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Contents
  1. 1Actions on a fire
    1. 1.1A simple cooling calculation
  2. 2Matching the agent to the fuel
  3. 3Forms and delivery
  4. 4Compatibility and secondary effects
  5. 5Selection and application evidence
  6. 6Control, extinction and re-ignition
  7. 7Performance and limits
  8. 8See also
  9. 9Notes
  10. 10References

An Extinguishing agent is a substance used to stop combustion, limit its spread or prevent it from starting again. Water, foam, dry powders and gaseous agents work in different ways. Their performance depends on the fuel, fire form, enclosure, delivery method and compatibility with surrounding materials.[1][2]

An agent is not defined by one universal action. Water often cools both fuel and flame, while foam can separate a liquid surface from air and radiant heat. Powders can interfere with flame chemistry and coat a solid. A single discharge can combine several of these actions.[1][3]

Selection therefore begins with the fire rather than with a preferred product. The agent must reach the burning region in a useful form and remain effective long enough. An agent that removes visible flame may still leave hot fuel or deep-seated combustion capable of re-ignition.[4][5]

Actions on a fire

The Extinguishing mechanisms described in NUREG-1805 fall into four groups. Fuel can be separated from the flame, oxygen can be removed or diluted, temperatures can be reduced, or chemicals can modify combustion reactions. Real agents commonly use more than one group at the same time.[1]

Four panels show fuel separation, oxygen reduction, cooling and chemical interference.
Four groups of extinguishing action can occur together. Based on Iqbal and Salley (2004), p. B-15.

Cooling water reduces the production of gaseous fuel from a heated solid. It also reduces flame temperature and the feedback of heat to that solid. Water turning to steam can additionally impede oxygen supply in some confined conditions, while fog can reduce radiant heat transfer.[1]

Water absorbs energy while its temperature rises and absorbs further energy when it evaporates. Specific heat describes the first contribution; latent heat describes the phase change. These properties help explain cooling, but neither gives a universal quantity of water needed to extinguish a fire.[6][7][2]

Foam acts differently on a liquid pool. A blanket limits contact with air and reduces radiant heating of the liquid. Cooling can reduce vapour pressure, while water draining from foam can dilute a water-soluble fuel. These contributions vary with the liquid and the condition of the blanket.[1]

Dry chemicals can affect active species in flame reactions. They can also absorb heat, obstruct radiation and, for some formulations, form a surface coating. Particle size and chemical composition both affect performance, so powder cannot be selected by mass alone.[3]

Gaseous agents include halocarbon and inert-gas types. Their actions differ: heat absorption and chemical effects contribute to halocarbon performance, while inert gases primarily reduce oxygen availability. The balance depends on the particular agent, so the behaviour of Halon 1301 does not define every halocarbon substitute.[8]

A simple cooling calculation

The sensible heat absorbed by water equals its mass multiplied by its specific heat and temperature rise. This calculation describes heating within the liquid phase. It uses a constant specific heat over the chosen interval, as in Van Rossum's introductory method.[6]

Es=mcp(T2−T1)

Symbol Description Unit
Es Sensible energy absorbed J
m Mass of water kg
cp Specific heat at constant pressure J/(kg K)
T1,T2 Initial and final liquid temperatures °C

For a 1 kg calculation basis, water initially at 20 °C is heated to 100 °C. Using the tabulated water value of 4,186 J/(kg K), the temperature increase is 80 K. The resulting sensible energy is approximately 335 kJ; this calculation assumes that the water remains liquid until the final temperature.[6][2]

Es=1×4186×80=334880 J≈335 kJ

Evaporation would absorb additional energy, which is excluded from this result. Water that misses the heated material or drains away early may absorb much less than the illustrative quantity. A heat-capacity calculation therefore explains one mechanism without predicting application efficiency, nozzle performance or extinguishment.[7][9]

The distinction between energy and rate is also relevant. Energy measures an accumulated quantity of heat, whereas the fire's heat-release rate describes energy released per second. Comparing a quantity in kilojoules directly with a fire size in kilowatts would omit the duration of heat transfer.[10]

Matching the agent to the fuel

Fire classes group fires to support agent selection, but their letters and meanings differ between systems. The examples here use the US classifications reproduced in NUREG-1805. They should not be treated as identical to classifications used elsewhere.[11]

Ordinary combustibles such as wood, cloth and paper can often be cooled and wetted with water. Some dry powders also form a coating over these materials. That coating can matter where glowing or deep-seated combustion remains after the flames have disappeared.[11][12]

Flammable-liquid fires require attention to the liquid's behaviour. Water is denser than many hydrocarbon fuels and does not mix with them. Such fuel can float and continue burning, so an appropriate Firefighting foam may provide a surface blanket where plain water cannot.[2][13]

Selection moves from fuel and geometry to compatibility, delivery and post-discharge hazards.
Agent selection depends on more than a fire-class letter. Based on Iqbal and Salley (2004), pp. B-15–B-16 and Scheffey (2002), p. 4-88.

Water-miscible liquids present a different problem. Sufficient water can dilute them, but that can take a long time in a deep pool. Alcohol-resistant foam is formulated to protect its blanket against breakdown by polar solvents, making formulation more specific than a generic foam label.[14][5]

Energised electrical equipment changes the selection because an electrically conductive stream can create a shock hazard. NUREG-1805 identifies particular nonconductive agents for its US Class C examples. The classification concerns the electrical condition, not a new fuel that disappears when power is isolated.[11]

Combustible metals need agents tested for the particular metal and situation. NUREG-1805 warns against water-based agents in its Class D table because an agent must not react harmfully with the metal. A general-purpose label is not evidence of suitability for every metal fire.[11]

Cooking oils and fats also require suitable application. Water introduced beneath very hot oil can vaporise and eject burning material. Wet chemical and other agents listed for the applicable fire classification must be distinguished from an arbitrary water discharge.[11][14]

Forms and delivery

A Fire extinguisher stores a limited quantity for manual use. Its contents, nozzle and operating arrangement are designed as one unit. The label and tested application are therefore more informative than the appearance of the cylinder or the broad agent family.[12][15]

Fixed systems can deliver an agent through a pipe network and nozzles. Water-based sprinkler systems release water where heat opens individual heads in common arrangements. Deluge systems instead use open outlets and a separate detection system, so the area receiving water is determined differently.[16]

A Water mist system divides water into a fine spray containing a range of droplet sizes. Mawhinney and Back describe the 2002 fire-protection use of the term as including droplets up to 1 mm. Their definition distinguishes these sprays from a scientific mist; it is not presented as a current product certification criterion.[17]

A Gaseous extinguishing system can distribute agent through an enclosure without the residue associated with powders. Enclosure leakage, openings and ventilation can reduce concentration. Deep-seated material can also remain hot after surface flames disappear, leading to renewed burning when air returns.[4]

Foam delivery involves proportioning concentrate into water, generating bubbles and distributing the foam. Each stage affects the final blanket. A correct concentrate stored beside an incompatible proportioner or application device does not establish a functioning suppression system.[15]

Agent quantity and application rate must be considered together. Foam exposed to flame breaks down and loses water, so application must replace losses while preserving a residual layer. For powders and gases, losses through openings can likewise reduce the amount remaining at the fire.[18][12]

Compatibility and secondary effects

No agent is universally harmless. Water can react with particular materials to produce heat, flammable or toxic gases, or explosions. Fleming notes that sufficient water can sometimes overcome a reaction involving minor quantities, but that does not make water a default choice for reactive substances.[2]

Water and water-based foam can also create electrical hazards. Their use near energised equipment must follow the tested system and applicable safety arrangements. Extinguishing the original fire does not remove hazards introduced by the extinguishing medium.[15]

Dry powder discharge can reduce visibility and cause temporary breathing difficulty. Residue requires cleaning and can damage delicate electrical equipment. Monoammonium phosphate is described in NUREG-1805 as more corrosive than several alternative powders because of its acidic products.[12][19]

Gaseous agents can change the atmosphere within an enclosure. Their physiological effects depend on the agent and concentration, so they cannot all be treated as safe merely because they leave little residue. System design must address occupancy and exposure conditions for the particular agent.[8]

Fire effluent and agent decomposition products can remain after discharge. Historical descriptions of Halon performance in NUREG-1805 belong to their period and application. They are not evidence of current environmental acceptability or permission to install a particular substance.[20]

Selection and application evidence

Agent selection starts by defining the physical fire problem. A surface flame, a deep-seated solid fire and a running-liquid fire present different targets. The target determines whether cooling, surface coverage or chemical flame inhibition is most useful, and whether the agent can physically reach it.[1][13]

Geometry can change the result even when the fuel remains the same. Scheffey distinguishes a two-dimensional liquid pool from a pressurised spray or running fuel. Foam that spreads across a horizontal pool may not cover the moving surfaces of the three-dimensional fire.[13]

The agent's state during storage and discharge also matters. Water can be delivered as a conventional spray or as fine droplets, while gases can be stored under pressure and dispersed through a room. Dry powder must flow without caking and be projected into the fire by a gas.[17][3]

Formulation properties need to survive the complete delivery process. Foam must be proportioned and aerated correctly, powder must retain suitable flow characteristics, and gas must disperse before excessive leakage occurs. The name of the stored material alone does not describe those operational conditions.[15][12]

Product and system test evidence should correspond to the intended fuel and discharge arrangement. Fleming's discussion of sprinklers explains that special products are approved for particular goals and are not automatically interchangeable. The same distinction prevents a generic suppression claim from replacing relevant application testing.[16]

Water supply quality can affect more than hydraulics. Foam properties can change with contaminants, and small water-mist passages can be affected by blockage. Agent selection therefore includes the condition of the supply and the maintenance needed to preserve it.[18][17]

A system assessment should also record what happens after discharge. Water runoff, powder residue, foam solution and altered enclosure atmospheres create different recovery problems. These consequences do not necessarily outweigh fire control, but they belong to the selection evidence rather than being discovered afterwards.[19][15]

Control, extinction and re-ignition

Control limits the fire's development and protects surrounding fuels. It can be achieved while some burning continues, whereas extinction requires the combustion process to cease. These outcomes should not be exchanged when interpreting a test or describing an installed system.[21]

Suppression can begin before flames disappear. Cooling hot gases reduces their ability to heat other fuels, while surface wetting reduces further pyrolysis. A falling heat-release rate can therefore be a meaningful response even where small flames remain temporarily.[1][22]

Re-ignition is a separate phase of the assessment. Hot fuel, glowing material and a damaged foam blanket can permit combustion to return after the initial agent action ends. Adequate post-discharge coverage or retention is consequently different from initial flame knockdown.[4][15]

A delivery chain branches to fire control, extinction or renewed burning after agent loss.
Flame knockdown is not the whole suppression assessment. Based on Iqbal and Salley (2004), pp. B-43–B-44.

Agent delivery may also alter visibility and access. Powder clouds and space-filling foam can make it harder to locate remaining hot material. Inspection after suppression must account for those conditions rather than assuming that a clear view immediately follows discharge.[19][15]

Performance and limits

Extinguishment is not the same as control. A system can reduce heat release and prevent spread while combustion continues. In other circumstances, cooling adjacent material can prevent ignition even when the initial fuel continues to burn.[2][21]

Visible flame extinction is also not proof that a fire is out. NUREG-1805 describes cable tests in which internal temperatures continued to rise after a gaseous agent removed surface flames. Re-ignition occurred when ventilation restored air. The fuel condition and retention period therefore matter.[4]

Suppression evidence is often empirical. Fleming explains that complex water-suppression mechanisms have not supported a complete general design calculation. Sprinkler criteria consequently draw on full-scale tests and experience rather than a single universal suppression equation.[16]

Laboratory agent concentrations require the same caution. Water-mist experiments can use ideal mixing between spray and flame that is difficult to reproduce at enclosure scale. A measured laboratory concentration cannot by itself determine nozzle spacing or flow in an actual system.[9]

Fine water sprays illustrate why delivery form belongs in the agent description. Mawhinney and Back identify gas-phase cooling, oxygen depletion with vapour dilution, and surface wetting as primary mechanisms. Radiation attenuation and kinetic effects are secondary in their review, with their relative importance changing between applications.[9][22]

The powder family also contains meaningful chemical differences. NUREG-1805 lists sodium and potassium compounds and monoammonium phosphate among dry agents. Their relative test performance depends on particle size as well as chemistry, and only some formulations provide the surface coating associated with deep-seated ordinary-combustible fires.[3][12]

See also

Notes

  1. ↑ 1.0 1.1 1.2 1.3 1.4 1.5 1.6 Iqbal and Salley (2004), p. B-15.
  2. ↑ 2.0 2.1 2.2 2.3 2.4 2.5 Fleming (2002), p. 4-72.
  3. ↑ 3.0 3.1 3.2 3.3 Iqbal and Salley (2004), p. B-55.
  4. ↑ 4.0 4.1 4.2 4.3 Iqbal and Salley (2004), pp. B-43–B-44.
  5. ↑ 5.0 5.1 Scheffey (2002), p. 4-89.
  6. ↑ 6.0 6.1 6.2 Van Rossum (2027), §3.4.
  7. ↑ 7.0 7.1 Van Rossum (2027), §3.5.
  8. ↑ 8.0 8.1 Iqbal and Salley (2004), p. B-41.
  9. ↑ 9.0 9.1 9.2 Mawhinney and Back (2002), pp. 4-313–4-314.
  10. ↑ Van Rossum (2027), §3.6.
  11. ↑ 11.0 11.1 11.2 11.3 11.4 Iqbal and Salley (2004), p. B-16.
  12. ↑ 12.0 12.1 12.2 12.3 12.4 12.5 Iqbal and Salley (2004), p. B-56.
  13. ↑ 13.0 13.1 13.2 Scheffey (2002), p. 4-88.
  14. ↑ 14.0 14.1 Iqbal and Salley (2004), pp. B-57–B-58.
  15. ↑ 15.0 15.1 15.2 15.3 15.4 15.5 15.6 Iqbal and Salley (2004), p. B-60.
  16. ↑ 16.0 16.1 16.2 Fleming (2002), p. 4-73.
  17. ↑ 17.0 17.1 17.2 Mawhinney and Back (2002), p. 4-311.
  18. ↑ 18.0 18.1 Iqbal and Salley (2004), p. B-59.
  19. ↑ 19.0 19.1 19.2 Iqbal and Salley (2004), p. B-57.
  20. ↑ Iqbal and Salley (2004), p. B-43.
  21. ↑ 21.0 21.1 Iqbal and Salley (2004), pp. 10-1–10-2.
  22. ↑ 22.0 22.1 Mawhinney and Back (2002), p. 4-314.

References

  • Fleming, R. P. (2002). Automatic sprinkler system calculations. In P. J. DiNenno (Ed.), SFPE handbook of fire protection engineering (3rd ed., pp. 4-72–4-87). National Fire Protection Association.
  • Iqbal, N., & Salley, M. H. (2004). Fire dynamics tools (FDTs): Quantitative fire hazard analysis methods for the U.S. Nuclear Regulatory Commission fire protection inspection program (NUREG-1805). U.S. Nuclear Regulatory Commission.
  • Mawhinney, J. R., & Back, G. G., III. (2002). Water mist fire suppression systems. In P. J. DiNenno (Ed.), SFPE handbook of fire protection engineering (3rd ed., pp. 4-311–4-337). National Fire Protection Association.
  • Scheffey, J. L. (2002). Foam agents and AFFF system design considerations. In P. J. DiNenno (Ed.), SFPE handbook of fire protection engineering (3rd ed., pp. 4-88–4-122). National Fire Protection Association.
  • Van Rossum, E. (2027). Introduction to Fire Safety Engineering. Fire Safety Academy.