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Fermentation Enhanced Nutrient Removalat Janesville WWTF WWOA – 46th Annual Conference
October 11, 2012
Presented by: Nathan Cassity, AECOMJoe Zakovec, Janesville Wastewater Utility
Presentation Outline
• Project background• BNR design• Startup and operation• Supplemental carbon pilot• What’s next?
Project Background
Project Background
• Current flow of 14 MGD• Serves population of 60,000• Biological phosphorus removal (BPR) first
incorporated 2001 to 2003– Anaerobic / Oxic (A/O) configuration– Included backup chemical P removal facilities– Influent lacked sufficient VFAs– Chemical polishing used off and on
Project Background
Mixing Basins
Aeration Basins
PE PERAS
Anaerobic AerobicMixed Liquor
2003 A/O Process Configuration
20% anaerobic volume
80% aerobic volume
Project Background
2003 A/O Process Configuration
Project Background
• 2010 – 2011 upgrade project– $32 million upgrade– Capacity increase to 20 MGD– Incorporated biological nutrient removal
(BNR)– New cogeneration facilities– Renovation of several 30+ year-old facilities
Biological Nutrient Removal Design
Biological Nutrient Removal Design
• Project goals:– Enhance biological phosphorus removal to
eliminate chemical polishing• Effluent phosphorus goal between 0.3 mg/L and
0.5 mg/L– Incorporate biological nitrogen removal
• Effluent nitrogen goal between 6 mg/L and 8 mg/L
• Resources utilized– BioWin computer simulations– AECOM Canada experts
Biological Nutrient Removal Design
• Process configuration– Anaerobic / Anoxic / Oxic (A2O)
Anaer. Anoxic Aerobic
RAS WAS
Influent EffluentMixed Mixed Aerated
Internal Nitrate Recycle
Biological Nutrient Removal Design
PE RAS
Anaerobic
Aerobic
Mixed Liquor2011 A2O Process Configuration
12% anaerobic volume21% anoxic volume67% aerobic volume
Anaerobic
Anaerobic Aerobic Aerobic
Anoxic
Anoxic
Swing
SwingAnoxic
Anoxic
Swing
Anoxic
Anoxic
Swing
Biological Nutrient Removal Design
2011 A2O Process Configuration
PE RAS
Anaerobic
Aerobic
Anaerobic
Anaerobic
Aerobic Aerobic
Anoxic
Anoxic
Swing
Swing
Anoxic
Anoxic
Swing
Anoxic
Anoxic
Swing
Biological Nutrient Removal Design
• Fermentation incorporated into design due to low wastewater strength– Primary sludge is pumped to the fermenters– Fermenters store and thicken the sludge– VFA production is based on time and temperature– Operation based on target SRT
FermentersOverflow(VFAs)
Primarysludge
Fermented primary sludge
Biological Nutrient Removal Design
Fermenter SRT vs VFA Production
0.0
50.0
100.0
150.0
200.0
0 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15
time - days
mg/
L
Acetic Acid
• Overflow from fermenters provides the necessary VFA for biological phosphorus removal
• The remaining VFA flows into the anoxic zone for biological nitrogen removal
Biological Nutrient Removal Design
Anaer. Anoxic Aerobic
RAS WAS
Influent EffluentMixed Mixed Aerated
Internal Nitrate Recycle
Fermenter Overflow (VFAs)
Biological Nutrient Removal Design
Anaerobic Zones
Anoxic Zones Aerobic Zones
VFAs
Nitrate Recycle
Swing
Biological Nutrient Removal Design
• System components– Baffle walls
• Create boundaries for the environments• Minimize short-circuiting
Biological Nutrient Removal Design
• System components– Mixers
• Keep tankage completely mixed without aeration
Biological Nutrient Removal Design
• System components– Nitrate recycle pumps
• High flow, low head pumping between tankage
Biological Nutrient Removal Design
• System components– Swing zones – aeration can be turned on or
off
Startup and Operation
Startup and Operation
• BNR system overview
Fermenters
Anaerobic
Anoxic
Notconvertedyet
Aerobic
Startup and Operation
• Fermenters and anaerobic zones
Fermenter Overflow (VFAs)
Startup and Operation
• Fermenter overflow– Flow of 0.9 MGD– 7% of forward flow– Currently generating
1000 lbs/day VFA
Date Volatile Acids (mg/L)
01/03/12 10001/24/12 8702/14/12 12502/22/12 11502/28/12 21603/07/12 21803/14/12 18303/14/12 16303/21/12 6003/27/12 11804/04/12 7204/09/12 15004/18/12 12104/24/12 10505/04/12 139Average 132
Startup and Operation
0.00
0.50
1.00
1.50
2.00
2.50
3.00
3.50
4.00
5/17/2011 7/6/2011 8/25/2011 10/14/2011 12/3/2011 1/22/2012 3/12/2012
Efflue
nt Pho
spho
rus (mg/L)
Janesville Effluent Phosphorus
Start-up
Ethanol Waste Addition
Ethanol Waste Removal
Average 0.50 mg/L
Startup and Operation
• Biological Phosphorus Removal– Increase VFAs using fermentation
Fermenter Overflow (VFAs)
Total Phosphorus Average 0.09 mg/L
Total Nitrogen Average 5 mg/L
**Ethanol Plant Waste Being Received**
0
1
2
3
4
5
6/20/2012 6/30/2012 7/10/2012 7/20/2012 7/30/2012 8/9/2012 8/19/2012
Efflue
nt Pho
spho
rus (mg/L)
Janesville Effluent PhosphorusMost Recent Two Months
Startup and Operation
Total Phosphorus Average 0.35 mg/L
Total Phosphorus Average 0.50 mg/L
Startup and Operation
• Anoxic and aeration zones
0
2
4
6
8
10
12
14
16
5/27/11 7/16/11 9/4/11 10/24/11 12/13/11 2/1/12 3/22/12 5/11/12 6/30/12 8/19/12
Efflue
nt Nitrogen (m
g/L)
Janesville Effluent Total Nitrogen 2011 ‐ 2012
Startup and Operation
Start-upEthanol Waste Addition
Ethanol Waste Removal Average
7.0 mg/L Average 5.5 mg/L
Supplemental Carbon Pilot
Supplemental Carbon Pilot
• Pilot Project– Evaluate feeding supplemental carbon from
QLF Specialty Products • Liquid molasses blend product• 7.3 lbs COD per gallon (875,000 mg/L)
• Pilot Goal– Stabilize BPR performance near 0.10 mg/L
effluent total-P (no filters and no ferric chloride)
Supplemental Carbon Pilot
• QLF product fed into fermenters– Fermenters convert product to VFA’s– VFA loading in fermenter overflow increased
Fermenters
Overflow (VFAs) to Anaerobic Zones
Primarysludge
Fermented primary sludge
80 gpd QLF Feed(600 lb/d COD)
0
50
100
150
200
250
300
12/23/11 02/11/12 04/01/12 05/21/12 07/10/12 08/29/12
Volatile Acids (m
g/L)
Janesville Fermenter Overflow Volatile Acids
Supplemental Carbon Pilot
1000 lbs/day VFA
1600 lbs/day VFA
Started feeding 80gpd QLF Solution
Ave. temp. in July was 94°F
0
0.5
1
1.5
2
2.5
3
7/12/2012 7/22/2012 8/1/2012 8/11/2012 8/21/2012 8/31/2012 9/10/2012
Efflue
nt Pho
spho
rus (mg/L)
Janesville Effluent Phosphorus
Supplemental Carbon Pilot
Industrial Discharge?
Started feeding 80 gpd QLF Solution
0.10 mg/L P Average0.35 mg/L P Average
What’s Next?
What’s Next?
• 2012 Fall / Winter Activities– Continue supplemental carbon feed pilot– Continue BNR optimization study
• Analysis and adjustment of operating parameters• Stabilization of biological phosphorus removal
– Evaluate (based on above results) if TMDL P limits can be achieved without upgrades.
Fermentation Enhanced Nutrient Removalat Janesville WWTF WWOA – 46th Annual Conference
October 11, 2012
Presented by: Nathan Cassity, AECOMJoe Zakovec, Janesville Wastewater Utility