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PD-Sw205w 1 1 FOSNRS 2: Passive, 2-Stage Biofilter Treatment Systems for Reduction of Nitrogen from OWS – Pilot Study Results April 7, 2014 Josefin Hirst,

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Presentation on theme: "PD-Sw205w 1 1 FOSNRS 2: Passive, 2-Stage Biofilter Treatment Systems for Reduction of Nitrogen from OWS – Pilot Study Results April 7, 2014 Josefin Hirst,"— Presentation transcript:

1 PD-Sw205w 1 1 FOSNRS 2: Passive, 2-Stage Biofilter Treatment Systems for Reduction of Nitrogen from OWS – Pilot Study Results April 7, 2014 Josefin Hirst, P.E. The Florida Onsite Sewage Nitrogen Reduction Strategies (FOSNRS) Project SSSA Onsite Wastewater Conference April 7-8, 2014 Hazen and Sawyer, P.C.

2 PD-Sw205w 2 Presentation overview ■FOSNRS Task A: Nitrogen treatment and reduction options for Florida ■Pilot test results ■Summary ■Questions and answers

3 PD-Sw205w 3 3 FOSNRS Task A: Nitrogen treatment and reduction options for Florida

4 PD-Sw205w 4 Review of biological nitrogen reduction for onsite wastewater treatment Primary Treatment Mineralization of organic N to ammonia (NH 4) Nitrification Ammonia oxidized to nitrate (NO 3 ) by nitrifying bacteria, requires oxygen Denitrification Nitrate converted to N 2 gas by denitrifying bacteria in anoxic environment; requires supply of electron donor Dispersal Effluent discharge to the soil or landscape for final treatment

5 PD-Sw205w 5 What are “Passive” nitrogen reduction systems (PNRS)? ■Most current N-reducing onsite systems are mechanical treatment units, with pumps, blowers, controls ■Passive definition for this project: Passive nitrogen reduction systems (PNRS) are OSTDS that reduce effluent N using reactive media for denitrification and a single liquid pump, if necessary. ■Earlier work showed feasibility of bench-scale “passive” two stage biofiltration concepts (Smith et. al., 2008) Treatment Media Effluent TN (mg/L) TN Reduction (%) Zeolite & Sulfur Media2.297 Expanded Clay & Sulfur2.696.2

6 PD-Sw205w 6 Task A was designed to further the concepts developed in previous work ■Developed detailed performance data for passive biofiltration designs with various media configurations ■Produced scalable design criteria from pilot scale biofilters for subsequent full-scale testing ■Evaluated single pass and recirculating stage 1 biofilters ■Evaluated twenty-two biofilters consisting of nine unsaturated Stage 1 biofilters, nine saturated Stage 2 biofilters, and four vertically stacked biofilter designs.

7 PD-Sw205w 7 A unique pilot facility was constructed at UF research center ■University of Florida, Institute for Food & Agricultural Sciences (IFAS) ■475 acres of land in SE Hillsborough County ■Facility conducts agricultural research & trials for vegetables, fruit and ornamental plants ■Experts in soil and water science onsite Source: http://gcrec.ifas.ufl.edu/

8 PD-Sw205w 8 Test facility included numerous treatment trains ■All used two-stage biofilters: ●Stage 1 Nitrification ●Stage 2 Denitrification ■Stage 1 unsaturated filters included 2 media layers and evaluated 15” and 30” media depths ■We also evaluated single pass and recirculating stage 1 biofilters ■For denitrification, we evaluated both lignocellulosic and sulfur denitrification biofilters

9 PD-Sw205w 9 Various nitrification media were studied Zeo-Pure clinoptilolite Expanded polystyrene Examples of Stage 1 Media Expanded clay Torpedo sand

10 PD-Sw205w 10 Various denitrification media were also studied Elemental Sulfur Lignocellulosics Examples of Stage 2 Media Oyster shell (alkalinity amendment)

11 PD-Sw205w 11 PNRS test facility construction Setting up tanks Mixing Media Batches Gravel Underdrain

12 PD-Sw205w 12 Placing media in tanks

13 PD-Sw205w 13 Two stage single pass biofilters Stage 1 HLR 3 gal/d-ft 2 Stage 2 HLR 5.6 gal/d-ft 2

14 PD-Sw205w 14 We tested five trains of two-stage single pass treatment units

15 PD-Sw205w 15 Two-stage single pass biofilters Stage 1 Unsaturated Biofilters - Nitrification Stage 2 Saturated Upflow Biofilters - Denitrification

16 PD-Sw205w 16 Stage 1 recirculating biofilters schematic Nitrified Effluent Holding Tank Stage 1 HLR 3 gal/d-ft 2 Recycle Ratio 3:1 Stage 1

17 PD-Sw205w 17 Horizontal stage 2 biofilters schematic Peristaltic Pump Sample Ports Nitrified Effluent Stage 2 HLR 10 gal/d-ft 2

18 PD-Sw205w 18 Four recirculating stage 1 trains were followed by four stage 2 horizontal biofilters

19 PD-Sw205w 19 Stage 1 recirculating biofilters & Stage 2 horizontal saturated biofilters Stage 2 Saturated Biofilters - Denitrification Stage 1 Unsaturated Biofilters - Nitrification Pump Tank Nitrified Effluent Pump Tank

20 PD-Sw205w 20 PD-Sw205w 20 Pilot test results

21 PD-Sw205w 21 PNRS pilot testing influent STE quality cBOD 5 TSSTNTKNNH 3 -N Total Alkalinity Septic tank effluent (STE) n10 9 99 mean66.890.955.555.846.3332 std. dev.27.0136.119.918.819.187 min221530 20210 max9446780 67430

22 PD-Sw205w 22 Stage 1 nitrification biofilters mean effluent values BiofiltercBOD 5 TSSTNTKNNH 3 -N(NO 3 +NO 2 ) Single Pass XCLAY – 15”2.01.244.73.50.51041.2 XCLAY – 30”2.01.542.53.40.41739.1 CLINO – 15”2.02.241.03.10.01237.9 CLINO – 30”2.01.344.53.30.02041.2 Recirculating SAND – 30”2.24.030.82.90.25528.0 XCLAY – 30”2.02.234.52.40.01532.1 CLINO – 15”2.22.335.32.60.01032.7 CLINO – 30”2.02.533.04.00.01029.0

23 PD-Sw205w 23 Stage 1 single pass biofilters nitrogen time series Single Pass Expanded Clay: 30 inch depthSingle Pass Clinoptilolite: 30 inch depth CLINO – 30”XCLAY – 30”

24 PD-Sw205w 24 Recirculating Expanded Clay: 30 inch depth Stage 1 recirculating biofilters nitrogen time series CLINO – 30”XCLAY – 30” Recirculating Clinoptilolite: 30 inch depth

25 PD-Sw205w 25 Stage 1 nitrification biofilters effluent nitrogen box and whisker plots XCLAY-15” XCLAY-30” CLINO-15” CLINO-30” XCLAY-30” SAND-30” CLINO-15” CLINO-30” XCLAY-15” XCLAY-30” CLINO-15” CLINO-30” XCLAY-30” SAND-30” CLINO-15” CLINO-30” Single PassRecirculatingSingle Pass Recirculating Ammonia Nitrogen, mg N/L Nitrate & Nitrite Nitrogen, mg N/L

26 PD-Sw205w 26 Stage 2 denitrification biofilters mean effluent values BiofilterC-BOD 5 TSSTNTKNNH 3 -N(NO 3 +NO 2 ) Upflow SULFUR-30%2.02.81.31.20.320.075 LIGNO-50%61.01.58.32.20.876.18 SULFUR-80%6.06.22.6 1.140.047 LIGNO-25%2.03.017.33.10.6214.2 LIGNO-30%4.57.55.95.64.710.22 Horizontal SULFUR-80%13.31.52.52.41.350.11 SULFUR-30%8.53.51.6 0.580.035 LIGNO-50%89.513.010.0 0.270.020 GLYCEROL102.53.8 3.120.07

27 PD-Sw205w 27 Stage 2 upflow single pass biofilters nitrogen time series SULFUR-80% LIGNO-50%

28 PD-Sw205w 28 Stage 2 horizontal biofilters nitrogen time series SULFUR-80%LIGNO-50%

29 PD-Sw205w 29 Stage 2 denitrification biofilters effluent nitrogen box and whisker plots Mean = 14.2 SULFUR-30% LIGNO-50% SULFUR-80% LIGNO-25% LIGNO-30% SULFUR-30% SULFUR-80% LIGNO-50% GLYCEROL SULFUR-30% LIGNO-50% SULFUR-80% LIGNO-25% LIGNO-30% SULFUR-30% SULFUR-80% LIGNO-50% GLYCEROL Upflow Horizontal Upflow Horizontal Nitrate & Nitrite Nitrogen, mg N/L Total Nitrogen, mg N/L

30 PD-Sw205w 30 Single pass systems total nitrogen removal SULFURLIGNOCELLULOSIC

31 PD-Sw205w 31 Recirculating systems total nitrogen removal SULFURLIGNOCELLULOSIC

32 PD-Sw205w 32 Vertical sampler profile in Upflow biofilters lignocellulosic issues

33 PD-Sw205w 33 Lignocellulosic biofilters hydraulic retention time issues

34 PD-Sw205w 34 Solute profile in sulfur upflow biofilter sulfate production vs nitrate reduction

35 PD-Sw205w 35 Single pass vs recirculating biofilters: sulfate

36 PD-Sw205w 36 Lessons learned from pilot test ■Encouraging results from pilot PNRS; several system configurations capable of > 95% N reduction ■Sulfate production vs nitrate reduction ■Highly reactive elemental sulfur media ■Lignocellulosic retention time issues ■Recommended evaluation of combination lignocellulosic and elemental sulfur denitrification systems for full-scale treatment units

37 PD-Sw205w 37 PD-Sw205w 37 Questions? Josefin Edeback-Hirst, P.E. Hazen and Sawyer, P.C. 10002 Princess Palm Avenue, Suite 200 Tampa, FL 33619 jhirst@hazenandsawyer.com


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