AA BBaattttllee ttoo BBee tthhee BBeesstt:: AA CCoommppaarriissoonn ooff TTwwoo PPoowweerrffuull SSiiddeessttrreeaamm TTrreeaattmmeenntt TTeecchhnnoollooggiieess:: PPoosstt AAeerroobbiicc DDiiggeessttiioonn aanndd AAnnaammmmooxx David Oerke/CH2M Tom Johnson/CH2M Bruce Johnson/CH2M Heidi Bauer/CH2M Steve Graziano/CH2M 2016 Vail Operator Training Seminar What are PAD & Anammox? • Sidestream Treatment Technologies • Reduction of nitrogen • No supplemental carbon or alkalinity WEF Webcast 12/9/2009: Sidestream Treatment for Nutrient Removal and Recovery What is Post Aerobic Digestion? Aerobic digestion after anaerobic digestion • Advantages: – Reduction of N without chems. – VSS reduction – Odor reduction – Struvite stabilization • Challenges: – Biological heat – Foam Example Full-Scale PAD Facilities • Spokane County Regional WRF Chemically Enhanced • Denver Metro WRD NTP – 11/16 Primary Treatment • Boulder 75th Street WWTP -10/16 Step Feed Bioreactor Raw Membranes Solids Reduction & Nitrogen Removal Centrifuge Waste Solids Anaerobic Aerobic Digesters Digester Centrate What is Anammox Anaerobic Ammonium Oxidation • Advantages: – Reduction of N without chems. – Lower energy • Challenges: – Slow growth – Competition with nitrite oxidizing bacteria Example Full-Scale Anammox Facility Alexandria Renew Enterprises (AlexRenew) Water Resources Recovery Facility (WRRF) Wett, B., Murthy, S., Takacs, I., Hell, M., Bowden, G., Deur, A., Shaughnessy, M. (2007). Key Parameters for Control of DEMON DeammonificationProcess. Wat. Practice Comparison of Technologies Post Aerobic Digestion Anammox Target Flow Stream Entire anaerobic Dewatering liquors digestion effluent Nitrogen Removal Nitrification/ Partial Nitritation/ Method Denitrification Deammonification - Carbon Input Degradable material Not needed from anaerobic digestion - Aeration Intermittent Intermittent Biomass Used Conventional Specialized Methodology Pro2D2 whole plant simulator: – Baseline – PAD – Anammox CPES cost estimating system Assumptions: mg/L Influent Effluent – 75.7 ML/d (20 mgd) Limitation BOD 250 10 – Aeration Basins: TSS 240 10 • 5-stage Bardenpho VSS 192 • 8.5 day SRT TKN 39 – Biosolids facilities: NH3 30 1 • 24/7 operation TN 39 5.0 • Disposal via land TP 6 1.0 application Baseline PFD -No Sidestream Treatment PRIMARY RAW INFLUENT SCREENING AND CLARIFIERS AERATION BASINS SECONDARY FILTRATION PUMP STATION GRIT REMOVAL CLARIFIERS PLANT An- aerobic Anoxic Aerobic Anoxic Aerobic EFFLUENT Recycle RAS S A W GRAVITY BELT GRAVITY THICKENER sh THICKENER wa k c GraSvuitpye Trnhaictaknetner T ATE ThWickAeSned ADNIGAEESRTOIOBINC Ba BELPTR FEISLSTER BR GT L FI BIOSOLIDS Thickened Primary Solids e at Filtr Post Aerobic Digestion PFD PRIMARY RAW INFLUENT SCREENING AND CLARIFIERS AERATION BASINS SECONDARY FILTRATION PUMP STATION GRIT REMOVAL CLARIFIERS PLANT An- aerobic Anoxic Aerobic Anoxic Aerobic EFFLUENT Recycle RAS S A W GRAVITY BELT GRAVITY THICKENER sh THICKENER wa k GraSvuitpye Trnhaictaknenter T ATE ThWickAeSned ADNIGAEESRTOIOBINC PODSIGT EASETRIOONBIC Bac BELPTR FEISLSTER BR GT L FI BIOSOLIDS Thickened Primary Solids e at Filtr
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