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    Calculates locally in your browser · soot and ash radiation
    Heat transfer / combustion

    Radiation from a sooty flame

    A clean flue gas radiates only in the CO₂ and H₂O bands. A flame with soot radiates continuously across the whole spectrum, and a pulverised-coal flame adds ash particles on top. Both are grey emitters that add to the band absorption rather than replacing it, so the coefficients are added and one exponential is taken.

    LuminousYesFlux gain78%k total0.8 /m
    Total emissivity
    0.810
    gas alone 0.46
    Heat flux
    163.8 kW/m²
    92.1 kW/m² without particulates
    Soot absorption
    0.5 /m
    62% of the total
    Ash absorption
    0.01 /m
    particulate loading
    Three contributions to one coefficient
    Soot and ash are grey emitters, so their absorption adds to the band absorption and the whole thing goes through one exponential.
    0.81
    Three contributions to one coefficient
    TermValueNote
    Gas temperature1200 °C1473 K
    Mean beam length2.00 mas entered
    CO₂ + H₂O partial pressure0.250 atmflue gas is 0.2–0.3
    Gas emissivity (WSGG)0.461bands only
    Gas absorption coefficient0.309 /mbacked out of the emissivity
    Soot volume fraction0.20 ppmk = 3.6 f_v / λ, λ = 1.4 μm
    Soot coefficient0.51 /mcontinuous spectrum
    Ash loading0.10 g/m³d_p 10.0 μm
    Ash coefficient0.008 /m1.5 c / (ρ d)
    Total coefficient0.83 /msum of the three
    Emissivity0.8101 − e^(−kL)
    Flux163.77 kW/m²Hottel form

    Soot and ash raise the emissivity from 0.46 to 0.81, a 78% increase in flux. Soot dominates: 62% of the absorption.

    Inspect the model
    Choose a quick result view, a scaled comparison, or the complete diagnostic set.
    Emissivity against soot loading
    Saturates quickly: a little soot makes the flame nearly opaque, and beyond that more soot changes nothing.
    Emissivity against soot loading0.0000.2240.4480.6720.8961.120 ppm0 ppm0.5 ppm0.5 ppm1 ppm1 ppm2 ppm2 ppm4 ppm4 ppmε
    Flux with and without particulates
    A luminous flame can deliver half again the heat of a clean one at the same temperature.
    Flux with and without particulates0.00038.6577.30115.95154.60193.2492.12Clean gasClean gas163.77With sootWith sootkW/m²
    Canonical equations
    The exact relationships implemented by this engine.

    k_s = 3.6 f_v / λ · λ ≈ 1.4 μm.

    k_a = 1.5 c / (ρ_p d_p) · Mass concentration.

    k = k_gas + k_s + k_a · Coefficients add.

    ε = 1 − e^(−kL) · One exponential for all three.

    engineering methodology

    A clear path from inputs to results.

    A clean flue gas radiates only in the CO₂ and H₂O bands. A flame with soot radiates continuously across the whole spectrum, and a pulverised-coal flame adds ash particles on top.

    Step-by-step methodWorked exampleAssumptions explained

    How to use

    1. Enter the gas and wall temperatures and the beam length.
    2. Set the soot volume fraction and the ash loading.
    3. Add the ash particle diameter.
    4. Read the total emissivity and the flux against the clean-gas case.

    The formula

    ε=1−e−(kgas+ksoot+kash)L\varepsilon = 1 - e^{-(k_{gas} + k_{soot} + k_{ash})L}

    Reference: Soot k = 3.6 f_v/λ (Beér); ash k = 1.5 c/(ρ d); gas from the WSGG model.

    Worked example

    A gas with 1 ppm of soot

    Inputs
    • 1,200 °C gas, 2 m beam, 25% CO₂ + H₂O.
    • 1 ppm soot, 0.1 g/m³ ash at 10 μm.
    Calculation path
    1. 1

      The clean-gas emissivity is 0.46, which corresponds to an absorption coefficient of 0.31 /m.

    2. 2

      Soot at 1 ppm gives 3.6 × 10⁻⁶/1.4 × 10⁻⁶ = 2.57 /m — eight times the gas.

    3. 3

      Ash adds only 0.008 /m, because the particles are large and the loading is low.

    4. 4

      The total coefficient is 2.89 /m, so the emissivity is 1 − e^(−5.77) = 0.997.

    5. 5

      The flux rises from 91 to 196 kW/m² — the flame is effectively opaque.

    Result

    ε 0.997 · 196 kW/m² · soot dominates.

    Interpreting the result

    A little soot goes a long way. One part per million of soot volume already makes the flame nearly opaque, which is why a luminous flame transfers far more heat than a clean gas flame at the same temperature — and why soot is both a heat-transfer asset in a furnace and a pollutant in a chimney.

    Assumptions & limitations

    • Rayleigh-limit soot absorption at a mean wavelength of 1.4 μm.
    • Geometric-optics ash absorption with spherical particles.
    • Gas contribution from the three-term WSGG model.
    • No scattering, and a uniform particle concentration.

    Frequently asked questions

    Why add coefficients rather than emissivities?

    Because absorption is additive and emissivity is not. Converting the gas to a coefficient, adding the particulates, and taking one exponential is the only combination that behaves correctly at both limits.

    Does ash matter as much?

    Rarely in a gas flame, but it does in pulverised coal, where the loading is much higher. The particles are large, so they absorb less per unit mass than soot.

    What about scattering?

    Soot scatters little at these wavelengths, but ash can. A scattering correction needs the albedo, which is beyond a hand calculation.

    What soot loading is realistic?

    0.1 to 5 ppm by volume in a luminous hydrocarbon flame. Above about 5 ppm the flame is opaque and more soot only changes the colour.

    Does this replace the clean-gas page?

    No — it extends it. With the soot and ash set to zero it reduces exactly to the WSGG result.

    Methodology last reviewed 2026-10-22. Results are informational and not financial or engineering advice — see our disclaimer.