Environmental Engineering Reference
In-Depth Information
namics analysis on mercury transformation is to be performed if possible, if the
typical gas components, initial concentration of mercury and reaction condition
(pressure, temperature) are input into the Equilib module.
Table 4.12 shows mercury compound included in the model, which comprises the
mercury chemical species in gas/liquid/solid phases when specified elements or
compounds react or partially react to reach a state of chemical equilibrium. In fact,
most of them are intermediate products which are unstable, liable to decompose
with a temperature increase.
Table 4.12 Mercury compound included in the model
Gas phase
Hg, Hg[+], Hg 2 , HgH, HgCl, HgCl 2 , Hg(CH 3 ) 2 , HgO, HgS
Liquid phase
Hg, HgCl 2 , Hg(CH 3 ) 2
HgO, HgS, HgSO 4 , Hg 2 SO 4 , Hg 2 CO 3 , Hg 2 C 2 O 4 , Hg 2 (N 3 ) 2 , Hg 2 (N 3 ) 2 ,
Hg 2 (CNS) 2 , Hg 2 (C*N*S) 2
Solid phase
During calculation, four cases with various initial conditions are given here
(Table 4.13). A typical coal-fired flue gas such as O 2 (0 - 7%), CO 2 (fixed at 13%),
N 2 as balance gas (80% - 87%), were considered firstly. Other cases involved 4%
O 2 , 13% CO 2 , 83% N 2, HCl (0 - 1000 ppm), NO (0 - 900 ppm), SO 2 (0 - 1200 ppm)
simultaneously. The initial mercury concentration in the flue gas was 18.75 g/m 3 ,
equivalent to 9.3E - 08 by mole fraction. The flue gas temperature was arranged at
300 900 K, ambient pressure. In general, mercury tended to be oxidized with the
assistance of an oxidizing agent, such as chlorine, oxygen, nitrogen oxide, sulfur
oxide. The mercury transformation was defined as mercury oxidization, as
mercury transformation
mass of mercury oxide in the flue gas
ˁ
(4-28)
˙
*100%
ˇ
mass of mercury oxide
mass of elemental mercury
Table 4.13 Initial condition during the calculation
Case 1
Case 2
Case 3
Case 4
O 2
N 2
CO 2
4%O 2 -13%CO 2 -83%N 2
O 2
(%)
Mole
fraction
N 2
(%)
Mole
fraction
CO 2
(%)
Mole
fraction
HCl
(ppm)
NO
(ppm)
SO 2
(ppm)
0
0
87
1.214
13
0.181
0
0
0
0.2
0.002
86.8
1.212
13
0.181
20
100
100
0.5
0.007
86.5
1.207
13
0.181
50
300
500
1
0.014
86
1.200
13
0.181
100
600
1200
2
0.028
85
1.186
13
0.181
150
900
-
4
0.056
83
1.158
13
0.181
500
-
-
7
0.098
80
1.117
13
0.181
1000
-
-
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