Factors Impacting Atmospheric Discharges and Selection of Pressure Protection Disposal Systems

Size: px
Start display at page:

Download "Factors Impacting Atmospheric Discharges and Selection of Pressure Protection Disposal Systems"

Transcription

1 Factors Impacting Atmospheric Discharges and Selection of Pressure Protection Disposal Systems Patrick Smith and Abdul Aldeeb MKOPSC 2010 International Symposium College Station, Texas October 26, 2010 Copyright Siemens AG All rights reserved.

2 Introduction Direct discharge to atmosphere is a common practice that has long been considered safe, simple, dependable, and economically feasible compared to other overpressure protection mechanisms Discharging highly hazardous chemicals (HHC) to atmosphere remains a major challenge Several recent incidents have shown the need to eliminate HHC disposal to atmosphere

3 Agenda Current Practices to Design Atmospheric Discharges Factors Influencing Discharges to Atmosphere Discharge Location Decision-Making Approach

4 Current Practices to Design Atmospheric Discharge Systems The American Petroleum Institute Standard 521 Fifth Edition, 2007 (Addendum, 2008) [API 521] provides design approach for two types of systems: Pressure relief valves that discharge directly to atmosphere 15' RV-1 4 N 6 2' 15' Vessel 1

5 Current Practices to Design Atmospheric Discharge Systems Disposal through a common vent stack that discharges to the atmosphere

6 Current Practices to Design Atmospheric Discharge Systems Direct Discharge to Atmosphere API provides two criteria to determine if directing a relief device to atmosphere is advisable Both criteria focus on jet-momentum effects of the discharged vapors High velocities at the discharge of the tail pipe improve the mixing with air and reduce the concentration of the flammable or toxic material below threshold values over a short period of time

7 Current Practices to Design Atmospheric Discharge Systems Direct Discharge to Atmosphere The first criterion presented in API 521 indicates that the vapor can be diluted below its lower flammability limit due to mixing with air when the Reynolds number, R e, meets the following criteria: R e j Where j is the density of the gas at vent outlet and density of air. is the

8 Current Practices to Design Atmospheric Discharge Systems Direct Discharge to Atmosphere The second criterion indicates that for exit velocities that exceed 500 ft/s, the discharged flammable hydrocarbon is expected to be efficiently mixed with air and diluted to concentrations below the lower flammability limits at a distance of 120 diameters (based on tail pipe inner diameter) from the end of the tail pipe. Wind Release Plume

9 Current Practices to Design Atmospheric Discharge Systems Atmospheric Vent Stacks Sections 6.7 and detail the design requirements associated with atmospheric vent stacks: Recommends modeling of the release to ensure that the flammable vapor concentration does not exceed 10% to 50% of the lower flammable limit Approach presented for individual relief devices is not recommended for atmospheric vent stacks

10 Factors Influencing Discharges to Atmosphere It is evident from the API guidance that atmospheric discharges of vapors are not necessarily inherently unsafe. For liquid and two-phase discharges, the problem is more challenging. Experiments have shown that at high discharge velocities, the resultant droplets of liquids are extremely small.

11 Factors Influencing Discharges to Atmosphere In order to address the atmospheric discharge suitability, several factors will be evaluated: 1. Chemical type and concentration 2. Discharge Phase 3. Discharge Location 4. Scenario Likelihood 5. Disposal Options and Cost

12 Factors Influencing Discharges to Atmosphere - Chemical Type and Concentration Primary hazards are typically associated with the flammability and toxicity of the fluid Corrosive properties and potential formation of explosive mixtures should also be considered. For each property, the maximum acceptable concentration threshold should be determined. Lower Flammability Limit (LFL) Immediately Dangerous to Life or Health (IDLH) Short Term Exposure Limit (STEL) Permissible Exposure Limits (PEL) In many cases, dispersion modeling will be required.

13 Factors Influencing Discharges to Atmosphere 1. Chemical type and concentration 2. Discharge Phase 3. Discharge Location 4. Scenario Likelihood 5. Disposal Options and Cost

14 Factors Influencing Discharges to Atmosphere - Discharge Phase Vapor discharges are generally considered safer compared to liquid and two-phase discharges Liquid and two-phase discharges should be evaluated for the additional potential flammable, toxic, corrosive, or explosive hazards

15 Factors Influencing Discharges to Atmosphere 1. Chemical type and concentration 2. Discharge Phase 3. Discharge Location 4. Scenario Likelihood 5. Disposal Options and Cost

16 Factors Influencing Discharges to Atmosphere - Discharge Location Discharging to confined spaces or to areas where personnel or source of ignition may be present will impact the design of atmospheric discharges

17 Factors Influencing Discharges to Atmosphere 1. Chemical type and concentration 2. Discharge Phase 3. Discharge Location 4. Scenario Likelihood 5. Disposal Options and Cost

18 Factors Influencing Discharges to Atmosphere - Scenario Likelihood Impacted by the operator overpressure guidelines, training, operating procedures, and credits for available layers of protection Atm CWR CWS HLA LT2 LT1 LC1 Stm Cond

19 Factors Influencing Discharges to Atmosphere 1. Chemical type and concentration 2. Discharge Phase 3. Discharge Location 4. Scenario Likelihood 5. Disposal Options and Cost

20 Factors Influencing Discharges to Atmosphere - Disposal Options and Cost Once all the previous factors are addressed, a comparison of the various disposal options should be implemented. A decision to accept atmospheric discharge should be impacted the least by the cost factor

21 Discharge Location Decision Making Approach Process analysis resulted in identifying applicable overpressure scenario. Toxic vapors are expected. NO Liquid or two-phase discharge is possible. YES Toxic, flammable, or corrosive fluid is expected.

22 Discharge Location Decision Making Approach Toxic, flammable, or corrosive fluid is expected. YES NO Is there a potential for chemical hazard or environmental impact? YES NO Is there an open drain open? NO YES Atmospheric discharge is acceptable. Discharge To closed-system is required.

23 Discharge Location Decision Making Approach NO Toxic vapors are expected. Flammable vapors are expected. YES YES YES Is concentration <25xIDLH? NO Discharge To closed-system is required. Is the discharge velocity >500 ft/s at device capacity? YES Are all points of interest >120 diameters from the discharge point?* NO NO YES NO Are jet effects sufficient to disperse the material at 25% of device capacity?** NO Does a rigorous dispersion modeling indicate that atmospheric release will be safe? Atmospheric discharge is acceptable. YES NO YES

24 Conclusions Safe disposal system decision-making approach should consider atmospheric discharge impact and possible alternative discharge locations. Atmospheric pressure relief should only be considered safe when thorough evaluation is completed. Atmospheric pressure relief valves and common atmospheric vent stack design considerations and risk are not exactly the same. Most flare headers have limited capacity and forcing atmospheric relief valves into potentially undersized headers could create more problems than are solved.

25 Thank you for your attention!

Consequence Modeling and PSM Wilbert Lee Senior Staff Process Risk Engineer Chevron Energy Technology Company

Consequence Modeling and PSM Wilbert Lee Senior Staff Process Risk Engineer Chevron Energy Technology Company Consequence Modeling and PSM Wilbert Lee Senior Staff Process Risk Engineer Chevron Energy Technology Company Consequence Modeling The use of models to assess the potential for injury to persons and damage

More information

Consequence Modeling and PSM Wilbert Lee Safety Technology Unit Chevron Energy Technology Company

Consequence Modeling and PSM Wilbert Lee Safety Technology Unit Chevron Energy Technology Company Consequence Modeling and PSM Wilbert Lee Safety Technology Unit Chevron Energy Technology Company Consequence Modeling The use of models to predict the nature and extent of injury to persons and damage

More information

The Application of Pressure-Impulse Curves in a Blast Exceedance Analysis

The Application of Pressure-Impulse Curves in a Blast Exceedance Analysis The Application of Pressure-Impulse Curves in a Blast Exceedance Analysis Jeffrey D. Marx and Kendall M. Werts Volume 26, Issue 3, May 2013, Pages 478 482 Journal of Loss Prevention in Process Industries

More information

Mitigating Emissions and Maintenance Constraints with Flare Consolidation

Mitigating Emissions and Maintenance Constraints with Flare Consolidation Mitigating Emissions and Maintenance Constraints with Flare Consolidation White Paper Effectively controlling change in a plant environment results in a cumbersome process with an inefficient paper-based

More information

CHEMICAL PROCESS SAFETY; CHEN 455

CHEMICAL PROCESS SAFETY; CHEN 455 CHEMICAL PROCESS SAFETY; CHEN 455 Instructor: Dr. Ray Mentzer, JEB 213 Phone: (979) 458 0090 e-mail: ray.mentzer@chemail.tamu.edu Texas A&M University College Station, TX 77843-3122 Class: 10:20 11:10

More information

STUDY ON THE HARM EFFECT OF LIQUID HYDROGEN RELEASE BY CONSEQUENCE MODELING

STUDY ON THE HARM EFFECT OF LIQUID HYDROGEN RELEASE BY CONSEQUENCE MODELING STUDY ON THE HARM EFFECT OF LIQUID HYDROGEN RELEASE BY CONSEQUENCE MODELING LI. Zhiyong 1, 2, 3, PAN. Xiangmin 2, 3, MENG. Xi 2, 3 2, 3,*, MA. Jianxin 1. College of Civil Engineering and Architecture,

More information

Comparison of Standards Requirements with CFD Simulations for Determining Sizes of Hazardous Locations in Hydrogen Energy Station

Comparison of Standards Requirements with CFD Simulations for Determining Sizes of Hazardous Locations in Hydrogen Energy Station Comparison of Standards Requirements with CFD Simulations for Determining Sizes of Hazardous Locations in Hydrogen Energy Station Abstract Andrei TCHOUVELEV, Gary HOWARD and Vladimir AGRANAT Stuart Energy

More information

Assessment of Toxic Gas Dispersion using Phast and Panache

Assessment of Toxic Gas Dispersion using Phast and Panache Assessment of Toxic Gas Dispersion using Phast and Panache Tejeswi Ramprasad 1, Madhavi Gaonkar 2, Diptendu Das 3 1 ME Research Student, Department of Chemical Engineering, Jawaharlal Nehru Engineering

More information

PRV Stability Project Overview PERF 99-05

PRV Stability Project Overview PERF 99-05 PRV Stability Project Overview PERF 99-05 Ron Darby, PhD, PE and Abdul Aldeeb, PhD Presented to the API 2011 Fall Meeting November 14, 2011 Los Angeles, CA Project Objective To develop a method of predicting

More information

Use of CFD in the Performance-Based Design for Fire Safety in the Oil and Gas Sector

Use of CFD in the Performance-Based Design for Fire Safety in the Oil and Gas Sector Use of CFD in the Performance-Based Design for Fire Safety in the Oil and Gas Sector Camille Azzi* and Lars Rogstadkjenet camille.azzi@gexcon.com GexCon AS Bergen, Norway ABSTRACT This paper addresses

More information

Meeting of April 25 th, 2016 Tampa, FL

Meeting of April 25 th, 2016 Tampa, FL Date Distributed: April 11th, 2016 NATIONAL BOARD SUBGROUP FRP AGENDA Meeting of April 25 th, 2016 Tampa, FL The National Board of Boiler & Pressure Vessel Inspectors 1055 Crupper Avenue Columbus, Ohio

More information

Marshall University College of Information Technology & Engineering Safety Technology Department

Marshall University College of Information Technology & Engineering Safety Technology Department Marshall University College of Information Technology & Engineering Safety Technology Department Fall 2007 PROCESS SAFETY MANAGEMENT SFT 589 LOCATION: Smith Hall, Room 409, Huntington Campus TIME: Tuesdays,

More information

Consequence analysis OIL & GAS CONSULTANCY SERVICES

Consequence analysis OIL & GAS CONSULTANCY SERVICES Consequence analysis OIL & GAS CONSULTANCY SERVICES London London Hong Hong Kong Kong Houston Kuala Lumpur Kuala Lumpur Abu Dhabi Abu Dhabi Dubai Dubai Shanghai Shanghai Managing the risks of Oil & Gas

More information

APPENDIX A WORKBOOK FOR QUALITATIVE RISK-BASED INSPECTION ANALYSIS (UNIT RANKING)

APPENDIX A WORKBOOK FOR QUALITATIVE RISK-BASED INSPECTION ANALYSIS (UNIT RANKING) APPENDIX A WORKBOOK FOR QUALITATIVE RISK-BASED INSPECTION ANALYSIS (UNIT RANKING) A.1 Overview of Qualitative Workbook This workbook presents the details of the qualitative RBI analysis procedure, as described

More information

Class-2 Hazmat Transportation Consequence Assessment On Surrounding Population

Class-2 Hazmat Transportation Consequence Assessment On Surrounding Population Class-2 Hazmat Transportation Consequence Assessment On Surrounding Population U K Chakrabarti, Jigisha K Parikh Chemical Engineering Department, SV National Institute of Technology, Surat, Gujarat, India

More information

SECTION 3 HAZARD ANALYSIS OCS Production Operations

SECTION 3 HAZARD ANALYSIS OCS Production Operations Safety & Environmental Management Issue Date: 07/17/2017 Version 2.3 SECTION 3 HAZARD ANALYSIS Reviewed By Director of Production and Operations Steve Bodden Stone Energy Corporation Reviewed By Director

More information

Current State of PSM

Current State of PSM Current State of PSM Hydrocarbon Process Industry has exacting PSM audit requirements Current state of art tends more to manual or antiquated data processing systems Issues of data migration, operations

More information

Petroleum Production and Disposal Facility Static and Lightning Mitigation

Petroleum Production and Disposal Facility Static and Lightning Mitigation Overview Petroleum Production and Disposal Facility Static and Lightning Mitigation Over the years, there have been an inordinately high number of ignitions caused by lightning and static at petroleum

More information

QRA and ERS: an Integrated Approach

QRA and ERS: an Integrated Approach QRA and ERS: an Integrated Approach An iomosaic Corporation Whitepaper iomosaic Corporation Salem 93 Stiles Road Salem, NH 03079 Tel: 603-893-7009 Fax: 603-893-7885 iomosaic Corporation Houston 2650 Fountain

More information

Analysis & Benchmark of 4 years of HiPo Events and Events with Real Major Consequences in TOTAL RC

Analysis & Benchmark of 4 years of HiPo Events and Events with Real Major Consequences in TOTAL RC Analysis & Benchmark of 4 years of HiPo Events and Events with Real Major Consequences in TOTAL RC D. Roosendans / D. Robillard Department Major Risks TOTAL Refining & Chemicals TOTAL Refining & Chemicals

More information

PEI Candlestick (Utility) Flaring Systems (Theoretical by-products of combustion & destruction efficiency)

PEI Candlestick (Utility) Flaring Systems (Theoretical by-products of combustion & destruction efficiency) PEI Candlestick (Utility) Flaring Systems (Theoretical by-products of combustion & destruction efficiency) This is to certify that all standard PEI designed and manufactured candlestick (utility) type

More information

Abstract. 1. Introduction

Abstract. 1. Introduction Source and dispersion simulation of sour gas in an offshore complex of the sonda de Campeche R. Melo-Gonzalez, M.A. Resales-Torres, J. Martinez- Fernandez, J. Villanueva-Gonzaalez & J. Lopez-Ledesma Instituto

More information

Combustible Gas Issues in Nuclear Safety Panel Discussion

Combustible Gas Issues in Nuclear Safety Panel Discussion Combustible Gas Issues in Nuclear Safety Panel Discussion American Nuclear Society 2014 Winter Meeting Anaheim, CA 11 November 2014 J. Kelly Thomas, Ph.D. 2014 Baker Engineering and Risk Consultants, Inc.

More information

DETERMINATION OF CLEARANCE DISTANCES FOR VENTING OF HYDROGEN STORAGE

DETERMINATION OF CLEARANCE DISTANCES FOR VENTING OF HYDROGEN STORAGE DETERMINATION OF CLEARANCE DISTANCES FOR VENTING OF HYDROGEN STORAGE Tchouvelev, A.V. 1, Benard, P., Agranat, V. and Cheng, Z. 1 1 A.V.Tchouvelev & Associates Inc., 6591 Spinnaker Circle, Mississauga,

More information

Rigorous Simulation of LPG Releases from Accidental Leaks

Rigorous Simulation of LPG Releases from Accidental Leaks A publication of CHEMICAL ENGINEERINGTRANSACTIONS VOL. 26, 2012 Guest Editors:Valerio Cozzani, Eddy De Rademaeker Copyright 2012, AIDIC ServiziS.r.l., ISBN 978-88-95608-17-4; ISSN 1974-9791 The Italian

More information

The planning and design of effective wet duct/stack systems For coal fired utility power plants

The planning and design of effective wet duct/stack systems For coal fired utility power plants The planning and design of effective wet duct/stack systems For coal fired utility power plants David K. Anderson David Anderson is currently a Principal/Owner of Alden Research Laboratory, the oldest

More information

Hazardous Area Classification. Schalk J. P. Kruger

Hazardous Area Classification. Schalk J. P. Kruger Hazardous Area Classification Schalk J. P. Kruger Agenda Legislation Scope of Work (SOW) HAC team Chemicals Operating conditions Method/s of HAC HAC study HAC drawings Practical 2 Legislation Constitution

More information

Process Safety Management (PSM)

Process Safety Management (PSM) Process Safety Management (PSM) General Awareness Training By Gary Whitmore 1 This book is intended to provide the reader with a basic general awareness of the Occupational Safety and Health Administration

More information

LNG as a Marine Fuel Environmental Impact of LNG in Emergency Scenarios

LNG as a Marine Fuel Environmental Impact of LNG in Emergency Scenarios LNG as a Marine Fuel Environmental Impact of LNG in Emergency Scenarios Marcel LaRoche, Lloyd s Register Canada Greentech 2013 Vancouver, BC May 30 th, 2013 Agenda Characteristic s and Hazards of LNG What

More information

Source Characterization of Ammonia Accidental Releases for Various Storage and Process Conditions

Source Characterization of Ammonia Accidental Releases for Various Storage and Process Conditions For Presentation at the Air & Waste Management Association s 90 th Annual Meeting & Exhibition, June 8-13, 1997, Toronto, Ontario, Canada 97-MP8.05 Source Characterization of Ammonia Accidental Releases

More information

Fire Risk Assessment for Ammonia Onshore Export Terminal

Fire Risk Assessment for Ammonia Onshore Export Terminal 4B-2 6th Asia-Oceania Symposium on Fire Science and Technology 17-20, March, 2004, Daegu, Korea Fire Risk Assessment for Ammonia Onshore Export Terminal Yu. N. Shebeko, I. A. Bolodian, V. P. Molchanov,

More information

WORST-CASE CONSEQUENCE ANALYSIS HYDROGEN AND GASOLINE FUELING STATION IN BERKLEY, CALIFORNIA

WORST-CASE CONSEQUENCE ANALYSIS HYDROGEN AND GASOLINE FUELING STATION IN BERKLEY, CALIFORNIA WORST-CASE CONSEQUENCE ANALYSIS HYDROGEN AND GASOLINE FUELING STATION IN BERKLEY, CALIFORNIA Prepared For Fiedler Group 299 N. Euclid Avenue, Suite 550 Pasadena, CA 91101 Prepared By Quest Consultants

More information

The drum can be isolated with the control valves; pressure relief is required. We would like to recover without shutdown; we select a relief valve.

The drum can be isolated with the control valves; pressure relief is required. We would like to recover without shutdown; we select a relief valve. F1 The drum can be isolated with the control valves; pressure relief is required. We would like to recover without shutdown; we select a relief valve. 44 Add relief system to the following process drawing

More information

Synergies between process energy efficiency and relief loads

Synergies between process energy efficiency and relief loads Synergies between process energy efficiency and relief loads Mary Kay O Connor Process Safety Center 2008 Symposium Rob Brendel Jacobs Consultancy Inc. (Chicago) Petroleum, Chemicals & Energy Practice

More information

BOW OR STERN LOADING AND UNLOADING (BLU or SLU) FOR OIL CARRIERS, LIQUEFIED GAS CARRIERS OR CHEMICAL CARRIERS

BOW OR STERN LOADING AND UNLOADING (BLU or SLU) FOR OIL CARRIERS, LIQUEFIED GAS CARRIERS OR CHEMICAL CARRIERS Guide for the Class Notation Bow or Stern Loading and Unloading (BLU or SLU) for Oil Carriers, Chemical Carriers or Liquefied Gas Carriers GUIDE FOR THE CLASS NOTATION FOR BOW OR STERN LOADING AND UNLOADING

More information

Risk Management: a practical approach towards Safety Management

Risk Management: a practical approach towards Safety Management Risk Management: a practical approach towards Safety Management April 17, 2018 Annual European AIChE Seminar www.jacobs.com worldwide Agenda 1. Introduction to Jacobs 2. Risk Management Process Safety

More information

NUTC R203. Safety Risks of Hydrogen Fuel for Applications in Transportation Vehicles. Shravan K. Vudumu

NUTC R203. Safety Risks of Hydrogen Fuel for Applications in Transportation Vehicles. Shravan K. Vudumu Safety Risks of Hydrogen Fuel for Applications in Transportation Vehicles by Shravan K. Vudumu NUTC R203 A National University Transportation Center at Missouri University of Science and Technology Disclaimer

More information

The Benefits of Steam Tracing vs. Electric Tracing. Written by Horst Thieme, PE, James R. Risko and the Fluid Controls Institute Steam Trap Section

The Benefits of Steam Tracing vs. Electric Tracing. Written by Horst Thieme, PE, James R. Risko and the Fluid Controls Institute Steam Trap Section The Benefits of Steam Tracing vs. Electric Tracing Written by Horst Thieme, PE, James R. Risko and the Fluid Controls Institute Steam Trap Section Tech Sheet #ST 102 Many articles have been written concerning

More information

What happens when LNG is released underwater? Does a LNG pool form on the water surface? What are the attributes of the vapor released?

What happens when LNG is released underwater? Does a LNG pool form on the water surface? What are the attributes of the vapor released? What happens when LNG is released underwater? Does a LNG pool form on the water surface? What are the attributes of the vapor released? by Paper Presented at 2009 International Symposium Mary Kay O Connor

More information

PVP INVESTIGATION OF A SHELL AND TUBE EXCHANGER IN LIQUEFIED NATURAL GAS VAPORIZATION SERVICE

PVP INVESTIGATION OF A SHELL AND TUBE EXCHANGER IN LIQUEFIED NATURAL GAS VAPORIZATION SERVICE ASME PVP 2007/CREEP 8 Conference 2007 ASME Pressure Vessels and Piping Division Conference July 22-26, 2007, San Antonio, Texas, USA PVP2007-26592 INVESTIGATION OF A SHELL AND TUBE EXCHANGER IN LIQUEFIED

More information

Technical Papers. 31st Annual Meeting. International Institute of Ammonia Refrigeration. March 22 25, 2009

Technical Papers. 31st Annual Meeting. International Institute of Ammonia Refrigeration. March 22 25, 2009 Technical Papers 31st Annual Meeting International Institute of Ammonia Refrigeration March 22 25, 2009 2009 Industrial Refrigeration Conference & Exhibition The Hyatt Regency Dallas, Texas ACKNOWLEDGEMENT

More information

MSC Guidelines for Review of Oceangoing Tank Barge Cargo Authority Procedure Number: C1-42 Revision Date: 08/01/2018

MSC Guidelines for Review of Oceangoing Tank Barge Cargo Authority Procedure Number: C1-42 Revision Date: 08/01/2018 S. M. PETERSON, LCDR, Chief of Tank Vessel and Offshore Division Purpose: The purpose of this document is to provide guidance and information regarding the submission of the Tank Group Characteristics

More information

Meeting of April 25 th, 2016 Tampa, FL

Meeting of April 25 th, 2016 Tampa, FL Date Distributed: April 11th, 2016 NATIONAL BOARD SUBGROUP FRP MINUTES Meeting of April 25 th, 2016 Tampa, FL These minutes are subject to approval and are for committee use only. They are not to be duplicated

More information

Methane To Markets Partnership Expo October 30 to November 1, 2007 Beijing, China

Methane To Markets Partnership Expo October 30 to November 1, 2007 Beijing, China Methane Emission Measurement Techniques Methane To Markets Partnership Expo October 30 to November 1, 2007 Beijing, China 1 Why Quantify Emission Rates? Justification for repair/control costs. Prioritization

More information

What s On The Horizon: Possible Changes to OSHA s PSM and EPA s RMP Requirements

What s On The Horizon: Possible Changes to OSHA s PSM and EPA s RMP Requirements What s On The Horizon: Possible Changes to OSHA s PSM and EPA s RMP Requirements OCTC Operational Excellence & Sustainability Committee Meeting March 17, 2016 Gary M. Glass (513) 352-6765 Gary.Glass@ThompsonHine.com

More information

A Risk Informed Assessment of Hydrogen Dispensing in Warehouses

A Risk Informed Assessment of Hydrogen Dispensing in Warehouses A Risk Informed Assessment of Hydrogen Dispensing in Warehouses Kumar Bhimavarapu FM Global, Norwood, MA, USA. Abstract: Hydrogen dispensing units are installed increasingly in warehouses to refuel fuel

More information

Consequence-based Safety Distances and Mitigation Measures for Gaseous Hydrogen Refueling Stations

Consequence-based Safety Distances and Mitigation Measures for Gaseous Hydrogen Refueling Stations Page897 EVS Shenzhen, China, Nov -9, Consequence-based Safety Distances and Mitigation Measures for Gaseous Hydrogen Refueling Stations LI. Zhiyong 1, PAN. Xiangmin 2, 3, and MA. Jianxin 2, 3 1 College

More information

Safety challenges in view of the upcoming hydrogen economy: An overview

Safety challenges in view of the upcoming hydrogen economy: An overview Safety challenges in view of the upcoming hydrogen economy: An overview Hans Pasman and William Rogers Mary Kay O Connor Process Safety Center, Texas A&M University, College Station, TX 7784 Contents :

More information

HAZARD EVALUATION USING ALOHA TOOL IN STORAGE AREA OF AN OIL REFINERY

HAZARD EVALUATION USING ALOHA TOOL IN STORAGE AREA OF AN OIL REFINERY HAZARD EVALUATION USING ALOHA TOOL IN STORAGE AREA OF AN OIL REFINERY Praveen Patel 1, Nagendra Sohani 2 1 PhD Scholar, Mechanical Engineering Department, Suresh Gyan Vihar University, Rajasthan, India

More information

Forced Dispersion of LNG Vapor with Water Curtain

Forced Dispersion of LNG Vapor with Water Curtain Forced Dispersion of LNG Vapor with Water Curtain Morshed A. Rana and M. Sam Mannan Artie McFerrin Department of Chemical Engineering Texas A & M University, College Station International Symposium October

More information

Assessment of Risk Zones in A Seveso Plant: A Case Study

Assessment of Risk Zones in A Seveso Plant: A Case Study Modern Environmental Science and Engineering (ISSN 2333-2581) June 2018, Volume 4, No. 6, pp. 530-536 Doi: 10.15341/mese(2333-2581)/06.04.2018/006 Academic Star Publishing Company, 2018 www.academicstar.us

More information

Meeting of October 17 th, 2016 Las Vegas, NV

Meeting of October 17 th, 2016 Las Vegas, NV Date Distributed: October 21st, 2016 NATIONAL BOARD SUBGROUP FRP MINUTES Meeting of October 17 th, 2016 Las Vegas, NV These minutes are subject to approval and are for committee use only. They are not

More information

Chemical Engineering Design

Chemical Engineering Design The safe design and operation of facilities is of paramount importance to every company that is involved in the manufacture of fuels, chemicals and pharmaceuticals Processes must meet acceptable safety

More information

Properties of LNG Don Juckett US Department of Energy February 12, 2002 LNG Workshop Solomons, MD. U.S. Department of Energy

Properties of LNG Don Juckett US Department of Energy February 12, 2002 LNG Workshop Solomons, MD. U.S. Department of Energy Properties of LNG Don Juckett US Department of Energy February 12, 2002 LNG Workshop Solomons, MD U.S. Department of Energy Background LNG in the US US Natural Gas imports and Exports Projections of Market

More information

CFD Based Simulation of LNG Release during Bunkering and Cargo Loading/Unloading Simultaneous Operations of a Containership

CFD Based Simulation of LNG Release during Bunkering and Cargo Loading/Unloading Simultaneous Operations of a Containership Journal of Shipping and Ocean Engineering 7 (2017) 51-58 doi 10.17265/2159-5879/2017.02.001 D DAVID PUBLISHING CFD Based Simulation of LNG Release during Bunkering and Cargo Loading/Unloading Simultaneous

More information

Introduction to Pipeline Quantitative Risk Assessment

Introduction to Pipeline Quantitative Risk Assessment Introduction to Pipeline Quantitative Risk Assessment 66 th Canadian Chemical Engineering Conference October 18 th, 2016 Presented by Sam Sanati, P.Eng, FS Eng. 30 January 2017 1 Pipeline Incident, 2008

More information

Material Safety Data Sheet

Material Safety Data Sheet 1 1 0 Material Safety Data Sheet Black Cohosh Extract, 2.5% Powder MSDS He a lt h Fire Re a c t iv it y Pe rs o n a l Pro t e c t io n 1 1 0 E Section 1: Chemical Product and Company Identification Product

More information

BOW OR STERN LOADING AND UNLOADING (BLU or SLU) FOR OIL CARRIERS, LIQUEFIED GAS CARRIERS OR CHEMICAL CARRIERS

BOW OR STERN LOADING AND UNLOADING (BLU or SLU) FOR OIL CARRIERS, LIQUEFIED GAS CARRIERS OR CHEMICAL CARRIERS Guide for the Class Notation Bow or Stern Loading and Unloading (BLU or SLU) for Oil Carriers, Chemical Carriers or Liquefied Gas Carriers GUIDE FOR THE CLASS NOTATION FOR BOW OR STERN LOADING AND UNLOADING

More information

A PROCESS SAMPLE PROBE WITH IN-SITU ISOLATION AND FILTRATION

A PROCESS SAMPLE PROBE WITH IN-SITU ISOLATION AND FILTRATION A PROCESS SAMPLE PROBE WITH IN-SITU ISOLATION AND FILTRATION Phil Harris HariTec Michael Jenkins Universal Analyzers KEYWORDS Sample Probe, Sample Systems, Sample Handling, Hydrocarbons, Natural Gas ABSTRACT

More information

Using Risk Analysis Tools for Early Project Decision Support

Using Risk Analysis Tools for Early Project Decision Support Alternatives Using Risk Analysis Tools for Early Project Decision Support Goal Irfan Shaikh Risk Management Mary Kay O Connor Process Safety Center Symposium College Station, Texas October 28, 2009 Criteria

More information

Applying Dynamic Process Simulations Toward Flaring Reduction

Applying Dynamic Process Simulations Toward Flaring Reduction Applying Dynamic Process Simulations Toward Flaring Reduction White Paper Siemens AG 2018, All rights reserved 1 Dynamic process simulation has traditionally been a tool of process engineers and process

More information

A-2. An Inherently Safer Process Checklist

A-2. An Inherently Safer Process Checklist An Inherently Safer Process Checklist A-2 This checklist may be used to stimulate the thinking of inherent safety review and process hazard analysis teams, and any other individuals or groups working on

More information

Material Safety Data Sheet

Material Safety Data Sheet Material Safety Data Sheet Brilliant Green Solution, 1% MSDS 1 He a lt h Fire Re a c t iv it y Pe rs o n a l Pro t e c t io n 1 A Section 1: Chemical Product and Company Identification Product Name: Brilliant

More information

Guideline for In-Service Assessment of Ammonia Refrigeration Plants

Guideline for In-Service Assessment of Ammonia Refrigeration Plants Guideline for In-Service Assessment of Ammonia Refrigeration Plants This communication is intended to be used by plant owners and operators to provide guidance in preparation for an assessment of the plant

More information

Methane Emission Reductions in Oil and Gas Processing

Methane Emission Reductions in Oil and Gas Processing Methane Emission Reductions in Oil and Gas Processing EPA Middle East Meeting Washington, D.C. 2 October 2012 Don Robinson ICF International Vice President Agenda U.S. Processing Sector Methane Emissions

More information

Designing wet duct/stack systems for coal-fired plants

Designing wet duct/stack systems for coal-fired plants Page 1 of 8 Designing wet duct/stack systems for coal-fired plants As limits on SO 2 emissions become tighter, many coal-fired utility power plants are adding new flue gas desulfurization (FGD) systems

More information

Risk Analysis of a Chlorine Handling Facility

Risk Analysis of a Chlorine Handling Facility Risk Analysis of a Chlorine Handling Facility Dennis C. Hendershot Rohm and Haas Company Engineering Division P.O. Box 584 Bristol, PA 19007 Presentation to the Technical Seminar on Safety and Health in

More information

Material Safety Data Sheet

Material Safety Data Sheet Material Safety Data Sheet Methyl Violet,.2% MSDS Section 1: Chemical Product and Company Identification He a lt h Fire Re a c t iv it y Pe rs o n a l Pro t e c t io n A Product Name: Methyl Violet,.2%

More information

Material Safety Data Sheet

Material Safety Data Sheet Material Safety Data Sheet Ethidium Bromide, 1% MSDS Not a p He a lt h Fire Re a c t iv it y Pe rs o n a l Pro t e c t io n A Section 1: Chemical Product and Company Identification Product Name: Ethidium

More information

Innovative Multiphase Extraction Design Operating above the Upper Flammability Limit (UFL). Stuart Torr. M.Eng. EIT. October 2005 SYSTEM DESIGN GROUP

Innovative Multiphase Extraction Design Operating above the Upper Flammability Limit (UFL). Stuart Torr. M.Eng. EIT. October 2005 SYSTEM DESIGN GROUP Innovative Multiphase Extraction Design Operating above the Upper Flammability Limit (UFL). Stuart Torr. M.Eng. EIT October 2005 SYSTEM DESIGN GROUP Introduction Background Design Challenges Objectives

More information

ABS TECHNICAL PAPERS 2007

ABS TECHNICAL PAPERS 2007 Fire Risk Assessment of Gas Turbine Propulsion System for LNG Carriers *Kiho Moon 1, Seok-Ryong Song 1, Jorge Ballesio 2, Gary Fitzgerald 3, Gregory Knight 3 ( 1 Hyundai Heavy Industries, 2 American Bureau

More information

Material Safety Data Sheet

Material Safety Data Sheet Material Safety Data Sheet Peppermint Leaf Powder MSDS 0 He a lt h Fire Re a c t iv it y Pe rs o n a l Pro t e c t io n 0 A Section : Chemical Product and Company Identification Product Name: Peppermint

More information

MATH 1050Q Mathematical Modeling in the Environment

MATH 1050Q Mathematical Modeling in the Environment MATH 1050Q Mathematical Modeling in the Environment Lecture 21. Typical Quantitative Principles. Typical Situations. Dmitriy Leykekhman Fall 2010 D. Leykekhman - MATH 1050Q Mathematical Modeling in the

More information

Review of Directed Inspection and Maintenance: Techniques and Technologies for Leak Detection and Quantification.

Review of Directed Inspection and Maintenance: Techniques and Technologies for Leak Detection and Quantification. Review of Directed Inspection and Maintenance: Techniques and Technologies for Leak Detection and Quantification. Oil & Gas Subcommittee. Technology Transfer Workshop January 27, 2009 Monterrey, Mexico

More information

Appendix 1-A Well Testing

Appendix 1-A Well Testing Appendix 1-A Well Testing FLOW TESTING PURPOSE Flow testing is used to determine the performance of oil and gas wells and their economic potential. Various tests will be done to determine the amount of

More information

Amec Foster Wheeler. Canadian Environmental Protection Act (CEPA) E2 Plans: Environmental Emergencies Management

Amec Foster Wheeler. Canadian Environmental Protection Act (CEPA) E2 Plans: Environmental Emergencies Management Amec Foster Wheeler Canadian Environmental Protection Act (CEPA) E2 Plans: Environmental Emergencies Management Auditing Association of Canada Monday, May 8, 2017 By: Tony van der Vooren, Ph.D., P.Eng.,

More information

Public Safety Issues at the Proposed Harpswell LNG Terminal

Public Safety Issues at the Proposed Harpswell LNG Terminal Public Safety Issues at the Proposed Harpswell LNG Terminal James A. Fay 77 Massachusetts Avenue, Rm. 3-258 Cambridge, MA 02139 November 5, 2003 1 Introduction Fairwinds 1 has proposed to lease a site

More information

Introduction to Process Safety Engineering Lessons learned from incidents. By Geert Vercruysse

Introduction to Process Safety Engineering Lessons learned from incidents. By Geert Vercruysse Introduction to Process Safety Engineering Lessons learned from incidents By Geert Vercruysse PS Conference, Dordrecht, 30 th May 2018 8 Safety Functions for a Chemical Plant 1. Prevention of loss of containment

More information

Cheddar or Swiss? How Strong are Your Barriers? Bayan Saab, Process Safety Consultant, FVC International Symposium October 2009

Cheddar or Swiss? How Strong are Your Barriers? Bayan Saab, Process Safety Consultant, FVC International Symposium October 2009 Cheddar or Swiss? How Strong are Your Barriers? Bayan Saab, Process Safety Consultant, FVC 2009 International Symposium October 2009 Bio Bayan Saab 20 years Process/Operations and consulting experience

More information

Material Safety Data Sheet

Material Safety Data Sheet Material Safety Data Sheet Barley grass MSDS 0 He a lt h Fire Re a c t iv it y Pe rs o n a l Pro t e c t io n 0 E Section : Chemical Product and Company Identification Product Name: Barley grass Catalog

More information

NSPI Oil Release Report (as per Environmental Emergency Regulations)

NSPI Oil Release Report (as per Environmental Emergency Regulations) NSPI Oil Release Report (as per Environmental Emergency Regulations) Location (e.g. Region/Address, Generating Station) Date of Spill Time that Nova Scotia Power personnel first learned of spill Type of

More information

COMPLETE REVISION April Process Industry Practices Piping. PIP PNC00004 Piping Stress Analysis Criteria for ASME B31.

COMPLETE REVISION April Process Industry Practices Piping. PIP PNC00004 Piping Stress Analysis Criteria for ASME B31. April 2012 Process Industry Practices Piping PIP PNC00004 Piping Stress Analysis Criteria for ASME B31.3 Metallic Piping PURPOSE AND USE OF PROCESS INDUSTRY PRACTICES In an effort to minimize the cost

More information

Material Safety Data Sheet

Material Safety Data Sheet 0 1 0 Material Safety Data Sheet Nitrogen Standard, 1mgNO3/ml MSDS He a lt h Fire Re a c t iv it y Pe rs o n a l Pro t e c t io n 1 0 0 A Section 1: Chemical Product and Company Identification Product

More information

Material Safety Data Sheet

Material Safety Data Sheet Material Safety Data Sheet Chamomile Flower Extract MSDS 1 2 0 He a lt h Fire Re a c t iv it y Pe rs o n a l Pro t e c t io n 2 1 0 H Section 1: Chemical Product and Company Identification Product Name:

More information

DRAFT Procedures for Quantifying Fugitive VOC Emission Sources at Petroleum Facilities

DRAFT Procedures for Quantifying Fugitive VOC Emission Sources at Petroleum Facilities San Joaquin Valley Unified Air Pollution Control District DRAFT Procedures for Quantifying Fugitive VOC Emission Sources at Petroleum Facilities Approved By: Seyed Sadredin Director of Permit Services

More information

Washington State Ferries

Washington State Ferries SAFETY RISK ASSESSMENT STUDY BASIS Appendix 1 Washington State Ferries Report No. PP061307-02, Rev. 02 Document No.: 167NWYK-13 Date: 2014-06-04 Project name: Safety Risk Assessment Study Basis Det Norske

More information

RULE GASOLINE AND ROC LIQUID STORAGE TANK DEGASSING OPERATIONS (Adopted 11/8/94)

RULE GASOLINE AND ROC LIQUID STORAGE TANK DEGASSING OPERATIONS (Adopted 11/8/94) VENTURA COUNTY AIR POLLUTION CONTROL DISTRICT RULE 74.27 - GASOLINE AND ROC LIQUID STORAGE TANK DEGASSING OPERATIONS (Adopted 11/8/94) A. Applicability Effective 3/31/95, this rule shall apply to: 1. Any

More information

Material Safety Data Sheet

Material Safety Data Sheet Material Safety Data Sheet Methyl Orange Solution,.1% MSDS He a lt h Fire Re a c t iv it y Pe rs o n a l Pro t e c t io n A Section 1: Chemical Product and Company Identification Product Name: Methyl Orange

More information

Material Safety Data Sheet

Material Safety Data Sheet Material Safety Data Sheet Apricot Flavor MSDS 0 He a lt h Fire Re a c t iv it y Pe rs o n a l Pro t e c t io n 0 A Section : Chemical Product and Company Identification Product Name: Apricot Flavor Catalog

More information

Got Chemicals? The State of Play on Chemical Security Regulations

Got Chemicals? The State of Play on Chemical Security Regulations Got Chemicals? The State of Play on Chemical Security Regulations December 17, 2014 Speakers: Warren Lehrenbaum Daniel W. Wolff Evan D. Wolff The webinar will begin shortly, please stand by. The materials

More information

Pipeline Risk Management

Pipeline Risk Management trebol_52_ing 19/2/10 14:19 P gina 11 Pipeline Risk Management Ricardo Rodrigues Chemist, Executive Director do ITSEMAP Brazil 10/ 52 / 2010 trebol_52_ing 19/2/10 14:19 P gina 12 Major advances in Brazil

More information

Material Safety Data Sheet

Material Safety Data Sheet Material Safety Data Sheet Ammonium Lactate, 7% MSDS 2 He a lt h Fire Re a c t iv it y Pe rs o n a l Pro t e c t io n 2 H Section 1: Chemical Product and Company Identification Product Name: Ammonium Lactate,

More information

CHAPTER 5 FLAME & EXPLOSION

CHAPTER 5 FLAME & EXPLOSION CHAPTER 5 FLAME & EXPLOSION Flame Definition Relatively fast Exothermic Gas phase reaction Subsonic propagation Usually emits light Deflagration Combustion wave that travels sub-sonically relative to the

More information

Material Safety Data Sheet

Material Safety Data Sheet 1 1 0 Material Safety Data Sheet 1,2-Bis(2-methoxyethoxy)ethane MSDS He a lt h Fire Re a c t iv it y Pe rs o n a l Pro t e c t io n 1 1 0 A Section 1: Chemical Product and Company Identification Product

More information

vapor control systems Quality, Dependability, Service. Reputation Built on Valve Concepts, Inc. com A Cashco, Inc.

vapor control systems Quality, Dependability, Service. Reputation Built on Valve Concepts, Inc.   com A Cashco, Inc. vapor control A Cashco, Inc. Company systems Reputation Built on Quality, Dependability, Service. Get Consistent Quality By involving every employee in our ISO 9001:2000 Quality Assurance Program, you

More information

Industrial Aspects of Deflagration & Detonation in Pipelines. Presented by: Tony Ennis Haztech Consultants Ltd

Industrial Aspects of Deflagration & Detonation in Pipelines. Presented by: Tony Ennis Haztech Consultants Ltd Industrial Aspects of Deflagration & Detonation in Pipelines Presented by: Tony Ennis Haztech Consultants Ltd www.haztechconsultants.com 1 A Quotation to Start What has happened before will happen again

More information

A Course on Health, Safety & Accident Management

A Course on Health, Safety & Accident Management Session 1413 A Course on Health, Safety & Accident Management Ann Marie Flynn, Joseph Reynolds, and Louis Theodore Department of Chemical Engineering Manhattan College Riverdale, New York I. Introduction

More information

Material Safety Data Sheet

Material Safety Data Sheet 2 1 0 Material Safety Data Sheet Strawberry concentrate, colorless (flavor) MSDS He a lt h Fire Re a c t iv it y Pe rs o n a l Pro t e c t io n 1 2 0 A Section 1: Chemical Product and Company Identification

More information

Accreditation of Hot Tap Organizations

Accreditation of Hot Tap Organizations Accreditation of Hot Tap Organizations TSSA Guide for Survey Teams Technical Standards & Safety Authority Boiler & Pressure Vessels Safety Division 3300 Bloor Street West 14 th Floor, Centre Tower, Etobicoke,

More information

Comparative Quantitative Risk Assessment (QRA) Approach ON large Scale Underground Pipelines. Dohyung KIM, Jungwhan KIM, Seungho JUNG

Comparative Quantitative Risk Assessment (QRA) Approach ON large Scale Underground Pipelines. Dohyung KIM, Jungwhan KIM, Seungho JUNG Comparative Quantitative Risk Assessment (QRA) Approach ON large Scale Underground Pipelines Dohyung KIM, Jungwhan KIM, Seungho JUNG Environmental and Safety Engineering, Ajou University, Suwon City, Republic

More information