wzory na kol ścieki, INŻYNIERIA ŚRODOWISKA, rok 2, sem 2, TWiŚ
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Ukþady technologiczne do oczyszczania Ļciekw m. osadu czynnego
Oczyszczanie konwencjonalne
t
=
24
V
=
24
V
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0
Q Q
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q
q
Q
r
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Q
S
q
24
S
X
o
r
t
=
0
n
−
=
X
100
x
X
r
V
X
X
x
u
Q
Q
B
q
V
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6
X
10
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q
r
n
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Q
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Q
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−
S
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q
−
k
X
V
Q
d
0
Q
V
X
QQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQQ
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0
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y
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q
X
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obs
1
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k
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w
u
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Q
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sprawnoĻę usuwania zanieczyszczeı
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S
S
ȵ
−
(S
S
N
)
−
+
+
eNorg
syn
0N
eN
-
NH4
0
e
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Nitr
S
N
S
syn
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Q
N
syn
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obs
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Q
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syn
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zapotrzebowanie na tlen
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·248
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org
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N
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DN
usuwanie zwiĢzkw azotu
0,098
(15
−
T)
2,ʼn
=
ʼn
ʼn
Q
=
K
2,13
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p
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−
S
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k
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N
S
S
N
N
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−
4
−
−
utl
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NH
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syn
X
(
+
k
)
X
ʼn
d
o
p
y
N
N
utl
f
=
N
N
y
N
+
y
S
utl
NO
=
N
utl
r
3
N
n
1
+
+
N
t
q
utl
N
t
=
24
V
=
T
20
R
=
1,04
f
X
ȶ
−
N
N
R
N
N
N
T
20
R
=
−
r
ȶ
X
N
o
NO
DN
D
t
=
V
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t
3red
DN
R
DN
DN
DN
BZT
=
3
N
ȘX
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y
(S
e0
−
S
)
−
k
X
t
5usD
utl
d
0
S
q
BZT
−
S
BZT
Q
X
=
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q
=
r
=
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5N
0
5usD
C
(V
+
V
)
DN
N
t
O
QQQt
DN
Q+Qt
NQ
systemy zintegrowane
DNR
r
F
y'
N
q
NO
[(1
V
+
n)
NO
]
q
3
3
=
V
=
=
2,86
X
r
X
r
DNR1
DNR2
q
S
rDNR1QQQ0.03Q
Qr
x
Q+Q0.029QQQ
o
r
=
x
X
V
0.175
A
F
A
n
n
r
=
r
=
DNR2
DNR2
y
ʼn
2.86
y
ʼn
n
n
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