Fireproofing Critical Electrical & Instrumentation. Kris Thorsteinsson
|
|
|
- Audra Reed
- 7 years ago
- Views:
Transcription
1 Fireproofing Critical Electrical & Instrumentation Kris Thorsteinsson
2 E & I Thermal Damage Criteria Radiant Heat Flux &/or Temperature Damage or failure threshold criteria can be specified as either: temperature of a hot gas layer or fire plume, or radiant heat flux from the luminous flame and/or smoky zones of a fire The following four (4) slides show: Structural Steel Thermal Damage Criteria (one table) E & I Cables Thermal Damage Criteria (three tables) Conclusion cables are more vulnerable than steel to temperature and radiant heat flux: Cables are damageable at < 12.5 kw/m 2 vs. steel > 37.5 kw/m 2, Cables are damageable at approx. 250 C / 480 F vs. 538 C/1000 F The next two (2) slides show results of pool fire modeling of a hexane spill: 6 m diameter spill with 2 m/s wind; 17.2 m diameter API 521 fire with little wind Conclusion fire hazard zones for cables extend further horizontally and vertically than for structural steel 2 Fireproofing Critical E & I
3 Steel Thermal Damage Criteria Radiant Heat Flux &/or Temperature Structural Steel Thermal Damage Threshold Criteria Equipment Type process equipment and steel beams uninsulated steel columns & beams steel structures & equipment Radiant Heat Criteria*** Exposed Temperature Criteria*** references 37.5 kw/m 2 (3.3 Btu/ft 2 -s) (60 min. exposure) Alderman kw/m 2 ( Btu/ft 2 -s)* 593 C (1100 F)* Barry kw/m 2 (3.3 Btu/ft 2 -s) Technica 1988 process equipment 37.5 kw/m 2 (3.3 Btu/ft 2 -s) BS 5908 process equipment & vessels 44 kw/m 2 (3.9 Btu/ft 2 -s) IP 1993 steel members theoretical maximum 50 kw/m2 (4.4 Btu/ft 2 -s)** 540 C (1000 F)** EPC 2007 steel members design 25 kw/m 2 (2.2 Btu/ft 2 -s)** w/ safety factor 410 C (770 F)** EPC 2007 storage tanks 37.8 kw/m 2 (3.3 Btu/ft 2 -s) Robertson 1976 / Wells 1980 pipe / riser / process vessel rupture 37.5 kw/m 2 (3.3 Btu/ft 2 -s) (60 min. exposure) DNV 2009 steel beam yield 37.5 kw/m 2 (3.3 Btu/ft 2 -s) (60 min. exposure) DNV 2009 steel beam collapse 37.5 kw/m 2 (3.3 Btu/ft 2 -s) (120 min. exposure) DNV 2009 Notes *10-15 minute exposure time ** Indefinite exposure time *** Consider time to damage 3 Fireproofing Critical E & I
4 E & I Cables Thermal Damage Criteria Radiant Heat Flux &/or Temperature Equipment Type E & I Thermal Damage Threshold Criteria Radiant Heat Criteria*** Exposed Temperature Criteria*** references thermoplastic cables* 6 kw/m 2 (0.5 Btu/ft 2 -s) 205 C (400 F) EPRI 2010 thermoset cables* 11 kw/m 2 (1.0 Btu/ft 2 -s) 330 C (625 F) EPRI 2010 electronics 3 kw/m 2 (0.25 Btu/ft 2 -s) 65 C (150 F) EPRI 2010 Flamtrol XLPE, 12 AWG, I/C, 600 V** C ( F) EPRI 2010 plastic-insulated and clad E&I cables 12 kw/m 2 (1.1 Btu/ft 2 -s) C ( F) Mecklenburgh 1985 plastic tubing melting, 12.5 kw/m 2 (1.1 Btu/ft 2 Technica 1988 / CCPS -s) wood ignition 2000 severe damage to 12.6 kw/m 2 (1.1 Btu/ft 2 Robertson 1976 / Wells -s) property & cables 1980 electrical failure nonqualified cable 8 kw/m 2 (0.7 Btu/ft 2 -s) 130 C (265 F) Sandia 1983 electrical failure IEEE 383 qualified cable 18 kw/m 2 (1.6 Btu/ft 2 -s) 250 C (480 F) Sandia 1983 plastic cable insulation kw/m 2 degrades ( Btu/ft 2 -s) (10 min. exposure) Barry 2003 PE and PVC-insulated cable failure threshold (2-20 min. exposure) 250 C (480 F) NUREG 1805 Notes *No credit for conduit for delaying onset of damage * No credit for fire retardant coating or rating for delaying onset of damage ** Plant-specific or product -specific data may be used if appropriate basis is provided *** Consider time to damage - EPRI 2010 values use 19 minutes, Sandia 60 min. 4 Fireproofing Critical E & I
5 Thermoset Cables (e.g. XLPE, XLPO, flame retardant) Thermal Damage Criteria NUREG Fire Dynamics Tools 5 Fireproofing Critical E & I
6 Thermoplastic Cables (e.g. PE, PVC, non-flame retardant) Thermal Damage Criteria NUREG Fire Dynamics Tools 6 Fireproofing Critical E & I
7 Pool Fire Radiant Heat Levels Fire 6.0 m Dia. Radiant Heat Levels from 6 m Diameter Pool Fire - 2m/s Wind Speed 20 Convection Thermal Effects Above Fire not Modeled 15 Height above Pool Fire Base (m) 10 Steel Vulnerability - Hexane Fire Electrical Cable Vulnerability - Hexane Fire kw/m2 Hexane kw/m2 Hexane 5 6 m dia pool fire Draft Radiant Heat Modeling K. Thorsteinsson Distance from Pool Fire Centre (m) 7 Fireproofing Critical E & I
8 Pool Fire Radiant Heat Levels API 521 Size Fire 17.2 m Dia. Radiant Heat Levels from API 521 Pool Fire 17.2 m Equiv. Dia m/s Wind Speed Convection Thermal Effects Above Fire not Modeled Electrical Cable Vulnerability - Hexane Fire Height above Pool Fire Base (m) Steel Vulnerability - Hexane Fire kw/m2 Hexane kw/m2 Hexane m dia pool fire Draft Radiant Heat Modeling K. Thorsteinsson Distance from Pool Fire Centre (m) 8 Fireproofing Critical E & I
9 Common Radiant Heat Flux Damage Criteria Vegetation 10 kw/m 2 Protected / Unprotected Atmos. Tankage - 32 / 8 kw/m 2 Process Equipment kw/m 2 Process Buildings LPG Storage 25 kw/m 2 22 kw/m 2 Prolonged Operator Response 4.7 kw/m 2 Operator Response < 60 sec 6.3 kw/m 2 Control & Inst 12.5 kw/m 2 Property Lines & Roadways 5 kw/m 2 Combustible Structures 10 kw/m 2 Electrical Equipment / Cables 12.5 kw/m 2 9 Fireproofing Critical E & I
10 References EPRI Methods for Applying Fire Risk Analysis to Fire Scenarios (MARIAFIRES)-2008 NUREG/CP-0194, EPRI 2010 Mecklenburgh Process Plant Layout - JC Mecklenburgh, IChemE / Wiley, 1985 Technica Techniques for Assessing Industrial Hazards - A Manual - Technica / World Bank, 1988 Wells Safety in Process Plant Design, GL Wells, IChemE / Wiley, 1980 Robertson Spacing in Chemical Plant Design Against Loss by Fire, R Robertson, IChemE Symp Series 47, 1976 CCPS Guidelines for Chemical Process Quantitative Risk Analysis, 2nd Ed., AIChE CCPS, 2000 NUREG Investigation of Twenty-Foot Separation Distance as a Fire Protection Method as Specified in 10CFR50, App R, NUREG/CR-3192, Sandia, 1983 NUREG Fire Dynamics Tools - Quantitative Fire hazard Analysis Methods for the US Nuclear Regulatory Commission Fire Protection Inspection Program (NUREG 1805), 2004 Alderman Risk Assessment in the Oil and Gas Energy Industry, JA Alderman, Fire Protection Engineering, 2007 Barry Fire Exposure Profile Modeling; Some Threshold Damage Limit (TDL) Data, TF Barry, Fire Risk Forum, 2003 BS Fire and Explosion Precautions at Premises Handling Flammable Gases, Liquids and Dusts, BS , BSI, 1990 IP Fire Precautions at Petroleum Refineries and Bulk Storage Installations, Institute of Petroleum IP Part 19, 1993 EPC Engineering Instructions for Passive Fire Protection, EPC Firm Process Safety Group, 2007 DNV Case Study of Rapid Blowdown on Offshore Platform, DNV / BP, Fireproofing Critical E & I
Darchem Thermal Protection
Darchem Thermal Protection Engineered Materials Thermal and Fire Protection for life www.darchem.co.uk Introduction to Darchem Thermal Protection Darchem Thermal Protection is world renowned for the design,
CAROLFIRE The Cable Response to Live Fire Project
CAROLFIRE The Cable Response to Live Fire Project Presented by: Steven P. Nowlen Sandia National Laboratories Presented at: ANS Winter Meeting 2006 Albuquerque, NM Acknowledgements CAROLFIRE is a U.S.
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
FIRE RESISTANT CABLE CONSTRUCTION OF CABLES
FIRE RESISTANT CABLE In all fire disasters, fire smoke, heat and toxic fumes are the main obstacles to safe evacuation of a building or area. A major contribution towards overcoming these hazards is the
Decree of the Ministry of the Environment on fire safety of ventilation systems
THE NATIONAL BUILDING CODE OF FINLAND MINISTRY OF THE ENVIRONMENT Housing and Building Department Decree of the Ministry of the Environment on fire safety of ventilation systems Adopted in Helsinki, 18
Fire Performance Standard
Fire Performance Standard At present, in cable industry, Fire Retardant, Low Smoke Halogen Free (LSZH), Low Smoke Fume (LSF) and Fire Resistant cables are all described as Fire survival Cables. Flame Retardant
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
Ethanol Vehicle and Infrastructure Codes and Standards Citations
Ethanol Vehicle and Infrastructure Codes and Standards Citations This document lists codes and standards typically used for U.S. ethanol vehicle and infrastructure projects. To determine which codes and
Building Code Clarifications - 7. Fire Resistance
Building Code Clarifications - 7. Fire Resistance 7.1 (15-12-030) Use of combustibles in Type III construction roof assemblies Code Section (15-12-030) Use of Combustibles was revised on May 17, 2000,
Saeid Rahimi. Effect of Different Parameters on Depressuring Calculation Results. 01-Nov-2010. Introduction. Depressuring parameters
Effect of Different Parameters on Depressuring Calculation Results Introduction Saeid Rahimi 01-Nov-2010 Emergency depressuring facilities are utilized to accomplish at least one of the following objectives:
HOT WORK PERMIT PROCEDURES
COLUMBIA UNIVERSITY ENVIRONMENTAL HEALTH & SAFETY HOT WORK PERMIT PROCEDURES COLUMBIA UNIVERSITY MEDICAL CENTER February 2010 1 TABLE OF CONTENTS A. PURPOSE 3 B. SCOPE 3 C. POLICIES AND PROCEDURES 3-4
WHITE PAPER Fire & safety performance standards
WHITE PAPER Fire & safety performance standards Terminologies describing Fire Performance Terminologies describing Fire Performance often present a challenge to understand as how they apply to a cable
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
Building Cables and Wires
Building Cables and Wires 4 Introduction alfanar is equipped with state-of-the-art manufacturing facilities such as latest machineries, instrumentation, quality control and testing laboratory, etc., for
EUROPEAN STANDARDS PERSONAL PROTECTIVE CLOTHING FOR FLAME RESISTANT. Alexander Gstettner, Lenzing AG Austria
EUROPEAN STANDARDS FOR FLAME RESISTANT PERSONAL PROTECTIVE CLOTHING Alexander Gstettner, Lenzing AG Austria W a t e r How are the standards organized? A 1 Testing Methods Standards specifiying performance
Gas Standards and Safety. Guidance Note GAS INSTALLATIONS SUPPLIED FROM BIOGAS FACILITIES - ACCEPTANCE REQUIREMENTS GAS ACT 2000
Gas Standards and Safety Guidance Note January 2015 (GN106) Version 1.0 GAS INSTALLATIONS SUPPLIED FROM BIOGAS FACILITIES - ACCEPTANCE REQUIREMENTS GAS ACT 2000 A guide to assist in the design of biogas
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
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
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
HSE Information Sheet. Advice on acceptance criteria for damaged Passive Fire Protection (PFP) Coatings. Offshore Information Sheet No.
HSE Information Sheet Advice on acceptance criteria for damaged Passive Fire Protection (PFP) Coatings Offshore Information Sheet No. 12/2007 Introduction...2 Background...2 Additional information...3
ARE YOU IN COMPLIANCE WITH THE OSHA COMBUSTIBLE DUST DIRECTIVE? Revised March 18, 2009
Kidde Fenwal, Inc. Industrial Explosion Protection Group A UTC Fire & Security Company 400 Main Street Ashland, MA 01721 Tel 508-881-2000 Fax 508-485-3115 www.fenwalprotection.com FENWAL Protection Systems
Dispelling the Solar Myth - Evacuated Tube versus Flat Plate Panels. W illiam Comerford Sales Manager Ireland Kingspan Renewables Ltd.
Dispelling the Solar Myth - Evacuated Tube versus Flat Plate Panels W illiam Comerford Sales Manager Ireland Kingspan Renewables Ltd. 1 The Kingspan Group Energy independent buildings for a sustainable
Fire Testing of Recycled Materials for Building Applications
Fire Testing of Recycled Materials for Building Applications Robert H. White Abstract To gain wide market acceptance of new building products made from recycled materials, fire testing may be necessary.
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
5/3/2010. Article 500 address the requirements for hazardous locations: Wiring Equipment
Two Documents are used for the Classification of Combustible Dusts and Hazardous Locations: NFPA 499-Recommended Practices for the Classification of Combustible Dusts and Hazardous Locations for Electrical
PROCEDURES PREVENTION OF ACCIDENTAL IGNITION
Page No: 1 of 7 6.0 PURPOSE (192.751) All possible precautions shall be exercised to prevent the accidental escape and ignition of gas. Whenever possible, potential sources of ignition should be eliminated
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
A World Class Manufacturer of Induction Bends
A World Class Manufacturer of Induction Bends COFELY FABRICOM BENDING A leading position in bending High Flexibility and Close Tolerances As a world leading manufacturer of pipe bends, produced by induction
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
LNG and Petrochemical Security Risk Assessment and Management
LNG and Petrochemical Security Risk Assessment and Management American Association of Port Authorities Port Security Seminar Seattle, WA July 20, 2006 David A. Moore, PE, CSP AcuTech Consulting Group 2001
Approval Standard for Plastic Suspended Ceiling Panels
Approval Standard for Plastic Suspended Ceiling Panels Class Number 4651 February 1978 2002 FM Approvals LLC. All rights reserved. Foreword The FM Approvals certification mark is intended to verify that
NFPA 30-2008: Basic Requirements for Storage Tanks
NFPA 30-2008: Basic Requirements for Storage Tanks New York City Metro Chapter Society of Fire Protection Engineers New York, NY February 22, 2011 NFPA 30, Flammable and Combustible Liquids Code Storage
Jump Start: Storage Tank Protection in Aspen HYSYS and Aspen Plus
Jump Start: Storage Tank Protection in Aspen HYSYS and Aspen Plus A Brief Tutorial (and supplement to training and online documentation) Anum Qassam, Product Management, Aspen Technology, Inc. Jennifer
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
Practical Examples of Heat Regenerative System at Steelmaking Works
2nd India-Japan Energy Forum Practical Examples of Heat Regenerative System at Steelmaking Works On Monday 4 February 2008 in Delhi Nisshin Steel Co., Ltd. Yukio Tomita 1 Structure of the Regenerative
Liquefied Petroleum Gas Volume 1 : Large Bulk Pressure Storage & Refrigerated LPG
IP THE INSTITUTE OF PETROLEUM Liquefied Petroleum Gas Volume 1 : Large Bulk Pressure Storage & Refrigerated LPG MODEL CODE OF SAFE PRACTICE PART 9 ISBN 0 471 91612 9 First'printed 1987 Reprinted October
STANDARD SPECIFICATION. for. Plumbing, Heating, Hot Water, Cold Water & Electrical work. Sussex Lodge London W2 & 16 Stanhope Terrace London W2
STANDARD for Plumbing, Heating, Hot Water, Cold Water & Electrical work undertaken by owners within the building known as Sussex Lodge London W2 & 16 Stanhope Terrace London W2 BPME Consulting Engineers
Static Electricity. A Health and Safety Guideline for Your Workplace. What Are Some Sources of Static Electricity? What is Static Electricity?
A Health and Safety Guideline for Your Workplace What is static electricity? What causes it? How is it hazardous? And, most importantly, how can it be controlled? All of these questions will be answered
www.klmtechgroup.com TABLE OF CONTENT
Page : 1 of 13 Project Engineering Standard www.klmtechgroup.com KLM Technology #03-12 Block Aronia, Jalan Sri Perkasa 2 Taman Tampoi Utama 81200 Johor Bahru Malaysia ELECTIRAL GROUNDING TABLE OF CONTENT
Use of Decision Support Tools for Bushfire Risk Management in NSW
Use of Decision Support Tools for Bushfire Risk Management in NSW Presented by Stuart Midgley Director of Risk Management Performance NSW Rural Fire Service Definition Decision support tools or decision
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,
INTERNATIONAL STANDARD
INTERNATIONAL STANDARD IEC 60502-1 Second edition 2004-04 Power cables with extruded insulation and their accessories for rated voltages from 1 kv (U m = 1,2 kv) up to 30 kv (U m = 36 kv) Part 1: Cables
Grounding and Bonding Against Static Electricity. Jon Koppari, CSP, MS Occupational Safety and Health Instructor OSHA Training Institute
Grounding and Bonding Against Static Electricity Jon Koppari, CSP, MS Occupational Safety and Health Instructor OSHA Training Institute Objectives Identify Sources of Ignition. Identify Hazards associated
STORE HAZARDOUS SUBSTANCES SAFELY. incompatibles gas cylinders
STORE HAZARDOUS SUBSTANCES SAFELY Suitable containers incompatibles gas cylinders Oxy-Acetylene welding flammable substances 35 36 STORE HAZARDOUS SUBSTANCES SAFELY STORE HAZARDOUS SUBSTANCES SAFELY Storing
Indirect fired heaters
Indirect fired heaters Indirect Fired Heaters General INDIRECT BATH HEATERS have a wide variety of successful applications in the oil and gas production, processing and transmission industry. Some of the
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
ALVERNIA UNIVERSITY OSHA REGULATION: 29 CFR 1910.252 WELDING, CUTTING, AND BRAZING ( HOT WORK ) SECTION: 3600
OSHA REGULATION: 9 CFR 90.5 WELDING, CUTTING, AND BRAZING ( HOT WORK ) A. POLICY. This procedure follows requirements set forth in 9 CFR 90.5.. This policy applies to all Hot Work operations being done
LEAD FREE FIREX. Interlock Armored Cables TECK90 and MC Industrial Cables. w w w. n e x a n s e n e r g y. c o m
FIREX Interlock Armored Cables TECK90 and MC Industrial Cables LEAD FREE O V E R 1 8 0 Y E A R S O F E X P E R I E N C E 866-663-9267 w w w. n e x a n s e n e r g y. c o m Interlock Armored Cables Introduction....2
D A T A C O M M U N I C A T I O N S C O M P E T E N C E C E N T E R
F l a m e T e s t S t a n d a r d s f o r D a t a C o m m u n i c a t i o n s C a b l e M a r c h 2 0 0 7 D A T A C O M M U N I C A T I O N S C O M P E T E N C E C E N T E R Table of Contents Executive
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
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
Process Safety Management of Highly Hazardous & Explosive Chemicals. Safe Work Practices
Process Safety Management of Highly Hazardous & Explosive Chemicals Safe Work Practices Safe Work Practices 1910.119(f)(1) The employer shall develop and implement safe work practices to provide for the
HOT WORK PERMIT PROGRAM TRAINING. John Braun
HOT WORK PERMIT PROGRAM TRAINING John Braun 1.0 INTRODUCTION 1.2 Purpose The Hot Work Permit Program has been developed for University employees that work on or around hot work activities. This program
The Globally Harmonized System and OSHA Hazard Communication Revision
The Globally Harmonized System and OSHA Hazard Communication Revision Presented by: Denese A. Deeds, CIH Industrial Health & Safety Consultants, Inc. Shelton, CT 1 Overview Where are we with implementation
Pressure Vessels (Air Compressors) and LPG Tanks
Pressure Vessels (Air Compressors) and LPG Tanks 1. Identification of Workplace Hazard Any container, tank or vessel that contains pressurized material is a potential hazard to employees due to the force
A. Fire Protection Plan. B. Access and Parking
Standards for Construction Site Fire Safety For Use by Unidocs Member Agencies or where approved by your Local Jurisdiction Authority Cited: California Fire Code (CFC) These standards are intended to prescribe
CTI TECHNICAL BULLETIN Number 9: A publication of the Cable Tray Institute
CTI TECHNICAL BULLETIN Number 9: A publication of the Cable Tray Institute Cable Tray Wiring Systems Have Many Cost Advantages Cost is usually a major consideration in the selection of a wiring system.
Fireproofing Practices in Petroleum and Petrochemical Processing Plants API PUBLICATION 2218 SECOND EDITION, AUGUST 1999
Fireproofing Practices in Petroleum and Petrochemical Processing Plants API PUBLICATION 2218 SECOND EDITION, AUGUST 1999 Fireproofing Practices in Petroleum and Petrochemical Processing Plants Health,
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
IMPLEMENTING THE NEW ELECTRICAL SAFETY REQUIREMENTS
IMPLEMENTING THE NEW ELECTRICAL SAFETY REQUIREMENTS Paul A Zoubek, CSP, CIH Occupational Services, Inc. San Diego, CA 619-861 861-0612 paul@occsev.com OCCUPATIONAL SERVICES, INC. BACKGROUND Update Update
List of Frequently Utilized Storage Tank Standards and Practices
List of Frequently Utilized Storage Tank Standards and Practices Below is a list of frequently used storage tank standards and practices from organizations that are referenced in 25 PA Code, Chapter 245.
THERMAL BARRIERS FOR THE SPRAY POLYURETHANE FOAM INDUSTRY
THERMAL BARRIERS FOR THE SPRAY POLYURETHANE FOAM INDUSTRY Spray Polyurethane Foam Alliance Copyright 2005 To order copies of this publication, call 800-523-6154 and request SPFA Stock Number AY 126 TECHNICAL
HealthandSafetyOntario.ca. Introduction. Storage Containers. Storing Flammable Liquids
Flammable Liquids Storage Introduction This guideline is designed to help you store flammable liquids safely. It is based on the requirements of the Ontario Fire Code, Part 4, and of the Regulations for
CODE NOTES. Insulation Requirements in Commercial Buildings for Mechanical and Service Hot-Water Piping
BUILDING TECHNOLOGIES PROGRAM Insulation Requirements in Commercial Buildings for Mechanical and Service Hot-Water Piping The intent of the pipe insulation requirements is to reduce temperature changes
DIRECT-FIRED HEATERS: OPERATOR TRAINING. Intensive 2-Day Training Course for Facility Operators
DIRECT-FIRED HEATERS: OPERATOR TRAINING Intensive 2-Day Training Course for Facility Operators COURSE FACILITATOR Roger Newnham President OnQuest Canada ULC C. Eng., F.I.Mech.E., Eur. Ing. REPRESENTATIVE
Routine and Emergency Boiler Operation
Routine and Emergency Boiler Operation Learning Outcome When you complete this module you will be able to: Describe the routine safe and efficient operation of a packaged boiler. Learning Objectives Here
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,
Annex of the certificate (Page 1/6) Accreditation Scope
As a Testing Laboratory Annex of the certificate (Page 1/6) Accreditation Scope Address: Küçük Çiğli Mh. 8780/1 Sk. No:5 Çiğli 35681 İZMİR / TÜRKİYE Phone : 0 232 376 24 25 Fax : 0 232 386 33 98 E-Mail
Technical Requirements for Aboveground Storage Tanks (ASTs) Storing Class IIIB Liquids (other than used oil)
Technical Requirements for Aboveground Storage Tanks (ASTs) Storing Class IIIB Liquids (other than used oil) References: Comm 10 2009 EDITION / NFPA 30 2008 EDITION ITEM DESCRIPTION Comm 10 / NFPA General
STEEL BUILDINGS IN EUROPE. Single-Storey Steel Buildings Part 7: Fire Engineering
STEEL BUILDINGS IN EUROPE Single-Storey Steel Buildings Part 7: Fire Engineering Single-Storey Steel Buildings Part 7: Fire Engineering 7 - ii FOREWORD This publication is the seventh part of the design
Flare Pilot System Safety
Flare Pilot System Safety John Bellovich, Jim Franklin, and Bob Schwartz John Zink Company, LLC, 11920 East Apache, Tulsa, OK 74116; john.bellovich@johnzink.com (for correspondence) Published online 30
ENGINEERED DRAWINGS FOR PETROLEUM STORAGE TANKS
Facility Name: ENGINEERED DRAWINGS FOR PETROLEUM STORAGE TANKS The following is intended to be used as a guideline for information required to appear on engineered drawings involving petroleum storage
Controlling fire and explosion risks in the workplace
Controlling fire and explosion risks in the workplace A brief guide to the Dangerous Substances and Explosive Atmospheres Regulations Introduction to DSEAR This leaflet provides a brief introduction to
Morrison Bros. Co. General Product Specifications
Morrison Bros. Co. General Product Specifications Tank Mounted Spillbox The spill containment device is manufactured to contain spills and drips that may occur at the fill point on aboveground storage
VERIFY HARD COPY AGAINST WEB SITE IMMEDIATELY PRIOR TO USE
Nuclear Safe Work Practice 6.7 Safety Signs/Tapes/Ropes/Chains and Tags 1.0 PURPOSE/SCOPE To provide consistent standards for using safety signs, tapes, ropes and chains (barriers) to communicate existing
Fired Heater Design and Simulation
Fired Heater Design and Simulation Mahesh N. Jethva 1, C. G. Bhagchandani 2 1 M.E. Chemical Engineering Department, L.D. College of Engineering, Ahmedabad-380 015 2 Associate Professor, Chemical Engineering
Using Risk Assessment Tool to Evaluate the Fire-Induced Core Damage Frequency
, June 30 - July 2, 2010, London, U.K. Using Risk Assessment Tool to Evaluate the Fire-Induced Core Damage Frequency Sh. Kamyab, M. Nematollahi, M. Famourihoseinzade Abstract the frequency of fire-induced
David O Brien, CMP Products (David.OBrien@cmp-products.com)
David O Brien, CMP Products (David.OBrien@cmp-products.com) 1) Main Function of Cable Glands 2) Common Issues with Cable Glands 3) Compliance / Standards, changing times 4) How do we select Cable Glands?
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
21.1 Functions, Basic Configuration, and Interfaces
21 (6.2.M) Site Services Building 21.1 Functions, Basic Configuration, and Interfaces 21.1.1 Functions The primary functions performed by the site services building are to house, support, provide a suitable
Low Emission - Low Maintenance Burner Design
Reliability & Maintenance Conference & Exhibition May 24-27, 2005 Ernest N. Morial Convention Center New Orleans, Louisiana Low Emission - Low Maintenance Burner Design Presented By: Scott D. Reed Vice
Notes. Material 1. Personal Protective Equipment 2.
29CFR 1926.20(b)-Accident Reduction, 29CFR 1926.21- Safety Training & Education 29CFR 1926.20(a)-Unsafe Working Conditions 29 CFR 1910.132-138, the "Personal Protection Equipment" standard. & 20 CFR 1910.134
PSAC/SAIT Well Testing Training Program Learning Outcomes/Objectives Level B
s/objectives Level B CHEM 6014: Properties and Characteristics of Natural Gases Discuss the pertinent properties and uses of natural gases as they occur in gas processing. 1. Describe the physical properties
CFD Topics at the US Nuclear Regulatory Commission. Christopher Boyd, Ghani Zigh Office of Nuclear Regulatory Research June 2008
CFD Topics at the US Nuclear Regulatory Commission Christopher Boyd, Ghani Zigh Office of Nuclear Regulatory Research June 2008 Overview Computational Fluid Dynamics (CFD) is playing an ever increasing
Safe Operating Procedure
Safe Operating Procedure (Revised 07/09) HOT WORK PERMIT OPERATIONS (For assistance, please contact EHS at (402) 472-4925, or visit our web site at http://ehs.unl.edu/) Authority In recognition of the
MaxCell Technical Manual Design Parameters
MaxCell Technical Manual Design Parameters Breaking Strength by Product Style, lbs Product Style Standard MaxCell Fire Resistant MaxCell Test Method 4 Cell 2,750 2,200 ASTM D 5 Bellcore 5 5.. Cell 2,50
The soot and scale problems
Dr. Albrecht Kaupp Page 1 The soot and scale problems Issue Soot and scale do not only increase energy consumption but are as well a major cause of tube failure. Learning Objectives Understanding the implications
Sample Written Program. For. Flammable Liquids
Sample Written Program For Flammable Liquids 1 Flammable Liquids. (YOUR COMPANY NAME) Purpose Proper Storage and use of flammable liquids can significantly reduce the possibility of accidental fires and
Fuel Treatment and Conditioning Systems
RULES FOR CLASSIFICATION OF Ships PART 6 CHAPTER 14 NEWBUILDINGS SPECIAL EQUIPMENT AND SYSTEMS ADDITIONAL CLASS Fuel Treatment and Conditioning Systems JULY 2006 This chapter has been amended since the
Stilling Well Recommendations
White Paper June 24, 2009 Stilling Well Recommendations This document describes general requirements for stilling wells used for radar tank gauging applications. Automation solutions for oil & gas, defense
Hydrogen Detection in Oil Refineries
Hydrogen Detection in Oil Refineries Because every life has a purpose... Hydrogen Detection in Oil Refineries MSA Gas Detection: Hydrogen Gas Detection in Oil Refineries Oil refineries are large producers
Terminal Box. Specifications TNCN
Terminal box The /TNCC range comprises many standard sizes of enclosures manufactured in stainless steel 316L for maximum environmental protection. The main body is manufactured from minimum 1,5 mm sheet
Uline NFPA. SECTION 1 : CHEMICAL PRODUCT AND COMPANY IDENTIFICATION MSDS Name: Collapsible Bulk Containers
Uline NFPA HMIS Collapsible Bulk Containers Manufacturer MSDS Number: 70000000 1 1 0 HEALTH 1 FIRE 1 REACTIVITY 0 PPE SECTION 1 : CHEMICAL PRODUCT AND COMPANY IDENTIFICATION MSDS Name: Collapsible Bulk
Waste Oil Collection / Storage
ENVIRONMENTAL & REGULATORY SERVICES Storage Tank Regulation Section P. O. Box 7837 Madison, Wisconsin 53707-7837 TDD #: (608) 264-8777 http://www.commerce.state.wi.us http://www.wisconsin.gov Jim Doyle,
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
Combustible Dust. Overview
Combustible Dust Michael Wacker Industrial Hygienist Madison, WI Area OSHA Office Overview History of Combustible dust What is combustible dust Some recognized hazards OSHAs Combustible Dust NEP What does
Spill Prevention, Control and Countermeasure (SPCC)
Spill Prevention, Control and Countermeasure (SPCC) History Original promulgation 1973, effective 1974 Codified in 40 CFR 112 (EPA Jurisdiction) Proposed rulemaking 1991, 1993 and 1997 Amended July 17,
Energy and Energy Transformations Test Review
Energy and Energy Transformations Test Review Completion: 1. Mass 13. Kinetic 2. Four 14. thermal 3. Kinetic 15. Thermal energy (heat) 4. Electromagnetic/Radiant 16. Thermal energy (heat) 5. Thermal 17.
Sulfur Tail Gas Thermal Oxidizer Systems By Peter Pickard
Sulfur Tail Gas Thermal Oxidizer Systems By Peter Pickard Introduction SRU s (Sulfur Recovery Units) are critical pieces of equipment in refineries and gas plants. SRUs remove sulfur compounds from certain
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