
Guidelines for Determining the Probability of Ignition of a Released Flammable Mass
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FORWARD XI
1 INTRODUCTION 1
1.1 Objectives 1
1.2 Motivation for this Book 1
1.2.1 A Brief History of Fire Protection 2
1.2.2 The Development of Risk-Based Approaches to Flammables Management 3
1.2.3 Difficulties in Developing Ignition Probability Prediction Methods 4
1.2.4 Missing Variables 5
1.2.5 Summary of Industry Needs and Path Forward 5
1.2.6 Applications for This Book 6
1.2.7 Limitations in Applying the Approaches in This Book 7
1.3 Ignition Probability Overview 8
1.3.1 Theoretical Basis for Ignition 8
1.3.2 Key Ignition Factors Related to the Properties of the Fuel, and Available Surrogates that can be Used for Developing Probability of Ignition Predictions 13
1.3.3 Key Ignition Factors Related to the Release Source 19
1.3.4 Key Ignition Factors Related to the External Environment After the Release 27
1.4 Control of Ignition Sources 30
1.4.1 Ignition Source Management 30
1.4.2 Minimization of Release 33
1.5 Vapor Cloud Explosion Probability Overview 33
1.6 Detonation Overview 35
1.6.1 Detonation Using a Strong Ignition Source 35
1.6.2 Deflagration-to-Detonation Transition 35
1.6.3 Buncefield 35
1.7 Other Ignition Topics - Hydrogen 36
1.7.1 Ignition Mechanisms 36
1.7.2 Other Hydrogen Ignition Topics 37
2 ESTIMATION METHODS 39
2.1 Introduction 39
2.1.1 Event Tree 39
2.1.2 Failure Frequency Data for Use in Event Trees 41
2.1.3 Quantification of the Event Tree 41
2.2 Factors Influencing the Probability of Immediate Ignition 41
2.2.1 Temperature of Release Relative to the Autoignition Temperature 42
2.2.2 Minimum Ignition Energy (MIE) of Material Being Released 42
2.2.3 Pyrophoricity of Released Material 44
2.2.4 Pressure/Velocity of Discharge 44
2.2.5 Droplet Size 45
2.2.6 Presence of Particulates 46
2.2.7 Configuration/Orientation of Equipment Near/At the Point of Release 46
2.2.8 Temperature of Release (as it relates to its effect on MIE) 46
2.2.9 Phase of Release (API RBI) 47
2.2.10 Flash Point and Release Rate (TNO) 47
2.3 Factors Influencing the Probability of Delayed Ignition 47
2.3.1 Strength and Numbers of Ignition Sources 47
2.3.2 Duration of Exposure 51
2.3.3 Release Rate/Amount 51
2.3.4 Material Being Released 53
2.3.5 Release Phase/Flash Point/Boiling Point 53
2.3.6 Distance from Point of Release to Ignition Source 54
2.3.7 Meteorology 54
2.3.8 Events Originating Indoors 54
2.4 Factors Influencing the Probability of Explosion, Given Delayed Ignition 57
2.5 Potential Interdependence of Variables 57
2.6 Summary of Variables Used in Each Analysis Level 58
2.7 Basic (Level 1) Probability of Ignition Algorithms 59
2.7.1 Level 1 Algorithm for Probability of Immediate Ignition 59
2.7.2 Level 1 Algorithm for Probability of Delayed Ignition 60
2.8 Level 2 Probability of Ignition Algorithms 61
2.8.1 Level 2 Algorithm for Probability of Immediate Ignition 61
2.8.2 Level 2 Algorithm for Probability of Delayed Ignition 62
2.9 Advanced (Level 3) Probability of Ignition Algorithms 67
2.9.1 Level 3 Algorithm for Probability of Immediate Ignition 67
2.9.2 Level 3 Algorithm for Probability of Delayed Ignition 67
2.10 Developing Inputs When Chemical Properties Are Not Available 69
2.10.1 Estimating Input Properties of Chemicals Not in the Pick List 69
2.10.2 Estimating the Properties of Flammable Mixtures 71
2.11 Worked Example 73
2.11.1 Problem Statement 73
2.11.2 Level 1 Analysis 74
2.11.3 Level 2 Analysis 75
2.11.4 Level 3 Analysis 76
2.12 Application of the Models to a Study with Multiple Ignition Sources 77
3 TECHNICAL BACKGROUND AND DATA SOURCES 78
3.1 Introduction and Summary 78
3.2 Government-driven studies 82
3.2.1 Rew et al. 82
3.2.2 Bevi Risk Assessment Manual (TNO Purple Book) 91
3.2.3 HSE / Crossthwaite, et al. 95
3.2.4 HSE/Thyer 95
3.2.5 HSE/Gummer and Hawksworth - Hydrogen 97
3.2.6 Cawley/U.S. Bureau of Mines 98
3.2.7 Canvey 99
3.2.8 Witcofski (NASA) Liquid Hydrogen 100
3.3 Information Developed by Industry Groups 100
3.3.1 Cox/Lees/Ang 100
3.3.2 E&P Forum 103
3.3.3 API RBI 103
3.3.4 API RP 2216 108
3.3.5 IEEE 109
3.3.6 UK Energy Institute 110
3.4 Information Developed in Academia 113
3.4.1 Ronza, et al. 113
3.4.2 Offshore Explosions (Loughborough) 116
3.4.3 Srekl and Golob 116
3.4.4 Duarte et al. 117
3.4.5 Swain - Ignition of Hydrogen 118
3.4.6 Dryer et al. - Hydrogen and Light Hydrocarbons 118
3.4.7 Britton - Silanes and Chlorosilanes 119
3.4.8 Pesce et al. 120
3.5 Information Developed by Individual Companies 121
3.5.1 Spouge 121
3.5.2 Moosemiller 122
3.5.3 Johnson - Humans as Electrostatic Ignition Sources 123
3.5.4 Jallais - Hydrogen 125
3.5.5 Zalosh - Hydrogen 125
3.5.6 Smith - Pipelines 127
3.6 Studies Specific to Ignition of Sprays 128
3.6.1 Lee et al. 128
3.6.2 Babrauskas 130
3.7 Case Histories 131
3.7.1 Britton - External Ignition Events 131
3.7.2 Pratt - Gas Well and Pipeline Blowouts 132
3.7.3 Gummer and Hawksworth - Hydrogen Events 133
4 ADDITIONAL EXAMPLES 136
4.1 Introduction to Examples, and Potential "Lessons Learned" 136
4.1.1 "Reality" vs. Predictions 136
4.1.2 "Conservatism" - Does it Exist? 137
4.1.3 Cases where the Model may not be Appropriate or the Results Misinterpreted 138
4.1.4 Summary of Worked Examples 139
4.2 Worked Examples (based on other CCPS books) 140
4.2.1 "Vapor Cloud Explosion Hazard Assessment of a Storage Site" 140
4.2.2 "Open Field Release of Propane" 145
4.2.3 "Release from Pipeline" 149
4.3 Worked Examples (chemical and petrochemical plants) 152
4.3.1 "Ethylene Tubing Failure" 152
4.3.2 "Benzene Pipe Rupture" 154
4.3.3 "Spill from Methyl Ethyl Ketone Tank" 155
4.3.4 "Indoor Puncture of MEK Tote" 158
4.3.5 "Elevated Release" 161
4.4 Worked Examples (oil refineries) 164
4.4.1 "Gasoline Release from a Sight Glass" 164
4.4.2 "Overfilling a Gasoline Storage Tank" 168
4.4.3 "Overfilling a Propane Bullet" 170
4.4.4 "Hydrogen Release from a Sight Glass" 172
4.5 Worked Examples (Unusual Cases) 174
4.5.1 "Indoor Acid Spill - Ventilation Model" 174
4.5.2 "Release of Ammonia" 179
4.6 Worked Examples ('Out of Scope' Cases) 180
4.6.1 "Release of Gas from an Offshore Platform Separator" 180
4.6.2 "Dust Ignition" 183
4.7 Worked Examples of the Benefits of Plant Modifications and Design Changes 186
4.7.1 "Ignition by Hot Surfaces" 186
4.7.2 Release Prevention 189
4.7.3 Duration of Exposure 189
4.7.4 Benefit of Improved Ventilation of Indoor Releases - Continuation of "Indoor Acid Spill" Example 192
5 SOFTWARE ILLUSTRATION 194
5.1 Explanation and Instructions for Software Tool 194
5.2 Opening the Software Tool 194
5.3 General Inputs and Outputs 195
5.4 Level 1 Inputs 196
5.5 Level 2 Analyses 198
5.6 Level 3 Analyses 200
5.7 Explosion Probability 200
5.8 Illustrations of Software Use 201
5.8.1 "Vapor Cloud Explosion Hazard Assessment of a Storage Site" (example from Section 4.2.1) 201
5.8.2 "Open Field Release of Propane" (example from Section 4.2.2) 204
APPENDIX A. CHEMICAL PROPERTY DATA 207
APPENDIX B. OTHER MODELS FOR CONSIDERATION 213
CHAPTER 1
INTRODUCTION
1.1 OBJECTIVES
The goal of this book is to provide information and methods that can be used to estimate the probability of ignition for flammable gas and liquid releases to the external environment. This book and the accompanying software tools discuss technical material that the user should be familiar with prior to use. This book is intended for an audience of engineers and/or scientists who have experience with process safety and risk management systems.
The algorithms that are developed in this book are presented at different levels of sophistication to accommodate a wide range of users, including people in a process hazard analysis team who want an objective but crude prediction for risk ranking purposes or people performing quantitative risk assessments and developing relatively complex risk mitigation plans. Users can adopt the level of complexity and accuracy needed for their particular application with a commensurate level of effort in data input.
The scope of this book is limited to flammable gases, mists, and liquids. The designed application is for onshore facilities, although it may be possible to extend it to offshore applications if the user is able to properly account for the inherent differences between the two settings. This book specifically excludes the treatment of ignitable dusts for various reasons, not the least of which are: (a) the magnitude and physicochemical characteristics of dust clouds are very difficult to quantify for a given situation, particularly for dust “disturbance” events (in which accumulated dust dislodges from the tops of equipment and support structures) and (b) ignition probability data for dust ignitions are very limited at this time.
1.2 MOTIVATION FOR THIS BOOK
Up until the 1990s, many companies maintained groups of process safety specialists whose experience and expertise in different areas allowed in-house problem solving. Often, companies not only maintained safety test laboratories but performed safety research as well. Unfortunately, as safety technology has advanced it has become more complicated and difficult for most companies to apply. This book is intended to assist in-house risk analysts in one of the most difficult areas—estimating the probability of ignition of a given vapor cloud.
The motivation for this book is to achieve the following three primary outcomes:
- A standardized methodology for estimating probability of ignition that is open-source and can be applied consistently across the process industry
- Methods and tools that allow a user to estimate ignition probability quickly
- Ability to account for mitigation measures that reduce ignition probability
On the last bullet above, it is desired that a tool be able to address as many of the elements of the “fire triangle” as possible. In fact, the methods can address all sides of the triangle to varying degrees, but none completely, and all resulting in reductions in ignition probability rather than elimination of ignition altogether.
1.2.1 A Brief History of Fire Protection
Many catastrophic accidents in the process industries have resulted from the ignition of a flammable mass that was released into the environment. For this reason, safety professionals and regulators have continually sought methods to reduce the frequency of such events, and various approaches have been undertaken to accomplish this. Before the implementation of industry standards and codes, professionals used their individual and/or collective knowledge of past events and fire fundamentals to mitigate such events. Even in ancient Rome, the Emperor Nero developed regulations for fire protection after the city burned in A.D. 64. The Roman regulations included requirements for fire-resistant building materials and the use of separation distances, concepts that are still in use today.
The evolution from this knowledge-based approach into a series of industry-driven standards and codes occurred in order to share knowledge of flammable hazard management and to introduce standardized methods for dealing with flammable hazards. Not surprisingly, the nascent insurance industry of the nineteenth century promoted this initial effort, and various professional organizations were created in the twentieth century such as the National Fire Protection Association (NFPA), Society of Fire Protection Engineers (SFPE), and others in the U.S. and overseas. These organizations were instrumental in developing the field of flammables management.
The science of ignitions in the petroleum, chemical, and other industries developed in parallel. Klinkenberg and van der Minne (1958) provide references on static electricity in the industry that date back to the 1910s, The U.S. Bureau of Mines had a leading role in progressing knowledge in this area in the same time frame. Through these efforts and contributions by others in industry, advancements in both the theory and experimental support for these phenomena were made through the middle of the twentieth century.
As the chemical and petrochemical industries matured and grew, the potential for fires and explosions of ever-greater magnitudes also grew, and some tragic events such as those in Flixborough, Piper Alpha, Mexico City, and Pasadena drove regulators to become more intimately involved in the management of flammable hazards. In the U.S., the promulgation of the Occupational Safety and Health Administration’s “Process Safety Management of Highly Hazardous Chemicals” standard in 1992 set the stage for the regulation of such hazards, although the standard is largely built on and refers to the industry efforts that preceded it.
1.2.2 The Development of Risk-Based Approaches to Flammables Management
The most recent evolution of flammables management is the use of risk-based approaches. In a risk-based approach, the expected frequency of a fire or explosion is quantified and combined with the predicted outcome of the fire/explosion to determine the risk of a potential hazard. To some extent, this evolution has been driven by the increasing availability of the computing power required to perform detailed analyses for thousands of scenario combinations that can be present in a modern process industry facility. This was also coincident with a rise of risk-based “culture” and risk-based regulations in Europe in particular.
The development of the quantified risk-based methodologies in recent years has been accompanied by tremendous advancements in the theory, tools, and software available to predict the consequences of fires and explosions. Although the methods for consequence analysis continue to improve, one can argue that the methods for consequence analysis are fairly mature and thus address half of the “risk equation”:
Risk = f(Consequence, Frequency)
or, in terms familiar to practitioners of layers of protection analysis:
Risk = Consequence x Frequency/Risk Reduction Factors
The frequency side of the risk equation seems simpler conceptually and does not need to invoke Gaussian plume or computational fluid dynamics or other relatively higher mathematical solutions. In spite of this, or possibly because of this, the frequency of events has been a relatively neglected science. Now that is changing; because some regulators (mainly outside North America) require companies to perform quantified risk assessments, the regulators themselves have started to undertake standardization of frequency inputs to such studies. For example, some risk analysts are required to use specific values for the frequency of a leak of size X from a pressure vessel. While there is broad consensus on the values of many of these numbers in a “generic” situation, some inputs such as ignition probabilities are very situation-specific and so should be handled with greater rigor in many situations than is generally practiced.
Improvements to previous frequency/risk calculation methods are also timely given that the American Petroleum Institute (API) Recommended Practice 752 on building siting (API, 2009) permits use of risk as a basis for making building and personnel location decisions. Since the risk calculation for flammable events invariably incorporates a probability of ignition, greater precision and consistency in estimating this value are needed to ensure that risk assessments are both technically accurate and performed consistently across industry. Among other purposes, this book is therefore intended to provide new tools for users to comply with this API recommended practice and can be considered as a companion document to the CCPS book Guidelines for Evaluating Process Plant Buidings for External Explosions, Fires, and Toxic Releases (CCPS, 2012) as well as a supplemental resource for the CCPS book Guidelines for Enabling Conditions and Conditional Modifiers in Layer of Protection Analysis (CCPS, 2013).
1.2.3 Difficulties in Developing Ignition Probability Prediction Methods
From a mathematical point of view, determining ignition probabilities would seem to be a straightforward problem to solve—simply collect information or perform tests on events where flammables have been released and document the instances in which an ignition took place. However, the execution of this strategy is problematic from multiple perspectives, discussed next.
1.2.3.1 Data Bias
The simplest form of data analysis to develop ignition probability predictions is the following:
Probability of Ignition = Observed Ignitions/Observed Flammable Releases
There are numerous cases in which an event that resulted in a major fire or explosion has been documented in some form...
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