Environmental Engineering Reference
In-Depth Information
Temperature
(K)
25
20
15
10
5
0
10
Boiler depth (m)
0
Fig. 4.74 Temperature distribution in the furnace (K)
20
30
1700
Transection average temperature
Transection maximum temperature
Temperature in-situ
1600
1500
1400
1300
DŽ
1200
1100
1000
900
10
15
20
25
30
35
40
h (m)
Fig. 4.75 Comparison results between CFD and in-situ
4.5.2.2 Gas Components and Hg Distribution Fields
Figs. 4.76 and 4.77 show the concentration of gas components and Hg distribution
in the furnace. The temperature, velocity and the densities of O 2 , CO, HCl, H 2 S, Cl,
Cl 2 , Hg, HgCl 2 , HgO in the lower secondary air section are shown in Fig. 4.76. The
high temperature area and the high speed area almost coincide, which is outside the
rotating flame ball, as shown in Figs. 4.76(a) and (b). The concentration of O 2 and
CO is shown in Figs. 4.76(c) and (d). The former represents the oxidizing atmos-
phere and the latter the reducing atmosphere. The oxygen with high concentration
from the secondary air inlet has a deflection because of the brush from upstream.
 
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