The risk of fire is present during all stages and operations of the petroleum industry, whether during exploration and production (E&P) both in onshore and offshore installations or during refining/processing or transportation, storage or during dispensing to the end user. All petroleum products from crude to final products produce vapor that is being mixed with air creating the potential for ignitable mixture. While petroleum products have different rates of releasing vapors to the environment, they all share the risk of starting a fire when an ignition source is introduced to the mixture. Fires involving hydrocarbons can take several shapes from pool fires to fire balls and jet fires. Due to the severity and Heat Release Rate (HRR) of Hydrocarbon fires (which may result in catastrophic consequences), fire prevention, protection and mitigation measures are considered to be of utmost importance/most advanced in relation to same measures in other industries.

Hydrocarbons release vapor to the surrounding environment creating a mixture with air. This vapor/air mixture can take different concentrations depending on many factors. A fire can start if this mixture has concentration between two levels referred to as Lower Flammability limit (LFL) and Upper Flammability Limit (UFL). Any vapor/air concentration lass than LFL is considered too lean to burn and any concentration above UEL is too rich to burn. In the petroleum industry a facor of safety of 4 is normally used (that is several measures are in place to limit the vapor/air mixure concentration to 25 % of the Lower Flammability Limit (LFL) concentration).

Fire is a rapid chemical change that releases heat and light and is accompanied by flame, especially the exothermic oxidation of the flammable/combustible material.

For a fire to start, three elements must be present simultanuously:

  1. Combustilble material (solid, liquid or gas).

  2. Supply of air (oxygen) that is neccary for the combustion process.

  3. Introduction of ignition source (flame, spark, static electricity, heat, …).

To extinguish fire, one or more of the three fire triangle elements will have to be eliminated.

Class A fires: Involving ordinary combustibles (wood, clothing, papers,…) (extinguished by water, CO2, dry chemicals).

Class B fires: Involving hydrocarbons (both liquid and gas) and to be extinguished by (Foam,dry chemicals, Clean Agents (Halon replacements) and Fine Water Mist systems).

Class C fires: Involving electrical wiring and equipment. To be extinguished by CO2, dry chamicals and Clean Agents (Halon replacements).

Class D fires: involving metals. To be extinguished by special dry chemicals.

Fires in production facilities can be : Well blowout fires, flash fires, liquid pool fires, gas pool fires, jet fires, running liquid fires, confined and unconfined fires, etc.

Leakage in any piping system or equipment/vessels can result in jet fires, fire balls, liquid/gas pool fires, running liquid fires, etc.

A leakage in any transportation mode (network of piping, rail cars, tankers may result in jet fires, running liquid fires, pool fires, etc.

A leakage in any storge tank can result in jet fires, pool fires, running liquid fires.

The threat from fire is present at all times in the petroleum industry. To prevent fires from starting in the first place several measures have to be implemented including the proper design, proper construction matereials, proper processes and strict control of transient combustibles and ignition sources. Selecting the proper detection/suppression system provide assurance of controlling and extinguishing any potential fires as soon as they start developing. While having properly trained response tean provide assurances of mitigating any effects from any potential fire. Such measures will have to be reviewed and examined/updated periodically. While the fire science/technology is rapidly developing, the latest technology (whether in prevention, suppression, mitigation or analysis techniques) should always be applied in the petroleum industry to provide extra assurances for the safety of operators and production continuity. With the increased demand for oil on a global basis and the increased cost of producing, processing and storing petroleum and oil products, the fire safety becomes more prioritized than ever before.

This paper was selected for presentation by an SPE Program Committee following review of information contained in an abstract submitted by the author(s). Contents of the paper, as presented, have not been reviewed by the Society of Petroleum Engineers and are subject to correction by the author(s). The material, as presented, does not necessarily reflect any position of the Society of Petroleum Engineers, its officers, or members. Papers presented at SPE meetings are subject to publication review by Editorial Committees of the Society of Petroleum Engineers. Electronic reproduction, distribution, or storage of any part of this paper for commercial purposes without the written consent of the Society of Petroleum Engineers is prohibited. Permission to reproduce in print is restricted to an abstract of not more than 300 words; illustrations may not be copied. The abstract must contain conspicuous acknowledgment of where and by whom the paper was presented. Write Librarian, SPE, P.O. Box 833836, Richardson, Texas 75083-3836 U.S.A., fax 01-972-952-9435.

The author would like to express gratitude for several memebers of Socity of Petroleum Engineers (SPE) for their guidance and support during the course of this work.

Center for Chemical Process Safety (CCPS)
Guidelines for Fire Protection in chemical, petrochemical and hydrocarbon processing facilities
American Institute of Chemical Engineers
New York, NY