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8/16/2019 Vincent Pinto.pdf
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=
• .
, ,
.
BB A F
.
BB
.
• I 1989
() 1989.
• F
1990 E
• F A
H I. ( H B
I.)
• F BB A
2002 H
• 1,000
2010
Dr. Hallvard Ødegaard
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,
.
BB ,
Stagnant LiquidLayer
Imbedded
ParticulateMatter
Moving
Mixed
Liquor
Out Diffusionof
Biodegradation
Products
Erosion
Biofilm
BWT Media
Nutrients & O2enter Biofilm via
Adsorption
Diffusionmechanism
,
.
E
.
.
20
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:
8/16/2019 Vincent Pinto.pdf
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D D
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D BD . ≥ 8 / .
.
.
I
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≤ 3 / .
.
D
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D D
I I I I I
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Comparison
MBBR Activated Sludge
Single Pass Process Requires returnin g the sludge back to the hea d
of the process
No Process Adjustments Requi res an operator exper ienced in measur ingand balancing the biomass concentrationsbetween the different process.
Smaller Foo t Print Larger volumes requ ired f or th e sa me level oftreatment.
Not affected by washout of biology Surges in flow can wash out the biomass losingtreatment capability
Less mechanical equipment Requires return pumps and controls for wastepumps
More efficient nutrient removal Takes up to 12 weeks to develop maturenitrifiers if they are lost or die out.
• (BD, H3, 3, .)
.
• : /2/.
• C BD ( )
.
• G BD BD .
• (2) : A (3) I (2/3).
•
()
• F = 2,000 3/
• BD C = 300 / = 300 /3
• BD = 2,000 300 = 600,000 /
• = 200 3
• F F = 50%
• A = 100 3
• A = 680 2/3 (I )
• A = 100 680 = 68,000 2
• = 600,000 / / 68,000 2 = 8.82 /2/
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• :rA = rA-max * SBODeff / (SBODeff + Khs)……………(1)where,rA = SBOD removal rate, g/m
2 /day
rA-max = Maximum SBOD removal rate at 20o C = 15 g/m2 /day
SBODeff = Effluent SBOD or Substrate SBOD, mg/lKhs = Substrate half saturation coefficient = 10 mg/l
rA = SALR [(SBODin – SBODeff) / (SBODin)]………….(2)where,
SALR = surface area loading rate, g/m2 /day
•
• BD
50 90% : 5 15 /2/
> 90% 1: 10 20 /2/
2: 5 7.5 /2/
E BD < 5 / LR 1:10 – 20 g/m2/day
LR2: 5 –7.5 g/m2/day
LR3: 1 – 5 g/m2/day
• NH3-N Removal
Single Reactor 50 – 90% removal LR: 0.5 – 0.7 g-N/m2/day
Two Reactors > 90% Removal LR 1 : 1.0 – 1.5 g-N/m2/day
LR2: 0.25 –0.75 g-N/m2/day
1: ,
• 22 D• E A BD • E H3 < 4 /• C (6 10 C )
• ( C)• BB C• C • C •
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,
0
0.5
1
1.5
2
2.5
3
0 0.5 1 1.5 2 2.5 3 N H 3 - N R e m o v a l R a t e ( g N / m 2 / d a y )
NH3-N Loading Rate (g N/m2/day)
NH3-N Removal Rate vs. NH3-N Loading Rate
100% Removal
7 - 10 oC
11 - 14 oC
15 - 18 oC
19 - 22 oC
• I 0.5 0.6 H3 /2/, 99%.
• I 0.6 0.8 H3 /2/, 90%.• I 0.8 1.0 H3 /2/, 80%.• I 1.0 1.5 H3 /2/, 60%.
• I A = 30 /
• E = 4 /• = 87%
• D• 0.6 0.8 H3/2/
0.0
10.0
20.0
30.0
40.0
50.0
60.0
70.0
0 30 60 90 120 150 180 210 240 270 300 330 360
H3I
H3E
Number of Days [in 2010]
C o n c e n t r a t i o n ( m g / L )
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2: • C C., I. (CCI) 5 6 (1923 3)
( A D)
•
2:
• 1: B
• 2: C
• 3: F
• C
• I : 15,000 GD (57 3/)
• I CD: 15,000 /
• E CD: < 550 /
• E : < 2 /
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• I CD > 10,000 /, H > 8 .
• I CD < 10,000 /, H 3 5
0
2000
4000
6000
8000
10000
18-Jun-05 25-Jun-05 2-Jul-05 9-Jul-05 16-Jul-05 23-Jul-05 30-Jul-05 6-Aug-05 13-Aug-05
Time (Days)
S C O D ( m g / L )
70
75
80
85
90
95
100
105
110
115
H R T ( h o u r s )
SCOD InfluentSCOD EffluentFloc SCOD EffluentHRT
• H 70 80 (3 4 ).
• H 100 .
• F D• I F: 15,000 GD (57 3 /)
• I CD: 15,000 /
• E CD: < 550 /
• : 95,472 (360 3)
• C: AC 450
• C F F: 31%
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0
5,000
10,000
15,000
20,000
25,000
19-Nov-05 27-Feb-06 7 -J un-06 15-Sep-06 24-De c-06 3 -Apr -07
Time (days)
C O D ( m g / L )
Influent COD
Effluent COD
0
2
4
6
8
10
12
14
2 5- Oc t- 05 2 4- Ma r- 06 21 -A ug -06 1 8- Ja n-0 7 1 7- Ju n- 07
Time (days)
E f f l u e n t P h e n o l ( m g / L )
. 97%
y = 0.9668x
R 2 = 0.999
0
5
10
15
20
0 2 4 6 8 10 12 14 16 18 20
COD Surface Loading Rate (gCOD/m2/d)
C O D R e m o v a l R a t e
( g T C O D - F C O D / m
2 / d )
Full-Scale
Lab-Scale
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