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FORCE MAIN ODOR CONTROL   LAGUNA BEACH, CA WEF Odors and Air Emissions 2008
[object Object],[object Object],[object Object],[object Object],TWO APPROACHES IN ODOR CONTROL
CORROSION CONCERN
[object Object],[object Object],[object Object],[object Object],[object Object],SUPER OXYGENATION D.O. levels of 50 – 100 mg/L D.O. Saturation  =  40 mg/L at 1 ATM of Pressure using O2
TECHNOLOGY OVERVIEW Oxygen Gas Unscreened Raw Wastewater Force Main Oxygenated Raw Water Sidestream  Pump
ECO 2  ®   Oxygenation Cone System Intake System Discharge Oxygen Supply Booster Pump Influent 18” Force main 3 miles long Lift Station Wet Well TYPICAL FORCE MAIN INSTALLATION
SYSTEM COMPONENTS
Liquid Oxygen SOURCES OF OXYGEN O 2  Generator
ONSITE OXYGEN GENERATION
COST – LOX vs. GENERATION 5 Year N/A Payback $14,000 $24,500 Annual Operating Cost Electrical Cost $11,000 O&M Cost $3,000 Product Cost $18,500 Annual Lease $6,000 Operating Cost $53,000 $5,000 Capital Cost 1,000  1,000  Oxygen (lbs / day)  GENERATION LOX
LAGUNA BEACH, CA ,[object Object],[object Object],[object Object],[object Object],[object Object]
BLUEBIRD FORCE MAIN Bluebird PS Transition Manhole ,[object Object],[object Object],[object Object],[object Object]
BLUEBIRD PUMP STATION
FORCE MAIN DISCHARGE
MONTAGE RESORT
UNTREATED H2S LEVELS Peak: 800 ppm  Average: 145 ppm
[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],PROJECT OBJECTIVES
[object Object],[object Object],[object Object],[object Object],[object Object],SYSTEM DESIGN
DESIGN RULES OF THUMB 1.  Oxygen Demand: 1 Hour HRT = 10 mg/L D.O. Uptake 2.  Pressure Check: 1 ft Head Pressure = 1 mg/L D.O.
DESIGN DATA CHECKLIST
[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],DESIGN CALCULATIONS
PERFORMANCE STANDARD Measurement Point at Force Main Discharge Manhole Gas Phase H 2 S Average  <  5 ppm H 2 S
INSTALLATION INSIDE STATION
INSTALLATION LAYOUT Oxygen Generator Force Main  Pump Force Main ECO2 Cone Main Level Basement Sidestream  Pump
SYSTEM COMPONENTS
LAGUNA BEACH -  H 2 S RESULTS
Average: 0.4 ppm LAGUNA BEACH -  H 2 S RESULTS
BEFORE Average: 145 ppm
AFTER Average: 0.4 ppm
ECONOMICS - $40,700 Electrical Cost (Oxygen Generator) (15 hp Side stream Pump) - 3.6 Years Payback - $397,000 Capital Cost (Equipment + Installation) - $109,300 Annual Savings $150,000 -  Chemical Cost CHEMICAL ECO2
[object Object],[object Object],[object Object],[object Object],[object Object],APPLICATIONS
TRA - Dallas, TX 150 MGD  .   14,000 lb O 2  / day Anticipated Results:  0.0 mg/L DS into Primary Clarifier
Cheeney Creek WWTP - Fishers, IN 5.0 MGD  .  5 hrs HRT  Results:  5 - 10 mg/L D.O. at Plant Headworks Allisonville Road Smock Creek Hague Road
KSD - Kennebunk, ME 5.0 MGD  .   210 lb O 2  / day Results:  WWTP Plant D.O. Discharge 8 mg/L
GPA - Savannah Harbor, GA 22 MGD  .  30,000 lb O2 / day Results:  Cone D.O. Discharge 150 mg/L
[object Object],[object Object],ACKNOWLEDGMENTS
 
[object Object],[object Object],[object Object],[object Object],[object Object],ROOT CAUSE OF ODOR / CORROSION
[object Object],[object Object],[object Object],[object Object],[object Object],HENRY’S LAW AND GAS TRANSFER
FORCE MAIN ODOR CONTROL

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