Using CFD in Platform Design
|
|
|
- Myles Waters
- 8 years ago
- Views:
Transcription
1 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., Houston, TX Joar Dalheim, Scandpower AS, Kjeller, Norway
2 CFD (Computational Fluid Dynamics) in Fire & Blast Assessment Optimal Solutions Result In: 1. Increased Safety Deeper understanding of potential consequences Knowing HOW?!?! in detail where the risk drivers are Knowing what efforts that will best improve safety Better control of the actual risk level 2. Reduced Cost Mitigation efforts may more easily be proven to not be required Knowing how much steel is required to meet an acceptable level Reducing weight (both steel walls and passive fire protection)
3 Explosion Risk Example Level of Explosion Analysis Selection Level 1 Entire Module Filled at LFL & exploded Level 2 Gas Dispersion with most credible cloud exploded Level 3 Probabilistic QRA using Multivariate CFD in Conjunction with Risk Acceptance Criteria.
4 [Cond. Prob./yr] vs Explosion Overpressure (F-P) Design Load Identified for Acceptance Criterion of 10-4 /yr
5 Explosion Overpressure (barg) Explosion Level Realm w/i Plot of Overpressure vs % of Module Filled with Flammable Gas Level 1: Designing the blast wall to resist the largest theoretical cloud size Level 2: Designing the blast wall to resist the largest realistic cloud size (estimated from gas dispersion) Panel Pressure Deluge (barg) Level 3: Designing the blast wall to resist the cloud size with a frequency of 10-4 (NORSOK Z-013) 0 % 10 % 20 % 30 % 40 % 50 % 60 % 70 % 80 % 90 % 100 % Degree of filling (% of module) Mean Value (k50)
6 USD ($) Cost Comparison associated with 3 Explosion Levels: Blast Barrier Construction; Analysis; Sum Construction Costs Level 1 Level 2 Level 3 Analysis Costs
7 CFD Gas Dispersion Simulation Naturally Ventilated Module on an Offshore Platform Flammable Gas Volume depends on leak: location, direction, rate, duration; congestion & confinement; meteorological conditions.
8 CFD Gas Dispersion Simulation Forced Ventilated Module Flammable Gas Volume depends on leak: location, direction, rate, duration; congestion & confinement; HVAC system.
9 LNG Pool Formation & Associated Natural Gas Dispersion Flammable Gas Volume depends on leak: location, direction, rate, duration; physical obstructions; meteorological & surface conditions.
10 CFD - Flammable Liquid Spray Release Flammable Volume depends on leak: location, direction, rate, duration; congestion & confinement; flash & boiling points liquid; & surface conditions.
11 CFD -Explosion Simulation in Confined Volume Blast Loads depend on plume size & location; ignition location; gas composition; congestion & confinement; pressure relief panels; deluge system.
12 CFD Pool Fire on Sea Surface Fire Loads & Smoke Development depend on pool size & location; gas composition; congestion & confinement; wind conditions.
13 CFD Fire Simulation Inside Enclosed Module Fire Loads & Smoke Development depend on leak: location and direction, rate (pool size - diffusive fire), duration; congestion & confinement, HVAC.
14 CFD - Dynamic Non-Linear Structural Fire Response Simulation
15 CFD - Dynamic Non-Linear Structural Explosion Response Simulation
16 CFD Turbulence & Temperature Fields for Helicopter Operations
17 CFD Simulation of Outdoor Working Availability for Harsh Weather (related to Wind Chill Index) Includes: Layout effects; meteorology; climatology (monthly wind & temperature statistics)
18 Concluding Remarks Employing CFD is Increasingly Important in Effective Risk Management for Offshore & Onshore Facilities. Detailed Understanding of Potential Consequences Allow for Improved Engineering Design, Mitigation Measures & Procedures, for Enhanced Safety Performance & Financial Results. Effective Means to Improve Insight of New Hazards & Potential Consequences Where New Technologies are Applied.
19 For more information: Eric Peterson The Lloyd s Register Group works to enhance safety and approve assets and systems at sea, on land and in the air. Services are provided by members of the Lloyd s Register Group Lloyd s Register, Lloyd s Register EMEA and Lloyd s Register Asia are exempt charities under the UK Charities Act 1993.
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
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
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
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,
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,
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
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;
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
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,
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;
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
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
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
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,
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
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,
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
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
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
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
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
Liquefied Natural Gas (LNG)
Graduate Diploma in Petroleum Studies Major in Liquefied Natural Gas (LNG) INDUCTION Launching ceremony Week 39, 2012 Administration / Plant visit / Fundamentals of LNG and LNG main risks awareness Module
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
Goliat Barrier Management
Goliat Barrier Management ESRA Norge; March 25, 2015 www.eninorge.com Eni: Ole Rekdal Safetec: Helene Ness Hansen PL 229 Goliat Location and Partnership License awarded in 1997 Present licensees Eni Norge
In accordance with NFPA 30, these containers are not to store Class I flammable liquids.
In accordance with NFPA 30, these containers are not to store Class I flammable liquids. Zurich recommends storing these containers in dedicated liquid storage rooms, detached buildings, or in listed dispensing
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
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
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
The SPE Foundation through member donations and a contribution from Offshore Europe
Primary funding is provided by The SPE Foundation through member donations and a contribution from Offshore Europe The Society is grateful to those companies that allow their professionals to serve as
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
Safety Integrity Level (SIL) Studies Germanischer Lloyd Service/Product Description
Safety & Risk Management Services Safety Integrity Level (SIL) Studies Germanischer Lloyd Service/Product Description Germanischer Lloyd Service/Product Description Safety Integrity Level (SIL) Studies
Fire Hazard Calculations for Hydrocarbon Pool Fires Application of Fire Dynamics Simulator FDS to the Risk Assessment of an Oil Extraction Platform
Fire Hazard Calculations for Hydrocarbon Pool Fires Application of Fire Dynamics Simulator FDS to the Risk Assessment of an Oil Extraction Platform Stefania Benucci, Giovanni Uguccioni D Appolonia S.p.A
THE HONG KONG INSTITUTION OF ENGINEERS 香 港 工 程 師 學 會. Admission Requirements for the Fire Discipline (Normal Route) Item Description Remarks
Admission Requirements for the Fire Discipline (Normal Route) Item Description Remarks Age Academic requirements (either (a), (b), (c) or (d) ) 25 minimum The academic requirement for Member in the Fire
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
Area Classification Why? Where? How? Who? When?
Area Classification Why? Where? How? Who? When? Patrick Leroux TOTAL AREA CLASSIFICATION Why? A brief history of accidents Severe accidents in coal mines occurred through the world in the 19 th and 20
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
EXPLOSIVE ATMOSPHERES - CLASSIFICATION OF HAZARDOUS AREAS (ZONING) AND SELECTION OF EQUIPMENT
EXPLOSIVE ATMOSPHERES - CLASSIFICATION OF HAZARDOUS AREAS (ZONING) AND SELECTION OF EQUIPMENT OVERVIEW ASSESSING THE RISK RELATIONSHIP BETWEEN FIRES AND EXPLOSIONS CLASSIFYING HAZARDOUS AREAS INTO ZONES
Practical Examples of Fire Protection Engineering Practices and Technology for PSM
Practical Examples of Fire Protection Engineering Practices and Technology for PSM Presented at: Mary Kay O'Connor Process Safety Center International Symposium Beyond Regulatory Compliance, Making Safety
Flammable Liquids 29 CFR 1910.106
Flammable Liquids 29 CFR 1910.106 OSHA s Directorate of Training and Education These materials were developed by OSHA s Directorate of Training and Education and are intended to assist employers, workers,
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
ICHEME SYMPOSIUM SERIES NO. 139 A METHODOLOGY FOR CONCEPT RISK ASSESSMENT OF OFFSHORE DEVELOPMENTS
A METHODOLOGY FOR CONCEPT RISK ASSESSMENT OF OFFSHORE DEVELOPMENTS FK Crawley, Dr MM Grant, MD Green WS Atkins Consultants Limited, 20 N Claremont St., Glasgow G3 7LE This paper describes a simple means
Norsk Olje og gass Selbusjøen 21.5.2014. www.eninorge.com
Norsk Olje og gass Selbusjøen 21.5.2014 www.eninorge.com Innholdet i presentasjonen Goliat værdata Goliat innretningen valg av løsninger Risikostyring i arktiske strøk Lysarkene er hovedsakelig skrevet
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
FLAMMABLE AND COMBUSTIBLE LIQUIDS. n OSHA Changes
FLAMMABLE AND COMBUSTIBLE LIQUIDS OSHA Changes Introduction This module covers the two primary hazards associated with flammable and combustible liquids: explosion and fire. In order to prevent these hazards,
Enclosures 1-866-338-0988. DuraSystems Barriers, Inc. www.durasystems.com Email: sales@durasystems.com. The Passive Fire Protection Specialists
Enclosures Sturdy single and double wall fire protection construction Impact resistant Fast & easy installation Pre-manufactured and modular Available in galvanized, stainless steel & other specialty metals
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
Combustible Dust - Things that go Boom. W. Jon Wallace, CSP, MBA Workplace Group, LLC O: 919.933.5548 E: jwallace@workplacegroup.
Combustible Dust - Things that go Boom W. Jon Wallace, CSP, MBA Workplace Group, LLC O: 919.933.5548 E: jwallace@workplacegroup.net Presentation Objectives After attending this presentation you will: Learn
Guidelines for energy efficient heating, ventilation and air conditioning (HVAC) systems
Guidelines for energy efficient heating, ventilation and air conditioning (HVAC) systems If you're a designer or a BCA, this guidance on the energy efficiency of HVAC systems in commercial buildings may
1 Computational Fluid Dynamics: the future in safety technology! 1 Jürgen Schmidt
IX Contents Preface XIX List of Contributors XXI 1 Computational Fluid Dynamics: the future in safety technology! 1 Jürgen Schmidt 2 Organized by ProcessNet: Tutzing Symposion 2011 CFD its Future in Safety
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
Practical Guidelines for Electrical Area Classification in Combustion Turbine-Generator Power Plants
Practical Guidelines for Electrical Area Classification in Combustion Turbine-Generator Power Plants Ram K. Saini, P.E. Principal Engineer, Chuck Emma, P.E. Principal Engineer, Burns and Roe Enterprises,
Remote Power Systems
Remote Power Systems Remote Power Systems Customized Power Solutions Orga s photovoltaic and battery backup systems can be found on offshore platforms and onshore remote sites all around the world when
REDUCING UNCERTAINTY IN SOLAR ENERGY ESTIMATES
REDUCING UNCERTAINTY IN SOLAR ENERGY ESTIMATES Mitigating Energy Risk through On-Site Monitoring Marie Schnitzer, Vice President of Consulting Services Christopher Thuman, Senior Meteorologist Peter Johnson,
FIRE RISK ASSESSMENT IN GERMANY - PROCEDURE, DATA, RESULTS -
International Conference Nuclear Energy in Central Europe 2000 Golf Hotel, Bled, Slovenia, September 11-14, 2000 FIRE RISK ASSESSMENT IN GERMANY - PROCEDURE, DATA, RESULTS - H.P. Berg Bundesamt für Strahlenschutz
Technical training 2014. Working together for a safer world
Technical training 2014 Working together for a safer world Engineering dynamics Machinery dynamics of rotating equipment 05 Operational modal analysis for engineering dynamic problems 06 Machinery dynamics
NORSOK STANDARD RISK AND EMERGENCY PREPAREDNESS ANALYSIS
NORSOK STANDARD RISK AND EMERGENCY PREPAREDNESS ANALYSIS Z-013 Rev.1, March 1998 This NORSOK standard is developed by NTS with broad industry assistance. Please note that whilst every effort has been made
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
Fire Security Systems
Fire Security Systems Fire Security Systems mail@fire-security.net www.fire-security.net P: 1 604 941 1001 F: 1 604 648 9311 Who is Fire Security Systems For 25 years, Fire Security has been involved in
TYPICAL FIRE SAFETY INSPECTION VIOLATIONS
TYPICAL FIRE SAFETY INSPECTION VIOLATIONS The following is a list of typical violations often found by inspectors and a generic solution. You can use this list to improve the safety of your facility, to
Chad V. Mashuga mashuga@tamu.edu
EDUCATION / LICENSING Curriculum Vitae Chad V. Mashuga mashuga@tamu.edu Ph.D. in Chemical Engineering, Michigan Technological University Dissertation Topic: Determination of the Combustion Behavior for
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
ELECTRICAL EMERGENCY SYSTEM PLAN REVIEW OVERVIEW OF CODE REQUIREMENTS
ELECTRICAL EMERGENCY SYSTEM PLAN REVIEW What to Look for during Plan Review OVERVIEW OF CODE REQUIREMENTS First determine the type of emergency power system; is the system designed for Emergency or Legally
Put us to the test. Construction testing and building investigations services from BRE. www.bre.co.uk
Put us to the test Construction testing and building investigations services from BRE www.bre.co.uk Backed by an extraordinary range of facilities BRE prides itself on being able to answer virtually any
Exova Warringtonfire fire safety engineering
Consultancy - Fire Engineering Exova Warringtonfire fire safety engineering We are committed to the philosophy where the fire safety design supports the vision, innovation or imagination of the building
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
Faculty of Science and Technology MASTER S THESIS
Faculty of Science and Technology MASTER S THESIS Study program/ Specialization: Offshore Technology/ Risk Management Writer: Reyhaneh Ghahremani Faculty supervisor: Bjørn H. Hjertager Spring semester,
Vehicle Maintenance Facilities Requirements for CNG and LNG Vehicles
Vehicle Maintenance Facilities Requirements for CNG and LNG Vehicles Presented by: Leo Thomason Executive Director Natural Gas Vehicle Institute (NGVi) at NFPA Conference and Expo, June 11, 2014 Leo Thomason
ModuSec. Secure and efficient IT room solutions Composite Panel Systems Compared. Panel Systems are not all the same!
Secure and efficient IT room solutions Composite Panel Systems Compared Panel Systems are not all the same! When it comes to accommodating critical IT systems, the first issue to look at is the environment
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
LNG as Ship Fuel. Effects on Ship Design, Operations and Supporting Infrastructure
LNG as Ship Fuel Effects on Ship Design, Operations and Supporting Infrastructure New Technologies for the Marine Highway TRB Marine Highways Committee (AW010(1)) January 14, 2013 LNG as a Ship s Fuel
Flammable liquid classes: Combustible Liquid Classes. Class IC. Class II. Class IB F.P. below 22.8 C (73 F), boiling point at or above 37.
BCFC Part 4 Flammable and Combustible Liquids Application: BCFC Part 4 Part 4 provides for the storage, handling, use and processing of flammable liquids and combustible liquids in buildings,, structures
Oil spill risk assessment and response planning for offshore installations
Finding 6 Oil spill risk assessment and response planning for offshore installations FINAL REPORT Oil Spill Response Joint Industry Project The global oil and gas industry association for environmental
OSHA Office of Training and Education 1
Flammable and Combustible Liquids OSHA Office of Training and Education 1 Introduction The two primary hazards associated with flammable and combustible liquids are explosion and fire Safe handling and
Preventing Overheated Boiler Incidents
Preventing Overheated Boiler Incidents PSE&G Appliance Service October 2012 Runaway Boiler Explosion Review Items Hazard Background Past Incidents PSE&G Emergency Response Future Process Improvements What
Harpur Hill, Buxton, SK17 9JN Telephone: +44 (0)114 289 2000 Facsimile: +44 (0)114 289 2050
Harpur Hill, Buxton, SK17 9JN Telephone: +44 (0)114 289 2000 Facsimile: +44 (0)114 289 2050 Outstanding safety Report questions Title concerning the use of gas turbines for power generation Report Number
Notes. Material 1. Appropriate Flammable Liquids
29 CFR 1910.106 Flammable Materials Flammable Liquids Preparation 1. Read Applicable Background information and related Company Policy Chapter. 2. Make Copies of this Lesson Plan for Personnel 3. Make
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
EXPRESSING AND COMMUNICATING UNCERTAINTY IN RELATION TO QUANTITATIVE RISK ANALYSIS ABSTRACT
EXPRESSING AND COMMUNICATING UNCERTAINTY IN RELATION TO QUANTITATIVE RISK ANALYSIS Roger Flage & Terje Aven University of Stavanger, Stavanger, Norway e-mail: roger.flage@uis.no, terje.aven@uis.no ABSTRACT
Flammable and Combustible Liquids. Slide 1 (of 23)
Flammable and Combustible Liquids Slide 1 (of 23) Introduction The two primary hazards associated with flammable and combustible liquids are explosion and fire Safe handling and storage of flammable liquids
HSE ASSESSMENT OF EXPLOSION RISK ANALYSIS IN OFFSHORE SAFETY CASES
HSE ASSESSMENT OF EXPLOSION RISK ANALYSIS IN OFFSHORE SAFETY CASES P W M Brighton, P J Fearnley and I G Brearley Health & Safety Executive, Offshore Safety Division, Merton House, Stanley Road, Bootle,
WINDEX ORIGINAL GLASS CLEANER
1. PRODUCT AND COMPANY IDENTIFICATION Product information Trade name : Use of the : Hard Surface Cleaner Substance/Mixture Company : S.C. Johnson & Son, Inc. 1525 Howe Street Racine WI 53403-2236 Emergency
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
CFD Based Air Flow and Contamination Modeling of Subway Stations
CFD Based Air Flow and Contamination Modeling of Subway Stations Greg Byrne Center for Nonlinear Science, Georgia Institute of Technology Fernando Camelli Center for Computational Fluid Dynamics, George
Blast Resistant Building BP Refinery Rotterdam
Blast Resistant Building BP Refinery Rotterdam 14 May, 2008 1 1 Contents Presentation Introduction KCI Functional Specification Blast Resistant Building Basis for design Blast & impact loading Design modeling
TECHNICAL INFORMATION
Page: 1/6 This checklist recognizes the major accident hazards found by experience of previous HAZID studies. It is not intended to be totally exhaustive and feedback from users should be incorporated
RR749. Comparison of risks from carbon dioxide and natural gas pipelines
Health and Safety Executive Comparison of risks from carbon dioxide and natural gas pipelines Prepared by the Health and Safety Laboratory for the Health and Safety Executive 2009 RR749 Research Report
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
Fire safety in the North/South Line project. Designing measures for fire resistance in infrastructure
Fire safety in the North/South Line project Designing measures for fire resistance in infrastructure 15 april 2015 https://www.flickr.com/photos/noordzuidlijn/ Prologue Separate contractors for concrete
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,
For further information, contact Penspen Integrity:
This document was downloaded from the Penspen Integrity Virtual Library For further information, contact Penspen Integrity: Penspen Integrity Units 7-8 St. Peter's Wharf Newcastle upon Tyne NE6 1TZ United
亞 太 風 險 管 理 與 安 全 研 討 會
2005 亞 太 風 險 管 理 與 安 全 研 討 會 Asia-Pacific Conference on Risk Management and Safety Zonal Network Platform (ZNP): Applications of a state-of-the-art deterministic CFD based scientific computing tool for
DEEP PANUKE TECHNICAL NOTE
DEEP PANUKE Page 1 of 33 TECHNICAL NOTE Topic: Removal of Beach Valve Station Isolation Valve Assembly (P74-SDV-011) Assessment Background: The Deep Panuke gas export pipeline is approximately 175km in
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
The EU-GHS Hazard statements in English (Precautionary statements: from page 5)
REACH Compliance GmbH Route des Chevallets 7 CH-1658 Rossinière Switzerland Expert advice in Chemical safety, Safety at work and Industrial hygiene Phone 0041 26 924 32 10 Fax 0041 26 924 32 11 info@reach-compliance.ch
Installation Instructions for Alarm Module Kit A043F059
Instruction Sheet 07-2013 Installation Instructions for Alarm Module Kit A043F059 1 Introduction The information contained within is based on information available at the time of going to print. In line
Flammable and Combustible Liquid
Flammable and Combustible Liquid Storage Challenges Christopher J. Wieczorek, Ph.D., FM Global David Nugent, The Valspar Corporation Global Research Update: High Challenge Storage Protection 27 June 2012,
Emergency Isolation Valves at Pump Suction: Application for Flammable Liquids
667 A publication of CHEMICAL ENGINEERING TRANSACTIONS VOL. 48, 2016 Guest Editors: Eddy de Rademaeker, Peter Schmelzer Copyright 2016, AIDIC Servizi S.r.l., ISBN 978-88-95608-39-6; ISSN 2283-9216 The
AN INNOVATIVE SOLUTION FOR FIXED OFFSHORE LNG REGASIFICATION TERMINALS
AN INNOVATIVE SOLUTION FOR FIXED OFFSHORE LNG REGASIFICATION TERMINALS Augusto Bulte Project Manager Foster Wheeler C/Gabriel García Márquez 2 Las Rozas 28232 Madrid (Spain) ABSTRACT Several developments
AIR CONDITIONING - ENERGY CONSUMPTION AND ENVIRONMENTAL QUALITY
CONTENTS AIR CONDITIONING - ENERGY CONSUMPTION AND ENVIRONMENTAL QUALITY Air Conditioning - Energy Consumption and Environmental Quality - Volume 1 No. of Pages: 400 ISBN: 978-1-84826-169-3 (ebook) ISBN:
Introduction to Computational Fluid Dynamics (CFD) for Combustion. www.reaction-eng.com (801) 364-6925
Introduction to Computational Fluid Dynamics (CFD) for Combustion www.reaction-eng.com (801) 364-6925 What is CFD? CFD stands for Computational Fluid Dynamics CFD uses computers to represent (or model)