Title: Toledo Waterways Initiative and 185 mgd HRT Facility Wet Weather Partnership CSO Workshop Chicago, I
1Toledo Waterways Initiative and 185 mgd HRT
FacilityWet Weather Partnership CSO
WorkshopChicago, IL
- Larry Jaworski - Black Veatch
- F. Chris Middlebrough City of Toledo, OH
- Carol L. Hufnagel Tetra Tech
2Background
- Late 80s Early 90s Three CSO storage
tunnels constructed. - October 1991 Original US/OEPA vs. Toledo
lawsuit. - July 2002 Toledo voters approve ordinance to
settle lawsuit. - Consent decree.
- Start of Toledo Waterways Initiative.
3Consent Decree Requirements
- Discharge from Outfall 002 allowed only when flow
exceeds 400 MGD - Activated sludge treatment of all flows up to 195
MGD - 60 MG EQ basin (reduced to 25 MG pending EPA
approval) dewatered flows must receive activated
sludge treatment - 185 MGD high rate clarification facilities may
discharge only when flow exceeds 195 MGD EQ
basin is full - Prohibited return of wet weather treatment solids
to main plant headworks
4Bay View WWTP Flows
- Toledo, OH sewer system is 30 combined
- Bay View WWTP flows
- 45 MGD dry weather
- 70 MGD average annual
- 130 MGD peak month
- 400 MGD peak hour
- Maximum flow through secondary treatment is
approximately 195 MGD
5HRT Milestones
- February 2003 - Pilot Test Completed
- HRT - DensaDeg vs. Actiflo
- UV Disinfection - Medium Pressure vs. LPHO
- 2005 Construction Started
- October 2006 Performance Testing of HRT
- 2007 Begin Two-Year Effectiveness Study
6HRT Evaluation Factors
- Discharge Requirements
- Frequency of Use/Chemical Usage
- Pretreatment Needs
- Pumping
- Fine Screening
- Grit Removal
- Odor Control
- Startup Shutdown Requirements
- Solids Handling Requirements
- Flexibility to Use for Primary Tertiary
Treatment
7HRT Pilot Test
- Actiflo - Kruger (Veolia Water)
- DensaDeg - IDI
8Actiflo DesignConsiderations
- Fine Screening (lt 1/4 inch openings)
- f (Hydrocyclone opening)
- Requires Grit Removal
- Thin Sludge (lt0.5 solids)
- Volume 2 to 3 of Influent Flow
- ( capacity of recirculation
- pumps)
- Media Recirculation
- Cleaning System
9DensaDeg Design Considerations
- Less Consistent Performance Due to Ballast Media
(Sludge) Variability
- Fine Screening (lt 1/2 inch openings)
- Concentrated Sludge (3 to 4 solids)
- Slower Startup Due to Reliance on Sludge
Recirculation - Potentially deeper settling compartment than
Actiflo
10HRT Intermittent Operation Issues
- Dry process startup time required to establish
process equilibrium - Handling off-spec effluent
- Bringing parallel units on-line
- Maintaining a standby operational mode
- necessary for Actiflo
- Dewatering to prevent nuisance conditions
11Other Uses for HRT
- Primary Treatment
- Derate to about 1/3 to ½ of Wet Weather Treatment
Capacity - Uses less Ferric Chloride than for Wet Weather
Treatment - Densadeg better than Actiflo due to solids
thickening feature - Dry Weather Tertiary Treatment
- Lowers TSS phosphorus concentrations
- Improves chances of meeting 7-day limits when
averaged with wet days
12HRT Costs
- Capital costs very close to the same in most
cases - Smaller footprint for Actiflo due to higher
loading rates - Less pretreatment required for DensaDeg
- If solids cannot be returned to plant influent,
solids handling costs are lower for DensaDeg - OM costs slightly less for DensaDeg due mostly
to lower pretreatment requirements
13Reasons for Selection of DensaDeg
- No additional sludge processing facilities
required - No additional fine screening facilities required,
increasing amount of screening equipment to be
maintained and screenings to be handled - Rapid startup is not an issue
- Equipment is the same as existing equipment to
service and maintain - No need to maintain a standby mode
- No microsand and related maintenance and
housekeeping issues
14High Rate Clarification
EQ BASIN
UP TO 400 MGD
27 MGD
UP TO 205 MGD
SCREENING GRIT REMOVAL
SECONDARY CLARIFIERS
BAY VIEW PUMP STATION
CHLORINE CONTACT BASIN
232 MGD
CHLORINE CONTACT REAERATION
AERATION BASINS
168 MGD
PRIMARY CLARIFIERS
UP TO 195 MGD
PRIMARY CLARIFIERS
GRIT REMOVAL
SKIMMINGS REMOVAL
UP TO 400 MGD
EFFLUENT PUMPING
NEW WET WEATHER FACILITIES
15Bay View WWTP Layout
16Toledo, OhioBay View Wastewater Treatment Plant
Reaeration Chlorination
Main WWTP
XS Flow
DensaDeg
EQ Basin
Vortex Grit Removal Screening (1 sewer)
17Toledo, OH DensaDeg Layout
18Toledo, OH DensaDeg HRT
19HRT Pipe Gallery Sludge Pumps
20HRT and EQ Basin
21HRT Treatment Results
- Performance testing results
- Effluent TSS 7 to 38 mg/L with average of 25
mg/L. - TSS removal averaged approximately 80.
- Effluent CBOD 22 to 177 mg/L with average of 52
mg/L. - CBOD removal averaged approximately 55.
- Mixture of dry and wet weather conditions during
performance testing. - 2-year effectiveness study ongoing thru 2008.
22First 6 Months of 2-year Effectiveness Study
23Wet Weather Treatment System Performance
24Two-Year Effectiveness Study
- Ongoing.
- Performance testing results verified.
- Continuing optimization.
- Have met final effluent limitations at flows up
to 390 MGD. Including the big rain events of
late August 2007.
25Facility Optimization
- Pilot study and performance testing used 40 mg/L
or more FeCl3 and up to 3 mg/L of polymer - while City now generally doses 10-30 mg/L
FeCl3and 0.5-2 mg/L of polymer. - A lot of DensaDeg effluent sent to activated
sludge system. - Jar testing of recent events to further optimize
FeCl3 to polymer ratios. - Generally constant ratio whether dosing 45 and
1.5 mg/L or 15 and 0.5 mg/L (FeCl3 and polymer,
respectively).
26Some Lessons Learned
- Density meters and blanket sludge depth detectors
not necessary for intermittent operation - Startup for intermittently operating facility
takes longer to work out glitches longer
warranty period is helpful - Returning HRT effluent to secondary can inhibit
nitrification - Alkalinity consumption (HRT nitrification) ?
loss of effluent buffering capacity (pH concerns)
27HRT Construction Costs
232 MGD Capacity
0.29/gpd
28HRT Annual OM Costs
Treating 1000 MG/yr
89/MG
29