Environmental Engineering Reference
In-Depth Information
Transformation in Flue Gas
0.4
-0.8
0.0
-1.2
-0.4
-1.6
-0.8
-2.0
1.0
1.2
1.4
1.6
1.2
1.4
1.6
1.8
ln
C
Hg
Fig. 4.28
and
K
1
when
C
HCl
=60 ppm and
T
=573 K (
=1.8;
K
1
=0.07694;
r
2
=0.923)
ln
C
Hg
Fig. 4.27
and
K
1
when
C
HCl
=60 ppm and
T
=373 K (
=1.847;
K
1
=0.01378;
r
2
=0.994
)
1.5
0.4
1.0
0.0
0.5
-0.4
0.0
-0.8
-0.5
-1.2
-1.0
.6 .8 .0 .2 .4 .6
0.8
1.0
1.2
1.4
1.6
1.8
ln
C
Hg
Fig. 4.30
and
K
1
when
C
HCl
=60 ppm and
T
=973 K (
=1.85;
K
1
=0.1078;
r
2
=0.8901)
ln
C
Hg
Fig. 4.29
and
K
1
when
C
HCl
=60 ppm and
T
=773 K (
=1.531;
K
1
=0.07951;
r
2
=0.934)
0.4
1.0
0.8
0.0
0.6
-0.4
0.4
-0.8
0.2
0.0
-1.2
-0.2
0.8
0.9
1.0
1.1
1.2
1.3
1.0
1.2
1.4
1.6
1.8
ln
C
Hg
ln
C
Hg
Fig. 4.31
and
K
1
when
C
HCl
=60 ppm and
T
=1173 K (
=1.789;
K
1
=0.2290;
r
2
=0.931)
Fig. 4.32
and
K
1
when
C
HCl
=80 ppm and
T
=373 K (
=1.814;
K
1
=0.03939;
r
2
=0.956)
0.4
0.8
0.4
0.0
0.0
-0.4
-0.4
-0.8
-0.8
-1.2
1.0
1.2
1.4
1.6
0.6
0.8
1.0
1.2
1.4
1.6
1.8
ln
C
Hg
Fig. 4.33
and
K
1
when
C
HCl
=80 ppm and
T
=573 K (
=1.91;
K
1
=0.066;
r
2
=0.975)
ln
C
Hg
Fig. 4.34
and
K
1
when
C
HCl
=80 ppm and
T
=773 K (
=1.86;
K
1
=0.07024;
r
2
=0.961)
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