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    Wastewater Nitrogen Removal

    Bill McAllister, P.E.

    AMI Conference on Worker Safety, Human Resources, and the Environment

    Kansas City, MO

    March 9, 2011

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    Presentation Outline

    Background

    Biological Nitrogen Removal (BNR)

    Case Study-Beef Slaughter & Fab Facility

    Proprietary BNR Systems Evaluation Basis of Design

    Final Process Design

    Supplemental Carbon Evaluation Circular Vs Rectangular Basins (Common Wall)

    Wastewater Reuse Considerations

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    Background

    Regulatory Focus on Nutrient Reductions

    Nitrogen & Phosphorus

    Dead Zones in Coastal Waters

    State Issues Drinking Water Protection

    Recreation Use Protection

    Aquatic Life Protection

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    Background

    Nitrogen Removal Systems

    Biological Nitrogen Removal (BNR) Breakpoint Chlorination

    Ammonia Stripping

    Ion Exchange Membrane Filtration

    Advanced Oxidation

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    Biological Nutrient Removal

    Biological Nitrogen Removal Mechanisms

    Biological Conversion of Nitrogen to Nitrogen Gas Disposal of Biological Waste Sludge

    Many BNR Configurations and ProprietarySystems

    Conventional Bardenpho Process (Four Stage)

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    Biological Nutrient Removal

    Four Stage Bardenpho Process

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    Case Study

    Large Beef Slaughter and Fab Facility

    Wastewater Discharge to a Low Flow Stream

    Development of a Long-Term Wastewater Plan

    Reliable Removal of Ammonia & Nutrients

    Provide a Wastewater Quality for Future BeneficialReuse For Plant, Agriculture, and Other Water Needs

    Cost Effective

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    Case Study

    Reviewed & Screened Many PotentialProprietary BNR Systems and Conventional

    Activated Sludge

    Owner Selected Five Proprietary BNR Systemsto Further Evaluate and Visit Full-Scale

    Facilities. Siemens Orbal Process

    Schreiber Process

    Eimco Carrousel Process

    WesTech OxyStreamProcess

    Parkson Biolac Process

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    Case Study

    Siemens Orbal Process

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    Case Study

    Schreiber Process

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    Case Study

    Eimco Carrousel & WesTech OxyStream Processes

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    Case Study

    Parkson Biolac Process

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    Case Study

    Influent Wastewater Loadings

    (Anaerobic Lagoon Effluent)

    Parameter Daily Average

    Flow, MGD 3.6

    CBOD5, mg/L 300TSS, mg/L 800

    Ammonia Nitrogen, mg/L 190

    Alkalinity, mg/L 1,100

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    Case Study

    Effluent Quality Requirements

    Parameter Value

    BOD5, mg/L 16

    TSS, mg/L 30pH, s.u 6.0 to 9.0

    Ammonia Nitrogen, mg/L 1.2

    Nitrite+Nitrate Nitrogen, mg/L 10

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    Case Study

    Final Process Selection

    Conventional Bardenpho Process (Four Stage)

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    Case Study

    Final Process Size

    Process Unit Value

    Pre-Anoxic Basin 3,000,000 Gallons

    Aeration Basins (each) 3,000,000 Gallons

    Minimum Internal Recycle Flow 10,000 GPM

    Post-Anoxic Basin 900,000 Gallons

    Post-Aeration Basin 50,000 Gallons

    Final Clarifiers (each) 90 ft. Diameter

    Aerated Sludge Storage & Thickening Basin 900,000 Gallons

    Belt Filter Press Capacity 35,000 dry lbs/day

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    Case Study

    Preliminary Site Plan

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    Case Study

    Supplemental Carbon Sources

    Wastewater Methanol

    Proprietary Products

    Micro-C (EOS)

    BioCarb DN

    Unicarb DN (Univar)

    Brenntag (Chematron)

    Biodiesel Glycerol Waste Other Industrial Byproducts

    Must Be Low Nitrogen Product

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    Case Study

    Methanol Vs Wastewater

    Owner Requested a Cost Comparison to Use Either Chemical(Methanol) or Wastewater for the Supplemental Carbon Source(Denitrification Use)

    Developed Conceptual Capital and O&M Cost Opinions

    Use of Existing Covered Anaerobic Lagoon

    Estimated a 2 to 3 Yr Simple Payback For Wastewater

    O&M Costs Included Costs for Chemical, Biogas Loss, and Power

    Option Capital Cost, $ Annual O&M Cost, $

    Methanol 600,000 530,000

    Wastewater 1,300,000 230,000

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    Case Study

    Circular Vs Square Process Basins Owner Requested a Cost Comparison to Construct Four

    Circular or Rectangular Basins (common wall). Complete Preliminary Structural Design

    Received Construction Costs from a Contractor

    Four Circular Basins $4.3 Million Four Square Basins $5.7 Million

    Savings For Circular Basins $1.4 Million

    Costs Did Not Include:

    Excavation and Backfill

    Permits

    Taxes

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    Case Study

    Water Reuse Considerations

    Project will Include Effluent Water Reuse. Beef Plant Use

    WWTF Use

    Irrigation (Future)

    Chlorinate Beef Plant and WWTF Reuse Water

    Beef Plant Uses

    Non-Contact Condenser Water

    Livestock Pens Washdown Inedible Clean-Up Water

    Slaughter & Fab Clean-Up Water (Future???)

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    Questions