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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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