Environmental Engineering Reference
In-Depth Information
initially on the left side only, spread all around the base of the
flame. This was
accompanied with subsequent reduction in the yellowish component and an
increase in the bluish component of the
fl
fl
ame. The
fl
flame height also kept on
reducing slightly. Another characteristic feature of the
fl
flame noticed was that of the
fl
flame being present more on one side of the burner than the other, due to swirling.
This is because the swirl is directional, and it makes the air to move in a particular
direction (anticlockwise), and hence the
fl
flame also has some of these directional
characteristics.
Figure 6 represents the variation of temperatures normalized with the tempera-
ture of the corresponding diffusion
ame. It can be observed that the temperature
decreases only slightly initially as the premixing air is introduced and increased.
After that there is a steep reduction in temperature. The temperature rises from
Φ p = 3.32, till
fl
Φ p = 2.77, then reduces slightly at
Φ p = 2.38, and then again rises to
a higher temperature at
Φ p = 1.85. With further addition of premixing air, the
temperature falls to its minimum at
Φ p = 1.11. The data presented in Fig. 6 show
that the temperature for partially premixed
flame is lesser than the temperature
observed for the corresponding pure diffusion
fl
flames. This can be attributed to
cooling due to premixing air addition and counters the premise of improvement in
combustion in the presence of increased premixing air. At higher primary air
fl
fl
ow
Φ p), the swirling ef
rates (lower
ciency of air increases causing better and thorough
mixing of fuel and air resulting in an increase in temperature rather than just
increasing the air velocity and causing cooling effect.
Figures 7 and 8 present the variation in CO and UHC concentrations with
premixing equivalence ratio. It shows that CO and UHC concentration increases
from that for a purely diffusion
fl
flame with increasing levels of premixing and peaks
at
Φ p = 3.32. Figure 6 had shown that the exit temperature decreases in this range
and this decrease is especially sharp around this point. As the combustion is hin-
dered due to the decrease in temperature, which in turn is caused by the presence of
an excess of primary air, the concentration of CO increases. However, the
fl
ame
Fig. 6 Temperature variation
with premixing equivalence
ratio
1.00
Normalized Temperature
0.98
0.96
0.94
0.92
0.90
0.88
0.86
0.84
0.82
0.80
0
1
2
3
4
5
6
7
8
9
10 11 12
Φ
p
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