City of Dayton Advanced
Wastewater Treatment Facility
TREATMENT REQUIRED
|
PARAMETER |
30 - Day
Average |
30 - Day
Average |
Actual
Performance |
Actual
Performance |
|
Summer |
Winter |
Summer |
Winter |
| CBOD5 |
8 |
25 |
BDL |
BDL |
| SS - mg/L |
12 |
30 |
BDL |
BDL |
| Coliform/100 ml |
1,000 |
N/A |
30 |
N/A |
| Chlorine Residual - mg/L |
<0.038 |
N/A |
BDL |
N/A |
| Dissolved Oxygen - mg/L |
>5.0 |
>5.0 |
7.7 |
7.8 |
| Ammonia (NH3-N) - mg/L |
1 |
5 |
BDL |
BDL |
BDL = Below
Detectable Level
PLANT DESIGN DATA
(All loadings calculated at 72 MGD)
| DESIGN YEAR |
2010 |
| DESIGN POPULATION |
340,000 |
| AVERAGE DESIGN FLOW |
72 MGD |
| MAXIMUM DESIGN FLOW |
150 MGD |
DESIGNED PERFORMANCE
|
At 72 MGD |
BOD |
SS |
NH3-N |
|
|
|
|
| Influent Concentration - mg/L |
280 |
250 |
25 |
| Primary Removal - % |
32 |
63 |
N/A |
| Secondary Removal - % |
85 |
85 |
N/A |
| AWT Influent - mg/L |
40/45* |
40/45* |
26/26* |
| AWT Removal - % |
80/45* |
50/55* |
92/70* |
| Effluent Filter Influent - mg/L |
|
35 |
|
| Effluent Filter Removal - % |
|
85 |
|
| Effluent Concentration - mg/L |
12/30* |
12/30* |
2/8* |
* = (summer/winter)
TREATMENT UNITS
PUMP STATIONS
| Total Pumping Capacity |
210 MGD |
| Number of Pumps |
7 |
| Capacity of Each |
30 MGD |
| Total Pumping Capacity |
35 MGD |
| Number of Pumps |
5 |
| Capacity of Each |
7 MGD |
GRIT BASINS
- NORTH - Gets 40% of Total Flow
| Number of Basins |
2 |
| Dimensions |
40 ft X 40 ft |
| Depth |
2 ft |
- SOUTH - Gets 60% of Total Flow
| Number of Basins |
2 |
| Dimensions |
40 ft X 40 ft |
| Depth |
3 ft |
PRIMARY SETTLING
- NORTH - Gets 40% of Total Flow
| Number of Basins |
4 |
| Diameter |
115 ft |
| Water Depth |
12 ft |
| Capacity (each) |
0.93 MGD |
| Surface Overflow Rate (all units
operating, 72 MGD) |
693 gpd/ft2 |
| Detention Time |
3.1 hours |
- SOUTH - Gets 60% of Total Flow
| Number of Basins |
3 |
| Dimensions |
240 ft X 80 ft |
| Water Depth |
13 ft |
| Capacity (each) |
1.87MGD |
| Surface Overflow Rate (all units
operating, 72 MGD) |
750 gpd/ft2 |
| Detention Time |
3.1 hours |
TRICKLING FILTERS
| Number of Basins |
20 |
| Diameter |
24165 ft |
| Media Depth |
7 ft |
| Media Type - Random fill slag
& limestone |
2 in to 4 in diameter |
| Organic Loading |
35 lbs BOD/1000 ft3 |
| Hydraulic Loading |
168 gpd/ft2 |
LOW LIFT PUMP STATION
| Total Pumping Capacity |
242 MGD |
| Number of Constant Speed Pumps |
2 |
|
|
72 MGD |
| Number of Variable Speed Pumps |
2 |
|
|
50 MGD |
SECONDARY SETTLING
- EAST
-Gets 40% of Total Flow
| Number of Basins |
4 |
| Diameter |
120 ft |
| Water Depth |
10.3 ft |
| Capacity (each) |
0.87 MGD |
| Surface Overflow Rate (all units
operating, 72 MGD)
| 636 gpd/ft2
|
| Detention Time |
2.9 hours |
- WEST Gets 60% of Total Flow
| Number of Basins |
6 |
| Diameter |
120 ft |
| Water Depth |
12.3 ft |
| Capacity (each) |
1.04 MGD |
| Surface Overflow Rate (all units
operating, 72 MGD)
| 636 gpd/ft2
|
| Detention Time |
3.5 hours |
INTERMEDIATE PUMP STATION
| Number of Variable Frequency
Drive Pumps |
3 |
| Number of Constant Speed Pumps |
2 |
| Capacity of Each |
38
MGD |
ACTIVATED SLUDGE PROCESS - 3 Pass, plug flow, fine bubble
dome diffusers, tapered aeration
| Number of Basins |
8 |
| Dimensions |
153 ft X 135 ft |
| Water Depth |
18 ft |
| Capacity (each)
| 2.8 MG
|
| Ammonia applied
| 15,612 lbs/day
|
| MCRT (avg)
| 11 days
|
| F/M Ratio
| 0.1
|
| Detention Time |
7.4 hours |
| Dome Diffusers |
6,030 per
Basin |
AERATION SYSTEM
| Number of Activated Sludge
Compressors |
4 |
| Capacity (each) |
22,000 scfm |
| Motor (4160 V) |
1,500 HP |
| Number of Channel Air
Compressors |
3 |
| Capacity (each)
| 3,000 scfm
|
| Motor (460 V)
| 150
HP |
FINAL SETTLING
| Number of Basins |
8 |
| Diameter |
160 ft |
| Water Depth |
16 ft |
| Capacity (each)
| 2.4 MGD
|
| Collectors
| Hydraulic suction, multiple
orifice header
|
| Surface Overflow Rate (all units
operating, 72 MGD) |
448 gpd/ft2 |
| Detention Time |
6.4
hours |
RETURN & WASTE ACTIVATED SLUDGE PUMPING
STATION
| Number of pumps |
10 |
| Capacity of Each |
13.6 MGD |
| Variable Frequency Drives |
10 |
| Number of pumps |
3 |
| Capacity of Each |
250 gpm |
| Variable Frequency Drives |
3 |
| Emulsion Polymer Storage |
4 units |
| Polymer Mix & Aging Tanks |
8 units |
| Chemical Feed Pumps |
8
units |
EFFLUENT FILTERS
| Tertiary Filters - 4 cells/units |
5 units |
| Cell dimensions (each) |
30 ft X 30 ft |
| Type |
Declining Rate, Automatic Gravity
Backwash |
| Maximum Capacity |
115 MGD |
| Blending Design Rate |
35 MGD |
| Media Type |
Anthracite Coal |
| Media Depth |
30 inches |
| Media Size |
1.4 to 1.6 mm |
| Backwash |
Combined simultaneous water and
air scour, 12 gpm/ft2 water, 4 cfm/ft2 air |
| Filter Run Time (design) |
18.8
hrs |
CHLORINATION FACILITY
| Liquid Feed Auto-Switchover
Systems |
2 units |
| Evaporators |
2 units |
| Chlorinators |
3 units |
| Total Feed Capacity (effluent) |
6,000 lbs/day |
| Total Feed Capacity (Non-Potable
Water) |
200 lbs/day |
| Chlorination Point |
After Effluent Filters |
| Contact Time @ peak flow |
15
Minutes |
CHLORINATION / DECHLORINATION / POST AERATION
BASINS
| Number of Basins - (3 passes
each) |
2 |
| Basin dimensions |
153 ft X 78 ft X 10ft |
| Chlorine Contact |
First Pass & Half of Second
Pass |
| Dechlorination |
Last Half of Second Pass |
| Coarse Bubble Post Aeration |
Third
Pass |
DECHLORINATION FACILITY - Liquid Sodium Bisulfate - 38%
NaHSO3
| Storage Tanks (5,700 gal each) |
3 units |
| Day Tanks (250 gal each) |
2 units |
| Chemical Feed Pumps (50 to 500
gpm) |
3
units |
POST AERATION FACILITY
| Blowers (positive displacement) |
3 units |
| Capacity (each) |
2,400 cfm @6
psi |
ACTIVATED SLUDGE THICKENING
| Dissolved Air Flotation Tanks |
4 units |
| DAF Tank Surface Area |
400 ft2 |
| Design Solids Loading (avg) |
9350 lbs/day |
| Feed Solids Concentration (avg) |
0.7% |
| Float Solids Concentration (w/o
polymer) |
4%
peak |
FERROUS CHLORIDE FEED FACILITY
| Location |
Inside DAF Building |
| Purpose |
Control of H2S in digester gas |
| Storage Tanks (2,500 gal each) |
2 units |
| Chemical Feed Pumps (0 to 280
gpm) |
2
units |
ANAEROBIC DIGESTERS - EAST BANK
| Number of Units |
4 |
| Diameter |
90 ft |
| Depth |
33 ft |
| Cover Type |
Floating |
| Operating Temperature |
98 F |
| Approx. Operating Volume (each
Digester) |
207,816
ft3 |
ANAEROBIC DIGESTERS - WEST BANK
| Number of Units |
4 |
| Diameter |
85 ft |
| Depth |
30 ft |
| Cover Type |
Floating |
| Operating Temperature |
98 F |
| Approx. Operating Volume (each
Digester) |
164,560 ft3 |
DIGESTER GAS STORAGE
| Gas Generation per day |
810,000 ft3 |
| Gas Holding Sphere |
1 unit |
| Sphere Diameter |
52 ft |
| Sphere Volume |
73,620 ft3 |
| Gas Holding Capacity @ 50 psi |
300,000
ft3 |
BIOSOLIDS BENEFICIAL USE
| Contractor |
Bio Grow Systems (Wheelabrator)
Inc. |
| Use Method |
Agronomic Land Application |
| Permitted Land in 13 Counties |
>30,000 acres |
| Biosolids Storage On-Site,
liquid |
500,000 gal |
| Biosolids Storage Area On-Site,
cake |
15,000 ft2 |
| Belt Filter Presses (2 meter) |
4 units |
| Biosolids Processed Daily (avg) |
45 dry
tons |
ENERGY RECOVERY
| Gas Burning Engines |
3 units |
|
|
12 |
|
| Turbo-charged
|
| Generators (direct coupled to
engines) |
3 units |
|
|
4160 |
|
| 3
|
|
| 60
|
| Design Loads on WWTP |
|
|
|
6,734,000 |
|
| 7,336 KW
|
| Design Production at WWTP |
|
|
|
8,467,000 |
|
| 1,620 KW
|
| Actual Production at WWTP |
|
|
|
8,313,917 |
|
|
922
KW |
ODOR CONTROL- Covers Headworks, N & S Grit, N
& S Primaries, Scum Collection Buildings
| Type |
Packed Tower |
| Diameter |
10 ft |
| Packing Depth |
13 ft |
| Packing Type |
Random Fill Polypropylene Media |
| SCFM |
25,000 |
| H2S Inlet |
300 PPM |
| H2S Outlet |
1 PPM |
| Liquid Recirculation Rate |
468 gpm |
| Blowdown Rate (Max) |
5
gmp |
DETRITUS DEWATERING BUILDING
| Building Dimensions |
60 ft X 80 ft |
| Detritus Screw Press |
1 |
- Screw Press Production Capacity
|
5 cu. yds. dry material / Hr |
| Conveyors |
|
|
|
1 |
- Directional Cross Conveyor
|
1 |
|
|
2 |
| Roll Off Containers |
2-20 cu. yd |
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