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Contents
  1. 1Flames, sparks and hot surfaces
  2. 2Ignition energy and flammable atmospheres
  3. 3Self-heating as an internal source
  4. 4Source and target interaction
  5. 5Fire statistics and frequency analysis
  6. 6Hazardous areas and prevention
  7. 7Fire investigation
  8. 8Calculating electrical source energy
  9. 9See also
  10. 10Notes
  11. 11References

An ignition source supplies energy capable of initiating combustion when it reaches a suitable fuel-oxidiser system. Flames, sparks, heated wires, incandescent particles and hot surfaces can act as sources. Chemical self-heating can also create an initiating condition inside a material. Effectiveness depends on the fuel, mixing, exposure and heat losses at the point of interaction.[1][2]

The source is only one part of Ignition. A flammable mixture and suitable thermal conditions must also be present. A source that is too small or loses energy too quickly can fail, while a modest flame or spark can initiate a much larger fire when the surrounding mixture is favourable.[3][4]

Ignition sources can also occur in sequence. NUREG-1805 describes a burning wastebasket becoming a source for a chair, after which the chair can ignite other fuel. The initial device and subsequent burning objects therefore play different roles in the developing fire. Every later burning object must be assessed both as a target and as a potential new source.[5]

Wastebasket ignites a chair and the chair becomes a source for another object.
Burning objects can become later ignition sources. Based on Iqbal and Salley (2004), p. F-37.

Flames, sparks and hot surfaces

A small pilot flame initiates a reaction in an already suitable fuel-air mixture. Its role is not necessarily to heat the whole fuel body or generate all the pyrolysis gases. Once the reaction begins, it can propagate away from the pilot through the connected mixture.[1]

Sparks and heated filaments can perform a similar pilot function. Their effect depends on energy, size, exposure time and the thermal and chemical properties of the mixture. Heat loss to surrounding gas and surfaces can quench the initial reaction before propagation develops.[3]

Hot surfaces create a different exposure because they can heat a fuel continuously. Surface temperature alone does not determine ignition: contact area, airflow, fuel thickness and exposure duration affect the energy balance. A small hot object can therefore produce a different outcome from a large surface at the same nominal temperature.[6]

Open flames introduce both a pilot and a heat source for further fuel production. They can ignite a gas mixture rapidly or heat liquids and solids until vapour and pyrolysis products become involved. These distinct roles should be identified when reconstructing a fire scenario.[1][7]

Electrical faults can produce local overheating or arcing. In one NUREG-1805 case, improperly grounded equipment caused fault current to overheat conductors and ignite material in two locations. This nuclear-plant incident illustrates a specific electrical sequence, not a universal frequency for cable ignition.[8]

Hot work includes activities using heat, sparks or open flame, such as cutting, welding and grinding. These activities can introduce an ignition source into areas where it is not normally present. Fuel arrangement and work procedures therefore form part of the source assessment.[5][9]

Oxygen-acetylene torches provide a particularly intense source. NUREG-1805 gives a hottest-flame value of approximately 3,500 °C for the torch conditions described. That value concerns the flame itself and does not equal the temperature reached by every target or the energy required for ignition.[10]

The Electric Power Research Institute (EPRI) and U.S. Nuclear Regulatory Commission (NRC) address welding and cutting in their 2005 nuclear fire-analysis methodology. They link frequency with maintenance activity, hot-work procedures and housekeeping. It treats these as plant-specific influences rather than fixed properties of a compartment. Similar reasoning applies to temporary work in other settings, although the numerical bins are specific to the nuclear method.[9]

A continuous fire watch can shorten detection time when hot work ignites fuel. The same guidance states that such fires are likely to be detected quickly when a watch has been posted. This is a response measure, not proof that ignition has been prevented.[11]

Ignition energy and flammable atmospheres

Minimum ignition energy is the lowest energy associated with ignition of a specified fuel-oxidiser mixture under stated conditions. It is relevant when a spark or other short-duration source contacts a flammable atmosphere. Mixture composition, temperature and the nature of the discharge affect the requirement.[3][12]

The 2005 International Fire Engineering Guidelines note that fuel-air mixtures within the flammable region can often be ignited by sources of only millijoules. The actual value depends on the mixture and test method. A small electrical or static source can therefore be significant even without a large hot surface.[13]

Flammability limits remain essential when interpreting this energy. Outside the propagating range, a source can create local combustion without a flame travelling through the wider mixture. Beyler distinguishes this local effect from sustained flame propagation within the limits.[14]

Prevention commonly keeps gas or vapour concentrations well below the lower flammable limit. The guidelines caution against relying on a mixture above the upper limit because subsequent dilution can return it to the flammable region. Ignition-source control works together with concentration control rather than replacing it.[13]

Self-heating as an internal source

Self-heating occurs when chemical reactions inside a material generate energy faster than it can be lost. The material then supplies part of the initiating heat itself. Poor thermal conductivity and insulating containers can help retain this energy.[2]

The critical condition depends on material chemistry, ambient temperature, size and shape. Larger bodies can favour runaway because heat is retained more effectively, while higher ambient temperature reduces the relative thermal driving force for cooling. No single external ignition device is required in these cases.[2][15]

Heat generated inside a body exceeds losses and produces internal runaway.
Self-heating can create an internal ignition source. Based on Gray (2002), pp. 2-211–2-212.

Preheated products add another variable. Hot laundry, recently manufactured chipboard and hot porous food products require attention to the material's own stacking temperature as well as ambient conditions. Gray explains that time to ignition can be much shorter for preheated bodies than for material stacked at ambient temperature.[2][16]

Spontaneous runaway often begins at the centre of a low-conductivity body. Charring or ash can therefore be found inside while the exterior appears less affected. This evidence can inform investigation, but it must be assessed alongside other possible ignition sources and preheating.[15]

Source and target interaction

The target is the fuel exposed to the source. Its physical and chemical properties determine how it responds, including conductivity, heat capacity, decomposition behaviour and geometry. A source-target description should retain these properties rather than treating ignition as a property of the source alone.[17]

Source heating a target while vapour, oxygen and heat losses shape ignition.
Ignition depends on source-target interaction and heat loss. Based on Kanury (2002), pp. 2-230–2-232.

For a solid, incoming energy is partitioned into internal conduction, reradiation and convection to adjacent gas. Moisture evaporation and pyrolysis then modify the response. The source can be steady in the model while the net heating of the target changes substantially over time.[3]

Mixing has a dual effect. It is necessary to bring fuel vapour and oxygen together, but it can also cool and dilute the mixture. Spontaneous ignition needs both suitable composition and sufficient thermal condition at the same location. More airflow is therefore not always more favourable.[3]

For piloted ignition, the pilot can be small relative to the target because it only initiates the reaction. It still cannot be infinitely small: reaction can be quenched if the source region does not exceed the mixture's critical dimensions and energy requirements. The relevant threshold belongs to the whole mixture-source arrangement.[3]

Source position can also change the fire that follows ignition. NUREG-1805 contrasts a pilot at the bottom of a curtain with the same pilot at the top. The first arrangement favours rapid upward flame spread, while the second produces slower downward spread. Source identification therefore includes its location relative to the fuel, as well as the device or energy type.[18]

Fire statistics and frequency analysis

Fire statistics can show which sources and first-ignited materials occur in reported incidents. Such evidence helps prioritise prevention and estimate ignition frequencies. It does not by itself establish the cause of an individual fire or the probability of ignition during one particular exposure.[4][9]

Nuclear fire probabilistic risk analysis uses detailed ignition-source counts and weighting factors. The method considers equipment, maintenance, occupancy and storage when assigning compartment-specific influences. These categories belong to US nuclear power plant analysis and should not be presented as universal building values.[9]

The 2005 guidance recommends work-order counts and staff information to assess maintenance-related transient fires. It separately addresses welding and cutting, including procedures that prohibit these activities during power operation. This demonstrates how administrative controls can alter the frequency assigned to a source scenario.[19]

Data quality remains important. The 2005 guidelines note that ignition statistics can support quantitative frequency studies and qualitative comparisons, but general prediction of ignition potential remained uncertain. Source identification and statistical frequency answer different questions.[4]

Hazardous areas and prevention

For Hazardous area classification, the source inventory has to be related to the potential presence of a flammable atmosphere. The IFEG gas and vapour discussion identifies mixture concentration as a separate part of ignition prevention. Removing one possible source does not establish that the atmosphere is outside its flammable range.[13]

Prevention can address an activity, the flammable atmosphere or the separation of fuel from energy. Detection and response act on a fire after ignition. The suitable combination depends on whether the source is permanent equipment, a temporary task or an internal reaction. One generic prohibition cannot cover all these mechanisms.[4][9]

Hot-work procedures provide a temporary-source example. Housekeeping addresses available fuel, work controls address source generation and a posted fire watch can shorten detection time. Evaluating only the torch or spark would miss the wider scenario that determines whether a small ignition becomes a damaging fire.[9][11]

For self-heating storage, source prevention can involve size, stacking temperature and heat dissipation rather than electrical exclusion. The source is distributed within the fuel body, so separating it from the fuel is not a meaningful description. Geometry and storage conditions become the principal controls.[2]

Fire investigation

Fire investigation seeks to establish the sequence and conditions of ignition from evidence. Potential sources are evaluated together with target materials, heat transfer and subsequent fire development. Finding a device capable of ignition is not alone proof that it initiated the event.[17][15]

Electrical evidence can include fault paths and conductor damage. The Palo Verde incident in NUREG-1805 linked simultaneous fires to a common overheated conductor caused by grounding faults. The value of that example lies in tracing the complete sequence rather than assigning every cable fire to an electrical fault without evidence.[8]

Self-heating evidence can include deep central charring and a comparatively intact exterior. Gray nevertheless stresses the need to consider solar exposure, recent processing and other preheating. Unknown cause can also be more common in large destructive fires because evidence is lost.[2][15]

A reliable investigation distinguishes initial ignition from later sources. A burning object found at one location may have started the fire there or may itself have been ignited by an earlier object. Reconstructing this order prevents the first discovered burning item from being misidentified as the original igniter.[5]

Calculating electrical source energy

A theoretical energy calculation is useful when the source is a simple electrical discharge. It describes the energy associated with the circuit, which can be compared with ignition-test evidence for a specified mixture. The discharge type must match the test. Zalosh distinguishes capacitive electrostatic discharges from inductive sparks because their duration and ignition effectiveness differ.[12]

For a purely capacitive discharge, energy depends on capacitance and the square of the voltage before discharge. Capacitance describes how much electrical charge a body stores for a given voltage. The equation is an idealised electrical relation, rather than a complete calculation of heat deposited in a particular fuel mixture.[12]

E=12CV2

Symbol Description Unit
E Theoretical energy of the capacitive discharge J
C Electrical capacitance F
V Voltage before discharge V

Zalosh's worked example considers an elevated powder silo with a capacitance of 500 pF. The example powder has an ignition energy of 10 mJ for inductive sparks and 50 mJ for capacitive sparks. The capacitive comparison therefore uses 50 mJ. These are the supplied example's values, not general properties of pharmaceutical powders or storage silos.[12]

Rearranging the energy equation gives the voltage associated with that capacitive ignition energy. Converting picofarads to farads and millijoules to joules gives approximately 14 kV. The calculation retains the unrounded value until the final result. Its meaning is a threshold comparison for the idealised source and specified powder in the example.[12]

V=2EC=2(50×10−3)500×10−12=14142…V≈14kV

Using the inductive value in this capacitive calculation would compare unlike discharge conditions. Zalosh explains that longer-duration sparks can ignite a dust cloud at lower energy than a short capacitive discharge. Dust concentration and mixture temperature also influence the measured threshold. The numerical energy alone therefore does not fully characterise the source's ignition capability.[12]

The same equation does not quantify ignition by frictional sparks, glowing particles or hot surfaces. Their heating histories and contact mechanisms differ from a purely capacitive discharge. Zalosh notes that evaluating mechanical friction and impact sparks is more difficult. Kanury's source-target description likewise requires the thermal and chemical conditions at the actual interaction.[12][3]

See also

Notes

  1. ↑ 1.0 1.1 1.2 Kanury (2002), p. 2-230.
  2. ↑ 2.0 2.1 2.2 2.3 2.4 2.5 Gray (2002), p. 2-211.
  3. ↑ 3.0 3.1 3.2 3.3 3.4 3.5 3.6 Kanury (2002), p. 2-232.
  4. ↑ 4.0 4.1 4.2 4.3 Australian Building Codes Board et al. (2005), p. 2.4-4.
  5. ↑ 5.0 5.1 5.2 Iqbal and Salley (2004), p. F-37.
  6. ↑ Kanury (2002), pp. 2-231–2-232.
  7. ↑ Van Rossum (2027), §4.1.
  8. ↑ 8.0 8.1 Iqbal and Salley (2004), pp. H-24–H-25.
  9. ↑ 9.0 9.1 9.2 9.3 9.4 9.5 EPRI and NRC (2005), p. 6-21.
  10. ↑ Iqbal and Salley (2004), p. 3-9.
  11. ↑ 11.0 11.1 EPRI and NRC (2005), p. 11-28.
  12. ↑ 12.0 12.1 12.2 12.3 12.4 12.5 12.6 Zalosh (2002), p. 3-405.
  13. ↑ 13.0 13.1 13.2 Australian Building Codes Board et al. (2005), p. 3.3-2.
  14. ↑ Beyler (2002), pp. 2-172–2-173.
  15. ↑ 15.0 15.1 15.2 15.3 Gray (2002), p. 2-212.
  16. ↑ Gray (2002), p. 2-213.
  17. ↑ 17.0 17.1 Kanury (2002), p. 2-229.
  18. ↑ Iqbal and Salley (2004), p. 6-3.
  19. ↑ EPRI and NRC (2005), p. 6-22.

References

  • Australian Building Codes Board, National Research Council of Canada, International Code Council, & Department of Building and Housing New Zealand. (2005). International fire engineering guidelines (2005 ed.). Australian Building Codes Board.
  • Beyler, C. L. (2002). Flammability limits of premixed and diffusion flames. In P. J. DiNenno (Ed.), SFPE handbook of fire protection engineering (3rd ed., pp. 2-172–2-187). National Fire Protection Association.
  • Electric Power Research Institute, & U.S. Nuclear Regulatory Commission. (2005). EPRI/NRC-RES fire PRA methodology for nuclear power facilities: Volume 2: Detailed methodology (EPRI 1011989; NUREG/CR-6850).
  • Gray, B. (2002). Spontaneous combustion and self-heating. In P. J. DiNenno (Ed.), SFPE handbook of fire protection engineering (3rd ed., pp. 2-211–2-228). 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.
  • Kanury, A. M. (2002). Flaming ignition of solid fuels. In P. J. DiNenno (Ed.), SFPE handbook of fire protection engineering (3rd ed., pp. 2-229–2-245). National Fire Protection Association.
  • Van Rossum, E. (2027). Introduction to Fire Safety Engineering. Fire Safety Academy.
  • Zalosh, R. (2002). Explosion protection. In P. J. DiNenno (Ed.), SFPE handbook of fire protection engineering (3rd ed., pp. 3-402–3-421). National Fire Protection Association.
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