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hence, depend on z i . The total energy of turbulence is a composition of two energies
generated by mechanical (
˃ wm ) and convective (
˃ wc ) forces:
2
2
2
r
w ¼ r
wm þ r
wc :
ð 5
:
13 Þ
It is assumed here that mechanical and convective forces do not correlate. Then,
by analogy, we can write:
2
2
2
r
z ¼ r
zm þ r
zc :
ð 5
:
14 Þ
r
zc value is calculated on the assumption that
The
d
dt r zc ¼ r wc z ðÞ;
where
t ¼ u
= :
u
ð 5
:
15 Þ
Here z 0 is the effective height at which the vertical turbulence is calculated.
Dependences on the height for
˃ wc are parameterized with relationships:
(
2 = 3
54w 2
1
:
z ðÞ
z
=
for
z
0
:
1z i ;
\
2
r
wc ¼
ð 5
:
16 Þ
33w 2
0
:
for
z 0
:
1z i ;
where the level z = 0.1z i corresponds to similar values of the vertical constituent of
turbulence.
Let h s be the height of the pollutants
u. Then using
Eqs. ( 5.15 )and( 5.16 ) we obtain the relationship between h s and z i . For h s
'
jet and t have the scale x
=
0.1z i
the following approximation is valid:
2
33w 2
t 2
r
zc ¼ 0
:
ð 5
:
17 Þ
With h s < 0.1zi i we have:
8
<
2
=
3 t 2
54w 2
1
:
ð
h s =
z i
Þ
for
r zc \
h s ;
3
83w z 1 = 3
33h 2 = 3
s
0
:
t þ 0
:
for
h s r zc \
0
:
1z i ;
zc ¼
r
i
:
2
z 1 = 3
i
231h 2 = 3
s
0
:
581w t þ 0
:
0
:
05z i
for
r zc 0
:
1z i
The mechanical constituent in Eq. ( 5.14 ) is calculated on the assumption that
variations of the vertical gradient due to mechanical mixing are constant in the
boundary layer and determined with the relationship:
2
wm ¼ 1
2u 2
r
:
;
ð 5
:
18 Þ
where u * is the friction rate.
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