employee Puzzle PRIOR TO THE WEEKLY MEETING: - Post the meeting notice by the timeclock - Read

More information

Natural Gas Information Contents

Natural Gas Information Contents Natural Gas Information Contents What is natural gas Natural Gas Components Physical Properties of Natural Gas Different Forms of Natural Gas The Use of Natural Gas Co-generation System Natural Gas and

More information

Explosion Prevention

Explosion Prevention Explosion Prevention Question: Many food and industrial products produced by member companies are dry powders or crystals. If mishandled, some of these products may form an explosive mixture of air and

More information

FNT EXPERT PAPER. // Data Center Efficiency AUTHOR. Using CFD to Optimize Cooling in Design and Operation. www.fntsoftware.com

FNT EXPERT PAPER. // Data Center Efficiency AUTHOR. Using CFD to Optimize Cooling in Design and Operation. www.fntsoftware.com FNT EXPERT PAPER AUTHOR Oliver Lindner Head of Business Line DCIM FNT GmbH // Data Center Efficiency Using CFD to Optimize Cooling in Design and Operation Energy is the biggest cost factor with the highest

More information

THE DDESB BLAST EFFECTS COMPUTER VERSION 4.0

THE DDESB BLAST EFFECTS COMPUTER VERSION 4.0 BECv4 The DDESB Blast Effects Computer Version 4.0, Swisdak, Michael M., and Ward, Jerry M., Minutes of the 29 th DoD Explosives Safety Seminar, July 2000. THE DDESB BLAST EFFECTS COMPUTER VERSION 4.0

More information

On-Site Risk Management Audit Checklist for Program Level 3 Process

On-Site Risk Management Audit Checklist for Program Level 3 Process On-Site Risk Management Audit Checklist for Program Level 3 Process Auditor name: Date: I. Facility Information: Facility name: Facility location: County: Contact name: RMP Facility I.D. Phone Number:

More information

Bharat Petroleum Corporation Limited,

Bharat Petroleum Corporation Limited, Bharat Petroleum Corporation Limited, Ennore Installation, Survey No: 1556 B Vallur village and 354/1 Athipattu village, Chennai 600081 RECEIPT, STORAGE & DISTRIBUTION OF MOTOR SPIRIT (MS), HIGH SPEED

More information

Your Boiler Room: A Time Bomb?

Your Boiler Room: A Time Bomb? Your Boiler Room: A Time Bomb? Is you boiler room a potential Time Bomb? A few basics you need to know to work safely in the boiler room: Two potentials for explosions in a boiler room: Water/steam side

More information

How to be Sure Your Dust Collector Design and Installation are NFPA Compliant. Presented by: Jeff Kice Kice Industries, Inc.

How to be Sure Your Dust Collector Design and Installation are NFPA Compliant. Presented by: Jeff Kice Kice Industries, Inc. How to be Sure Your Dust Collector Design and Installation are NFPA Compliant Presented by: Jeff Kice Kice Industries, Inc. Who is the NFPA? National Fire Protection Association Nonprofit international

More information

Challenges for Use of Fixed Fire Suppression Systems in Road Tunnel Fire Protection

Challenges for Use of Fixed Fire Suppression Systems in Road Tunnel Fire Protection Challenges for Use of Fixed Fire Suppression Systems in Road Tunnel Fire Protection Z. G. Liu *, A. Kashef, G. Lougheed, and A. K. Kim Fire Research Program, Institute for Research in Construction National

More information

HAZARDOUS AREA CLASSIFICATION OF LOW PRESSURE NATURAL GAS SYSTEMS USING CFD PREDICTIONS

HAZARDOUS AREA CLASSIFICATION OF LOW PRESSURE NATURAL GAS SYSTEMS USING CFD PREDICTIONS HAZARDOUS AREA CLASSIFICATION OF LOW PRESSURE NATURAL GAS SYSTEMS USING CFD PREDICTIONS Gant S.E. 1, Ivings M.J. 1, Jones A. 2, and Santon R. 1 1 Health and Safety Laboratory, Harpur Hill, Buxton, SK17

More information

A Review of HSE s Risk Analysis and Protection Based Analysis Approaches for Land-Use Planning. Final Report

A Review of HSE s Risk Analysis and Protection Based Analysis Approaches for Land-Use Planning. Final Report A Review of HSE s Risk Analysis and Protection Based Analysis Approaches for Land-Use Planning Final Report www.erm.com September 2004 Delivering sustainable solutions in a more competitive world HSE A

More information

How To Safely Dig For Natural Gas

How To Safely Dig For Natural Gas PNG DIAL B4-U-DIG book_final_nu 5/1/05 3:24 PM Page 2 Phoenix Natural Gas,197 Airport Road West, Belfast BT3 9ED. Tel. 08454 55 55 55. www.phoenix-natural-gas.com PNG DIAL B4-U-DIG book_final_nu 5/1/05

More information

The Earth, Sun, and Moon

The Earth, Sun, and Moon reflect The Sun and Moon are Earth s constant companions. We bask in the Sun s heat and light. It provides Earth s energy, and life could not exist without it. We rely on the Moon to light dark nights.

More information

MSC/Circ.1002 26 June 2001 GUIDELINES ON ALTERNATIVE DESIGN AND ARRANGEMENTS FOR FIRE SAFETY

MSC/Circ.1002 26 June 2001 GUIDELINES ON ALTERNATIVE DESIGN AND ARRANGEMENTS FOR FIRE SAFETY INTERNATIONAL MARITIME ORGANIZATION 4 ALBERT EMBANKMENT LONDON SE1 7SR Telephone: 020 7735 7611 Fax: 020 7587 3210 Telex: 23588 IMOLDN G IMO E Ref. MSC/Circ.1002 26 June 2001 GUIDELINES ON ALTERNATIVE

More information

General Physical Science

General Physical Science General Physical Science Chapter 4 Work and Energy Work The work done by a constant force F acting upon an object is the product of the magnitude of the force (or component of the force) and the parallel

More information

Learning Module 4 - Thermal Fluid Analysis Note: LM4 is still in progress. This version contains only 3 tutorials.

Learning Module 4 - Thermal Fluid Analysis Note: LM4 is still in progress. This version contains only 3 tutorials. Learning Module 4 - Thermal Fluid Analysis Note: LM4 is still in progress. This version contains only 3 tutorials. Attachment C1. SolidWorks-Specific FEM Tutorial 1... 2 Attachment C2. SolidWorks-Specific

More information

SIMPLIFIED METHOD FOR ESTIMATING THE FLIGHT PERFORMANCE OF A HOBBY ROCKET

SIMPLIFIED METHOD FOR ESTIMATING THE FLIGHT PERFORMANCE OF A HOBBY ROCKET SIMPLIFIED METHOD FOR ESTIMATING THE FLIGHT PERFORMANCE OF A HOBBY ROCKET WWW.NAKKA-ROCKETRY.NET February 007 Rev.1 March 007 1 Introduction As part of the design process for a hobby rocket, it is very

More information