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Bioavailable Phosphorus in Advanced Phosphorus Removal Facility Effluent Phase II Study Bo Li, Michael T. Brett Department of Civil and Environmental Engineering,

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Presentation on theme: "Bioavailable Phosphorus in Advanced Phosphorus Removal Facility Effluent Phase II Study Bo Li, Michael T. Brett Department of Civil and Environmental Engineering,"— Presentation transcript:

1 Bioavailable Phosphorus in Advanced Phosphorus Removal Facility Effluent Phase II Study Bo Li, Michael T. Brett Department of Civil and Environmental Engineering, University of Washington, Seattle, Washington 98195, USA; libo@u.washington.edu

2 INTRODUCTION Effluent total phosphorus (TP) concentration 3mg/L 500µg/L 50µg/L 20µg/L 100mg/L 200mg/L 250mg/L!! What is left here??

3 Phosphorus Characterization – Common Operational Categories: Total Phosphorus (TP) Total Reactive Phosphorus (TRP) Soluble Reactive Phosphorus (SRP) etc…. However…. These are all based on chemical analysis… INTRODUCTION

4 Phosphate (PO 4 -3 ) …. Inorganic P Apatite AlPO 4 FePO 4 Recalcitrant P Organic P Polyphosphate Inositol hexakisphophate L-α-phosphatidyl choline phosphoenol pyruvate Definition of Bio-available phosphorus (BAP) Phosphorus can be utilized by algae INTRODUCTION

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7 METHODS PHASE I STUDY – Spokane Region Spokane City Pilot Plant City of Coeur d’Alene Post Falls Liberty Lake Hayden Area Regional Sewer Board Inland Empire Paper Spokane River

8 Previous study on effluent TP vs. BAP% – Spokane City Pilot Plant (Three alum additions + filtration process) PHASE I RESULTS – Effluent TP vs. BAP% A very strong statistical correlation between the effluent TP and BAP% As more chemicals were added, the BAP% in the effluent declined. KEY NOTE KEY NOTE

9 P bioavailability in Spokane Regional WWTP effluents BAP% varied in effluents from different advanced nutrient removal facilities Less than 60% of P in the effluents are bioavailable. BAP% varied in effluents from different advanced nutrient removal facilities Less than 60% of P in the effluents are bioavailable. KEY NOTE KEY NOTE PHASE I RESULTS – Effluent TP vs. BAP%

10 21 P species – inorganic P, organic P, humic substances 75 samples from 17 Plants Treatment Process CategoryPlantsChemical Addition EBPR without chemical addition 3 MBR Processes 2 √ Single stage tertiary 6 √ Dual stage tertiary 6 √ METHODS WERF national *EBPR: Enhanced Biological P removal *MBR: Membrane Biological Reactor

11 Bioavailability of P species: P SpeciesReactivityBioavailability Al-P, Fe-P Apatite DNA, RNA Humic Substances 90% ≈15% WERF national RESULTS – P species Not all P are created equal Can’t estimate Bioavailable P merely based on chemical analysis Not all P are created equal Can’t estimate Bioavailable P merely based on chemical analysis KEY NOTE KEY NOTE

12 Find the best predictor of BAP – TRP vs. BAP RESULTS WERF national RESULTS – Effluent TRP vs. BAP TRP is a conservative measure of BAP! KEY NOTE KEY NOTE *TRP: Total Reactive P

13 BAP% & TP results RESULTS WERF national RESULTS – Effluent TRP vs. BAP Intensive chemical P removal processes were used to achieve low TP concentrations. KEY NOTE KEY NOTE WERF national RESULTS – Effluent BAP% vs. TP

14 CONCLUSIONS PHASE II STUDY – Objective 1 CBODP – Phosphorus associated with Carbonaceous Biochemical Oxygen Demand (CBOD) Assumptions: – CBODP = TP – SRP – k CBODP = k TP-SRP Lake Spokane CE-QUAL-W2 model *SRP: Soluble Reactive P BAP = CBODP*(1-e -kt )

15 CONCLUSIONS PHASE II STUDY– Objective 1  CBODP Decay rate (k CBODP ) Corresponding SourceDecay rate, day -1 Point Sources Liberty Lake WWTP0.0456 Spokane WWTP0.0736 Coeur D‟Alene WWTP0.0792 Post Falls STP0.066 Inland Empire Paper0.0186 Kaiser Aluminum0.1275 Hayden POTW0.0838 Hayden POTW summer discharge (for scenarios)0.0838 AVE0.07 Non-Point Sources Organic matter from Washington Tributaries0.066 Lake Coeur D‟Alene CBOD0.13 AVE0.10 Lake Spokane CE-QUAL-W2 model

16 CONCLUSIONS PHASE II STUDY – Objective 1 Objective 1: Determine dissolved phosphorus mineralization rates Hypothesis: The mineralization rate for the recalcitrant dissolved P for Spokane region WWTP effluents is likely to be different with the original value assumed by current TMDL model. Task: The algal dissolved P uptake experimental design can determine conservative dissolved organic P mineralization rates for any Spokane region effluent type. These mineralization rates can be integrated into the current Long Lake TMDL model.

17 CONCLUSIONS PHASE II STUDY– Objective 1 Objective 1: Determine dissolved phosphorus mineralization rates Experimental Design: Sample P Bioassay Dissolved P analysis (Days 0, 1, 2, 4, 8, 14 and 21) Dissolved P mineralization rate Autoclaved Selenastrum capricornutum Initial concentration:200,000 cells/ml. Incubate for 21 days. Continuous Illumination Temperature: 24 ± 2ºC Shake at 110 rpm.

18 CONCLUSIONS PHASE II STUDY– Objective 1 Objective 1: Determine dissolved phosphorus mineralization rates Experimental Design: Sample P Bioassay Dissolved P analysis (Days 0, 1, 2, 4, 8, 14 and 21) Dissolved P mineralization rate Autoclaved BAP = BAP%*TDP*(1-e -kt ) BAP%, K *TDP: Total Dissolved P

19 CONCLUSIONS PHASE II STUDY– Objective 1 Objective 1: Determine dissolved phosphorus mineralization rates Experimental Design: Sample P Bioassay Dissolved P analysis (Days 0, 1, 2, 4, 8, 14 and 21) Dissolved P mineralization rate Autoclaved BAP% = 75%, k = 1.1 day -1 BAP% = 43%, k = 1.5 day -1

20 CONCLUSIONS PHASE II STUDY– Objective 2 Objective 2: Resolving issues on bioassay methods from the Phase I Spokane BAP study Hypothesis: Ecology and EPA concerned that some of the very low effluent %BAP results we reported were at least partially a result of nutrient co-limitation (e.g., by nitrogen) and/or effluent toxicity. Task: We will conduct experiments to determine whether the low %BAP we have previously determined for Spokane region dischargers is partially an artifact of nutrient colimitation and/or effluent toxicity.

21 CONCLUSIONS PHASE II STUDY– Objective 2 Objective 2: Resolving issues on bioassay methods from the Phase I Spokane BAP study Experimental Design: Sample Bioavailability of P in the effluents amended with all of other nutrients P Bioassay amended with all of other nutrients + P

22 CONCLUSIONS PHASE II STUDY– Objective 3 Objective 3: The role of Humics in dissolved nutrient recalcitrance Hypothesis: It is hypothesized that both recalcitrant dissolved organic nitrogen (rDON) and dissolved organic P (rDOP) will be associated with large molecular weight size fractions, (> 10 kilo Daltons; kDa). Task: We will use ultra-filtration to size fractionate the "dissolved" or colloidal portion of effluents with a high proportion rDON and rDOP to determine whether nutrient recalcitrance is associated with a high proportion of nutrients in the large molecular weight size range associated with colloidal humic substances (i.e., > 10 kDa).

23 CONCLUSIONS PHASE II STUDY– Objective 3 Objective 3: Comparison of the humic hypothesis for rDON and rDOP Experimental Design: Sample Ultrafiltration (3, 10, 30 and 100 kDa) P and N analysis DON and DOP concentration in each size range Filtrate

24 CONCLUSIONS PHASE II STUDY– Objective 3 Objective 3: Comparison of the humic hypothesis for rDON and rDOP Experimental Design: Sample Ultrafiltration (3, 10, 30 and 100 kDa) P and N analysis DON and DOP concentration in each size range Filtrate Problem: 3kDa membrane might filter out some fractions of PO 4

25 Water Environment Research Foundation (WERF) Nutrient Challenge Program Spokane River Stewardship Partners (SRSP) ACKNOWLEDGEMENTS

26 QUESTIONS?


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