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Why
do industrial flames look the way they do? If
burner designs are symmetrical, then why do the
flames have such irregular shapes? We know that
the answer is of course that burners are fired
within a furnace, and the geometry of this enclosure
will have a great influence on the resulting
flowfield developing inside it. Obviously the
character of the flowfield will influence flame
shape, but how strong this influence will be
is always difficult to assess a priori. Most
operational problems can be corrected by adjustments
to the burners in the field, but the trade-off
is often a loss of efficiency and/or increased
pollutant formation.
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This
article aims to show how flame shape can be significantly
affected by internal furnace aerodynamics. To illustrate
this point we have chosen a study that was carried
out using 125-MMBTU/hour NATCOM Low-NOx Hyper-Mix
burners (figure1) fired in two 100,000-lbs/hour
D-Type boilers. These D-Type boilers are mirror
images of each other (figures 2a and 2b), but both
burners are identical. The burner (figure 1) has
a central low-velocity pilot gas injector, which
is surrounded by a central air-core. The central
air-core is itself surrounded by a variable-pitch
blade air-swirler. Natural gas is injected through
8 high velocity gas spuds located around the swirler
within the annular section of the axial-air by-pass.
Four of the gas spuds are axial injectors surrounded
by Hyper-Mix steam injectors and recirculated flue
gas injectors (FGR). The other four spuds are fired
at an angle in order to induce a counter-swirling
motion of the gas.
Figures 2a and 2b show the
flame shapes resulting from firing the burner
in each of the two D-Type boilers. For two such
boiler geometries that are mirror images of each
other, one would also expect the flames to be
mirror images. But this isn’t the case
because the burners are identical rather than
mirror images of each other; in fact both burners
induce a clockwise swirling motion of the air
and a counter-clockwise swirling motion of the
gas. The resulting flames have irregular shapes
with parts of the flame coming close to the tube-bank
walls. If the burners had been fired in a free
quiescent atmosphere, the flames would have been
symmetrical about the burners’ centerline.
Furthermore, if the burners had been fired within
a symmetrical enclosure (ex. cylindrical furnace),
the flames would still have been symmetrical
although shaped a little differently. When fired
within enclosures with irregular geometries however,
the developing internal recirculation patterns
become warped and contribute to distort the flame
envelope. Figure 3 shows the vector field representing
the flow patterns responsible for distorting
the flame of figure 2a. The vectors colored in
red show the envelope of the luminous flame,
which is being stretched out towards the left
wall by secondary currents that are not part
of the central clockwise swirling motion of the
flow leaving the burner.
Fig
3: UV - Velocity vectors at z=2.5m
Figs 4:
Luminous flame contour- optimized burner
configuration
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A luminous flame contour represents
the part of the flame emitting light that is
visible to the naked eye. This luminosity of
the flame is mostly due to unburned carbon particles
that have been heated to the point at which they
become incandescent. Natural gas flames, however,
emit very little light in the visible spectrum
(the flames are light blue), when burning in
fuel-lean to stoichiometric proportions and so
the absence of a visible contour does not imply
the absence of a flame. In fact, the highest
flame temperatures are reached for near-stoichiometric
mixtures and so it is also useful to examine
temperature profiles in order to ensure that
no hot spots exist on the furnace walls. The
temperature contours of figure 7 show that the
optimized flame is indeed well centered and does
not impinge on any of the furnace walls.
In summary, CFD methods,
applied using STAR-CD, have allowed us to observe
and quantify the details of industrial combustion
phenomena that are almost impossible to measure.
We have shown how CFD tools can enable us to
better understand the underlying physics and
so develop more efficient combustion technology.
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Fig
1: Burner geometry

Figs 2a and 2b: Luminous flame
contour - 2a standard configuration - 2b mirror image configuration
While it would be extremely difficult
to control these secondary recirculation patterns, CFD does
allow us to perform an in-depth analysis of the flowfield
and of the factors affecting it. The STAR-CD simulations
enable us to determine what is causing the flame to become
distorted. It is thus possible to identify which spuds are
responsible for the fuel burning close to the left wall and
to identify which modifications to the burner’s standard
configuration will eliminate or reduce the distortion. Figure
4 shows the luminous flame contour for the optimized burner
configuration where the injection angle of some of the high-velocity
gas spuds has been changed by rotating the pipes. This flame,
although it still has a non-symmetrical profile, is now well
contained in the center of the furnace. Another view of the
luminous flame contour for the optimized burner configuration
is shown in figure 5.
Figure 6 gives us an idea of the complexity of the flowfield inside the
furnace. A strong swirling flow can be seen developing in an annular pattern
in the center of the furnace. Recirculation patterns are present close
to the floor and roof of the furnace, while no recirculation patterns can
be seen developing in the horizontal plane at the elevation of the burner’s
centerline. Had the enclosure been cylindrical, the recirculation pattern
would have been toroidally shaped thus surrounding the flame. The shape
of a flame developing in a non-symmetrical enclosure is clearly strongly
influenced by the shear forces created by the non-symmetrical recirculation
patterns surrounding it

Fig 5: Luminous flame contour- optimized
burner configuration

Fig 6: Velocity vector field
- optimized burner configuration

Fig 7: Temperature Contours
- optimized burner configuration |
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