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Fire Dynamics I

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Smouldering along a Horizontal Cellulose Rod ... Flow of hot gas (when smoker draws on cigarette helps. ... conditions are different: hot against pipe, cool ... – PowerPoint PPT presentation

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Title: Fire Dynamics I


1
Fire Dynamics I
  • Lecture 12
  • Smouldering and
  • Spontaneous Combustion
  • Jim Mehaffey
  • 82.575 or CVG7300

2
  • Smouldering and Spontaneous Combustion
  • Outline
  • Smouldering combustion
  • Glowing combustion
  • Spontaneous combustion (ignition) of solids
  • General principles
  • Insulating fibreboard
  • Mathematical models
  • Related phenomenon

3
  • Smouldering Combustion
  • Slow, low-temperature, non-flaming combustion
    sustained by heat evolved when O2 reacts directly
    with surface of a solid
  • Smouldering is a serious fire hazard because
  • it typically generates a substantially higher
    yield of toxic compounds than flaming (though at
    a slower rate)
  • it provides a gateway to flaming that can be
    initiated by heat sources too weak to directly
    produce a flame.

4
  • Smouldering Combustion
  • Characteristics of materials (e.g. cigarettes)
    that experience smouldering
  • solid has a large surface area per unit mass,
    which facilitates surface oxidation
  • solid is permeable, which permits O2 to reach
    reaction site by diffusion and/or convection
  • solid is a good thermal insulator, which reduces
    heat losses and permits sustained combustion
    despite low heat heat release rates
  • solid forms a carbonaceous char when it undergoes
    pyrolysis. Char has a high heat of combustion
    and is susceptible to oxidation at moderate
    temperatures (gt 670 K 400C).

5
  • Smouldering Combustion
  • Rate of propagation of smouldering is controlled
    by supply rate of oxygen
  • Reverse propagation When oxygen diffuses through
    unburnt fuel toward reaction front
  • Example 1D upward smouldering through sawdust
  • Typical rate of upward advance is slow. It has
    been found to take 2 weeks to propagate upwards 1
    m
  • When air is supplied from above, rate of advance
    increases. Yield (mole fraction) of CO is 6 - 7
    for PU and 10 - 22 for cellulose insulation.

6
  • Smouldering Combustion
  • Forward Oxygen flow is in same direction as
    advance of smoulder front
  • Example cigarette during a draw
  • Rate of advance of smouldering still not fast
  • Yield (mole fraction) of CO is 9 for cellulose
    insulation

7
  • Smouldering Combustion
  • Can occur in porous materials which form
    carbonaceous char when heated
  • Examples paper, cellulosic fabrics, sawdust,
    fibreboard, latex rubber and some thermosetting
    foamed plastics
  • Materials which melt and shrink away from a heat
    source do not exhibit smouldering combustion

8
  • Initiation of Smouldering
  • Can follow flaming combustion of cellulosic
    materials if flame is extinguished
  • Can be induced by another smouldering source such
    as a cigarette
  • Radiant or conductive heating in the absence of a
    pilot
  • Self-heating leading to spontaneous combustion

9
  • Smouldering along a Horizontal Cellulose Rod

10
  • Smouldering along a Horizontal Cellulose Rod
  • Zone 1 Pyrolysis zone in which there is a steep
    temp rise and an outflow of visible airborne
    products.
  • Zone 2 A charred zone where temp is maximum,
    evolution of visible products stops and glowing
    occurs.
  • Zone 3 A zone of porous residual char and/or ash
    which no longer glows and whose temp falls slowly.

11
  • Smouldering along a Horizontal Cellulose Rod
  • Heat is released in Zone 2 where surface
    oxidation of char occurs and temps are 600 -
    750C. Heat of combustion of char is high.
    Oxygen reaches Zone 2 because of permeability of
    specimen.
  • Heat is conducted from Zone 2 into Zone 1 causing
    thermal decomposition of fuel to produce
    volatiles and carbonaceous char. Flow of hot gas
    (when smoker draws on cigarette helps. Temp must
    be above 250-300C for this to take place.
  • Rate of propagation of smouldering front depends
    on rate of penetration of O2 to surface of
    reacting char (heat release rate) and rate of
    heat loss

12
  • Smouldering along a Horizontal Cellulose Rod
  • Smoke Non-oxidized volatile products of
    pyrolysis.
  • Smoke includes gaseous products, but also high
    boiling point liquids and tars which condense to
    form an aerosol.
  • Smoke is combustible and, in principle, can give
    rise to a flammable atmosphere.
  • Smoke may also be quite toxic.
  • Smoke produced in smouldering is quite different
    from that produced in combustion.

13
  • Glowing Combustion
  • Surface oxidation of carboneous materials or char
  • No thermal degradation of parent fuel
  • Examples
  • activated charcoal
  • char after flaming has ceased

14
  • Spontaneous Combustion within Solids
  • Some combustible solids can ignite as a result of
    internal heating if an exothermic process
    liberates heat faster than it can be dissipated
  • This can occur only if the material
  • is sufficiently porous to allow air (O2) to
    permeate it
  • yields a rigid char as result of thermal
    decomposition
  • Smouldering (oxidation of char) begins inside the
    material and slowly propagates radially outward
  • Phenomenon is normally associated with relatively
    large mass of material (small surface to volume
    ratio)

15
  • Spontaneous Combustion within Solids
  • Heat generated by some exothermic process
  • surface oxidation interstices of porous
    materials
  • micro-biological activity
  • If rate of heat release gt rate of heat loss,
    material undergoes self-heating and may ignite
    (smouldering)
  • O2 must diffuse into material, so time to
    ignition (if it occurs) can be very long
  • However, spontaneous combustion (ignition) may
    occur at low ambient temperatures

16
  • Spontaneous Combustion within Solids
  • Smouldering (oxidation of char) begins inside the
    material and slowly propagates radially outward
  • May cause flaming when it reaches the surface

17
  • Case Study Insulating Fibreboard (3)
  • Forintek Royal Sun Alliance Insurance Company
  • Several fires occurred during transport of
    insulating fibreboard panels from a plant in the
    prairies to retailers in southern Ontario
  • Suspected insulating fibreboard panels
    experienced self-heating and spontaneous
    combustion
  • Forintek asked to investigate

18
  • Insulating Fibreboard Panels
  • Thickness 12.7 mm
  • Density 230 kg m-3
  • Insulating fibreboard is known to be subject to
    self-heating spontaneous combustion because
  • It is rather porous so O2 can permeate it
  • It is a good insulator so heat is trapped within
    it

19
  • Test for Self-heating Spontaneous Combustion
  • Drying oven stabilized at some temperature.
  • Cube of insulating fibreboard placed in oven
  • Three thermocouples placed in cube
  • at geometric centre
  • above centre
  • below centre
  • Observe thermal performance of cube
  • does cube experience self-heating whereby centre
    temperature exceeds oven temperature, and
  • does cube experience spontaneous combustion
    smouldering starts in centre progresses
    outwards

20
  • 190 mm Cube _at_ 145C

21
  • 190 mm Cube _at_ 155C

22
  • 190 mm Cube _at_ 150C

23
  • Summary of Findings Insulating Fibreboard (2)

24
  • Photograph of inside of Cube after Testing

25
  • The Frank-Kamenetskii Model
  • A thermal explosion theory developed to explain
    auto-ignition in vapour / air mixtures
  • Assumptions
  • Rate of heat generation / volume Hc ? A exp(- E
    / RT)
  • Heat is transferred through specimen by
    conduction, and this is a slow process
  • Heat transfer at surface to surroundings
    (convection radiation) is high, so that surface
    temp ambient temp
  • Physical properties are independent of
    temperature

26
  • The Frank-Kamenetskii Model
  • Provides a relationship between
  • Ta,cr critical ambient temperature for ignition
    (K)
  • ro dimension of sample (m). (Side of a cube
    2 ro)
  • ?cr critical parameter dictated by geometry of
    sample
  • ln?cr Ta,cr2 / ro2 C1 - C2 / Ta,cr
    Eqn (14-1)
  • C1 lnE Hc A ? / (k R)
  • C2 E / R

27
  • The Frank-Kamenetskii Parameter
  • For large cubes, assumption that surface temp
    ambient temp is reasonable and ?cr 2.52
  • For small cubes, the assumption breaks down and a
    correction factor must be applied
  • For 75 mm cube ?cr 1.97
  • For 190 mm cube ?cr 2.34
  • For 305 mm cube ?cr 2.52

28
  • The Frank-Kamenetskii Model
  • Using the structure of Eqn (14-1) as a guide,
    critical ambient data for the 75, 190 and 305 mm
    cubes were plotted on next slide as 1000 / Ta,cr
    vs ln?cr Ta,cr2 / ro2
  • The resultant plot is nearly linear and a
    regression analysis provided the equation
  • 3.662 - 0.07333 ln?cr Ta,cr2 / ro2
    1000 / Ta,cr

29
  • Correlation of Ignition Data
  • ln?cr Ta,cr2 / ro2

30
  • Summary of Findings Insulating Fibreboard (2)

31
  • Insulating Fibreboard Panels
  • An ambient temp of 104ºC is required for a pallet
    (1.22 m cube) of insulating fibreboard to
    experience spontaneous combustion
  • An ambient temp of 89ºC is required for a tractor
    trailer full of insulating fibreboard (2.44 m
    cube) to experience spontaneous combustion
  • Typical ambient temperatures found in a tractor
    trailer or railcar are clearly not sufficient to
    cause spontaneous combustion.
  • So how did spontaneous combustion occur?

32
  • Absorption of Water Vapour by Fibreboard
  • Wood and cellulosic fibres are hygroscopic
  • Absorption of water vapour by wood products is
    known to be an exothermic process.
  • Could this exothermicity play a role?
  • In the summer, it is much more humid in southern
    Ontario than in the prairies.
  • An experiment was devised to investigate this
    possibility.

33
  • Effect of Absorption of Water Vapour

34
  • Experiment Absorption of Water Vapour by
    Fibreboard
  • Measure moisture content of 75 mm and 305 mm
    cubes. Found to be 5.7
  • Dry 75 mm and 305 mm cubes in chamber at 50C and
    low relative humidity for 28 hours. Moisture
    content of 75 mm cube dropped to 1.5.
  • 305 mm cube allowed to cool overnight in chamber
    at 20C and RH lt 2.
  • Next morning, ambient conditions in chamber
    changed to 30C and RH 76. Evidence of
    self-heating due to absorption of water vapour
  • Following morning, ambient conditions in chamber
    were changed to 32C and RH 99. Again
    evidence of self-heating due to absorption of
    water vapour
  • Measure moisture content of 305 mm cube. MC
    6.9

35
  • Absorption of Water Vapour by Fibreboard
  • When stored at 32C and RH 95, moisture
    content of fibreboard can be 23-24
  • In summer in closed tractor trailer, may be 65C
    and RH 95. Moisture content of fibreboard
    very high
  • Sweden If fibreboard at 20C and RH 70 with
    M.C. 10 suddenly absorbs enough water vapour
    so M.C. increases by 4.5, temp of board may
    increase to 100C under adiabatic conditions
  • Board manufactured in prairies often has M.C.
    1-2
  • Potential for problems

36
  • Absorption of Water Vapour by Fibreboard
  • Fibreboard manufactured in prairies with M.C.
    1-2 shipped to Ontario where temp RH are much
    higher can absorb enough water vapour to drive
    temp in load of fibreboard in an enclosed vehicle
    to over 100C
  • This is hot enough so that oxidation within the
    load will commence and spontaneous combustion may
    occur
  • Prevention Remoisten board with liquid water
    after production. Energetics not so unfavourable

37
  • Spontaneous Combustion
  • of Animal Feedstuff (4)
  • Animal feedstuff processed byproduct from
    distillery

38
  • Spontaneous Combustion
  • of Skimmed Milk Powder (4)

39
  • Spontaneous Combustion
  • Yeast-Based Powder (4)

40
  • Time to Ignition Chemically active carbon (1)
  • Problems with cargo of active carbon (4-14
    tonnes) in holds of ships passing through tropics
    (38C)
  • Time to ignition appeared to be very long

41
  • Time to Ignition Chemically active carbon (1)
  • Times associated with observations slightly less
    than extrapolation from small-scale data

42
  • Related Phenomena
  • Linseed oil on cotton rags. Oil dispersed on
    rigid porous structure. Large surface area on
    which oxidation occurs but heat is not quickly
    dissipated.
  • In chemical plants where thermal insulation, or
    lagging, is applied to pipes carrying hot process
    fluids. Leakage from faulty flange into lagging
    can lead to a lagging fire. Boundary
    conditions are different hot against pipe, cool
    against air

43
  • Spontaneous Combustion in Haystacks
  • Stage 1 If hay is very wet (63-92 by weight
    water), micro-biological activity (bacteria) can
    raise temp to 70C
  • Stage 2 Chemical oxidation causes self heating.
    Water may be a catalysis for such low temp
    oxidation.
  • Stage 3 Ignition
  • At typical ambient temperatures, critical size
    for cubical haystack is 2ro 2 m
  • Bales of hay do not experience spontaneous
    ignition however, haystacks do

44
  • References
  • 1. D. Drysdale, An Introduction to Fire Dynamics,
    Chapter 8.
  • 2. T.J. Ohlemiller, Smoldering Combustion,
    Section 2 / Chapter 11, SFPE Handbook, 2nd Ed.
    (1995)
  • 3. J.R Mehaffey, L.R. Richardson, M. Batista and
    S. Gueorguiev, Self-heating and spontaneous
    ignition of fibreboard insulating panels, Fire
    Technology Vol 36, 226-235 (2000)
  • 4. P.F. Beever, Self-heating and spontaneous
    combustion, Section 2 / Chapter 12, SFPE
    Handbook, 2nd Ed. (1995)
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