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1 Evaluation of OSS Nitrogen Removal Technologies Regulatory Round Table Review Series March 11, 2014 Lynn Schneider, Washington Department of Health Office of Shellfish and Water Protection
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2 $EPA Nutrient NEP Grant Study Partners
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3 A.Source diversion B.Post-septic tank treatment C.Design of the soil dispersal component (drainfield) Wastewater Nitrogen Management Approaches A B C
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4 Problems: N reduction in OSS is highly variable Limited treatment options Regional environmental and water source affects on N removal not well-known OSS Nitrogen Removal Project Design Nitrogen In Nitrogen Out Biological System Changes Nitrogen from soluble to gaseous
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5 Objectives: Maximize N removal efficiencies Verify performance objective (<20 mg/L TN full test avg.) Expand reliable, affordable options OSS Nitrogen Removal Project Design
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6 Methods: Partner with UW & Ecology to: Use ETV Nutrient Reduction Protocol Develop standards & guidance OSS Nitrogen Removal Project Design
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7 ETV-Nutrient Reduction Protocol Minimum of 12 consecutive months Daily Design loading 480 gpd (100% + 10% of the rated capacity) 6 AM – 9 AM: ~35% of flow 11 AM – 2 PM: ~25% of flow 5 PM – 8 PM: ~40% of flow Stress Testing (effect of home activities) washday loading working parent low-loading power/equipment failure one week vacation
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8 ETV-Nutrient Reduction Protocol Sampling Days: Minimum of 12 monthly samples + additional 38 stress day sampling Total 55 data days
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9 ETV-Nutrient Reduction Protocol Performance Parameters: Total N, NH 3 -N, NOx-N (NO 3 +NO 2 ), Total P, CBOD, COD, TSS/VSS, alkalinity Site Grab for lab: fecal coliform In-situ samples: dissolved oxygen, pH, temperature
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10 Meters & Probes
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11 Snoqualmie WWTP Test Site
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12 Snoqualmie WWTP Test Site w/autosampler locations
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13 O2O2 O2O2 Organic N NH 4 + NO 2 - NO 3 - N 2 Ammonification Nitrification Denitrification (Aerobic) (Anoxic) Two step process: 1) Nitrification - nitrifies NH 4 + to NO 3 - 2) Denitrification - reduces NO 3 - to nitrogen gas Nitrogen Biochemical Transformations Organic N N2N2 Biological System ALKALI O2O2 C C C
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14 Nitrification is a two step process: 1.Utilizing bicarbonate alkalinity, Nitrosomonas bacteria will oxidize ammonia to nitrite by NH 4 + + O 2 + HCO 3 - C 5 H 7 O 2 N + NO 3 - + H 2 O + H 2 CO 3 2.Then Nitrobacter bacteria will oxidize nitrite to nitrate mole for mole by NO2 - + NH 4 + + H 2 CO 3 + HCO 3 - + O 2 + C 5 H 7 O 2 N + H 2 O + NO 3 Nitrogen Biochemical Transformations
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15 Denitrification is a one step process - Note: We used two variations: 1.NO 3 + Woodchips N 2 + OH - + CO 2 + H 2 O 2.NO 3 + BOD from septic tank influent N 2 + OH - + CO 2 + H 2 O Nitrogen Biochemical Transformations
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16 Vegetated Recirculating Gravel Filter (VRGF) 1 8 Nitrification Denitrification
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17 VRGF August 2012 June 2013
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18 VRGF Influent and Effluent Nitrogen Over 12-Month Test Period
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19 VRGF Influent and Effluent Fecal Coliform Over 12-Month Test Period
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20 Parameter unitsInfluentEffluent Total Nmg/L48.6 (9.5)15.1 (1.9) NH 3 -Nmg/L29.3 (5.3)4.1 (1.0) NOx-Nmg/L-9.5 (2.1) Org-Nmg/L-1.6 (0.9) BOD/CBOD*mg/L314 (98)5.6 (1.8) TSSmg/L354 (137)3.2 (2.0) VSSmg/L324 (131)2.9 (1.7) COD/SCOD*mg/L715 (223)21.0 (7.2) Total Phosphorusmg/L5.8 (1.3)3.5 (1.1) Fecal Coliform** CFU/100 mL 8.4E+62.3E+5 Alkalinity as CaCO 3 mg/L231 (36)153 (23) pH 7.4 (0.3)6.8 (0.2) Average Performance for VRGF Over 12-Month Test (68.9% TN Removal) *Effluents, **Geometric mean, ( ) is standard deviation
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21 VRGF Clogging Problem
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22 Enhanced Recirculating Gravel Filter (ERGF) 1 8 (5) Nitrification Denitrification
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23 ERGF July 2012 January 2013
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24 Parameter unitsInfluentEffluent Total Nmg/L48.6 (9.5)8.6 (2.2) NH 3 -Nmg/L29.3 (5.3)6.8 (1.9) NOx-Nmg/L-0.6 (0.6) Org-Nmg/L-1.3 (0.5) BOD/CBOD*mg/L314 (98)8.6 (1.9) TSSmg/L354 (137)5.3 (2.2) VSSmg/L324 (131)4.4 (2.0) COD/SCOD*mg/L715 (223)24.6 (5.7) Total Phosphorusmg/L5.8 (1.3)3.5 (1.4) Fecal Coliform**CFU/100 mL8.4E+64.6E+5 Alkalinity as CaCO 3 mg/L231 (36)203 (27) pH 7.4 (0.3)6.9 (0.2) Average Performance for ERGF Over 12-Month Test (82.3% TN Removal) *Effluents, **Geometric mean, ( ) is standard deviation
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25 ERGF Influent and Effluent Nitrogen Over 12-Month Test Period
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26 ERGF Influent and Effluent Fecal Coliform Over 12-Month Test Period
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27 Recirculating Gravel Filter (RGF) & Woodchip Bed - Two Stage System Nitrification Denitrification 1 6 3 days
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28 RGF & Woodchip Bed August 2012 June 2013
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29 RGF & Woodchip Bed July 2012 June 2013
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30 Parameter unitsInfluentRGF Effluent Average Woodchip Effluent Total Nmg/L48.6 (9.5) 23.9 (5.4)4.0 (3.8) NH 3 -Nmg/L29.3 (5.3) 0.7 (0.4)0.5 (0.5) NOx-Nmg/L- 21 (5.5)2.4 (3.7) Org-Nmg/L- 2.2 (1.2)1.1 (0.3) BOD/CBOD*mg/L314 (97.8) 4.7 (2.6)10.8 (14.1) TSSmg/L354 (137) 10.1 (12.7)2.1 (2.0) VSSmg/L324 (131) 5.8 (5.5)0.9 (2.3) COD/SCOD*mg/L715 (223) 21.6 (5.5)37.6 (20.7) Total Phosphorus mg/L5.8 (1.3) -3.4 (1.9) Fecal Coliform** CFU/100 mL 8.4E+6 1.6E+050.96E+03 Alkalinity as CaCO 3 mg/L231 (36) 84 (28)154 (36.6) pH 7.4 (0.3) 6.8 (0.3)6.6 (0.2) Average Performance for RGF-Woodchip Bed Over 12-Month Test Period *Effluents, **Geometric mean, ( ) is standard deviation (91.8% TN Removal and 960 CFU/100 mL effluent fecal coliform)
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31 Nitrogen Removal in RGF and Woodchip Bed Over 12-Month Test Period
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32 Fecal Coliform Removal in RGF and Woodchip Bed Over 12-Month Test Period
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33 CBOD in RGF and Woodchip Bed Effluents Over 12-Month Test Period
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34 ParameterUnit Vegetated RGF Enhanced RGF RGF/ Woodchip Bed Total Areaft 2 256180221 Treatment Media Depthft3.5 2.0-RGF 2.8-Woodchip Bed Average Effluent TNmg/L15.1 (18.5)8.6 (12.3)4.0 (13.1) Average TN removal%68.882.391.8 Average Effluent CBODmg/L5.6 (8.2)8.6 (11.22)10.8 (28.9) Geometric mean of Effluent Fecal Coliform CFU/100 mL230,000460,000960 Comparison of the 3 Nitrogen Removal Systems ( ) is 95% Percentile
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35 1.Webpage posting the ETV Reports summarizing the results from the 3 systems 2.Provide technical support for Hood Canal On-Site Sewage System Nitrogen Reduction (HCOSSNR) demonstration project 3.Complete RS&Gs for the RGF/Woodchip Bed and the VRGF systems Project Outcomes
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36 UW Civil and Environmental Engineering David Stensel - UWCEE Project Coordinator Michael Brett – UWCEE Project QA Manager Crystal Grinnell – Research Assistant Stephany Wei - Research Assistant Songlin Wang – UWCEE field engineer City of Snoqualmie Wastewater Treatment Plant Tom Holmes - Wastewater Superintendent Lyle Beach - Laboratory Analyst Brian Richardson - Senior Operator Peter Lombardi, Orenco Systems Inc. Dennis Hallahan, Infiltrator Systems Inc. Acknowledgements from Health
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37 To learn more about the project go to www.doh.wa.gov search for Denitrification Lynn Schneider (360) 236 -3379 Lynn.Schneider@DOH.WA.GOV Washington State Department of Health Office of Shellfish and Water Protection
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