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In Integrated ed Ac AcoD oD system em of of the the or organic - PowerPoint PPT Presentation

In Integrated ed Ac AcoD oD system em of of the the or organic nic fr fractio tion of of MSW and MSW and se sewage sl sludg udge: e: Case Case study udy A. Piasentin 1 , L. Girotto 1 , G. Moretto 2 , F. Ardolino 3 & F. Cecchi* *Innoven


  1. In Integrated ed Ac AcoD oD system em of of the the or organic nic fr fractio tion of of MSW and MSW and se sewage sl sludg udge: e: Case Case study udy A. Piasentin 1 , L. Girotto 1 , G. Moretto 2 , F. Ardolino 3 & F. Cecchi* *Innoven srl, Spinoff University of Verona 1 Alto Trevigiano Servizi S.r.l., Montebelluna (TV) 2 Department of Environmental Sciences, Informatics and Statistics, University Ca’ Foscari of Venice 3 Department of Environmental, Biological and Pharmaceutical Sciences and Technologies, University of Campania “Luigi Vanvitelli”

  2. Naxos 2018 6 th IC ‐ SSWM 13 – 16 June 2018 Contents 1. Introduction AcoD system overview • Feasible routes for OFMSW recovery • AcoD integration within existing WWTPs • 2. Materials and Methods Case study presentation • Mixtures characterization • Steady state conditions operating parameters • Steady state conditions performance parameters • Energy considerations • Preliminary LCA study • 3. Conclusions

  3. Naxos 2018 6 th IC ‐ SSWM 13 – 16 June 2018 ACoD: as territory service was discussed in the 2 th IC ‐ SSWM according to the following schemes TERRITORY Cecchi F., et Al. (1994). Water Science & Technology; Cecchi and Cavinato (2015), Waste Management and Research

  4. Naxos 2018 6 th IC ‐ SSWM 13 – 16 June 2018 Two main objectives for OFMSW recovery and valorisation trough AcoD: 1 Maximisation of energy recovery 2 Maximisation of matter recovery 1 2 The choice is driven by territory diversity and available technologies

  5. Naxos 2018 6 th IC ‐ SSWM 13 – 16 June 2018 Case Study Approach Screw press flowchart Squeezed wet biowaste contains approx. 15 ‐ 20% TS • This approach could favour ACoD with SS in nearby WWTPs •

  6. Naxos 2018 6 th IC ‐ SSWM 13 – 16 June 2018 Case study: full ‐ scale implementation of OFMSW ‐ SS AcoD Treviso WWTP Squeezed OFMSW from door ‐ to ‐ door separate collection ensures high quality organic waste Parameter Mean ± St. Dev. Max Min TS, g/kg 135 ± 52 211.0 33.2 TVS, g/kg 113 ± 44 176.6 24.9 Organic waste recycling in Treviso Province = 85.3% TVS/TS, % 84 ± 3 97 75 (ARPAV, 2017)

  7. Naxos 2018 6 th IC ‐ SSWM 13 – 16 June 2018 Case study: full ‐ scale implementation of OFMSW ‐ SS AcoD Treviso WWTP Treviso (TV) • A.T.S. S.r.l. WWTP

  8. Naxos 2018 6 th IC ‐ SSWM 13 – 16 June 2018 Feedstock mixture characterization Parameter Mean ± St. Dev. Max Min TS, g/kg 33.8 ± 5.3 48.9 19.4 TVS, g/kg 24.9 ± 3.8 34.9 13.8 TVS/TS, % 74 ± 4 88 55 pH 5.4 ± 0.25 5.92 5.08 COD, gCOD/kgTS 811 ± 52 979 693 TKN, gN/kgTS 41.3 ± 6.2 48.9 19.2 P org , gP/kgTS 11.0 ± 3.1 20.0 4.8 Effluent characterization 2000 m 3 anaerobic digester CSTR Parameter Mean ± St. Dev. Max Min TS, g/kg 18 ± 2.7 28.0 13.5 TVS, g/kg 12.1 ± 2.3 19.0 8.0 TVS/TS, % 67 ± 7 88 52 COD, gCOD/kgTS 736 ± 53 906 648 TKN, gN/kgTS 40.0 ± 8.1 49.1 19.1 P org , gP/kgTS 13.7 ± 3.7 27.1 9.1

  9. Naxos 2018 6 th IC ‐ SSWM 13 – 16 June 2018 Steady state conditions operating parameters Hydraulic Retention Time 50 40 30 HRT (d) 20 10 0 300 350 400 450 500 550 600 650 700 Days During steady state conditions an average HRT = 20 days was mantained

  10. Naxos 2018 6 th IC ‐ SSWM 13 – 16 June 2018 Parameters of steady state operating conditions OFMSW flow rate fed to digester 14,0 OFMSW flow rate (m 3 /d) 12,0 9.5 m 3 /d 10,0 8,0 6,0 4,0 2,0 0,0 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 Periods Sludge flow rate fed to digester 140 Sludge flow rate (m 3 /d) 88 m 3 /d 120 100 80 60 40 20 0 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 Periods

  11. Naxos 2018 6 th IC ‐ SSWM 13 – 16 June 2018 Parameters of steady state operating conditions Organic Loading Rate 3,0 Total OLR (kgVS/m 3 d) 2,5 1.8 kgVS/m 3 d 2,0 1,5 1,0 0,5 0,0 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 Periods OFMSW OLR Sludge OLR Average OFMSW OLR = 0.7 kgVS/m 3 d • Average Sludge OLR = 1.1 kgVS/m 3 d • *All results shown are related to steady state conditions and based on an average of 20 days Steady state conditions cover a time period from 22/04/17 to 28/02/18

  12. Naxos 2018 6 th IC ‐ SSWM 13 – 16 June 2018 Steady state conditions performance parameters Biogas production 2500 Biogas production (m 3 /d) 2000 1500 1000 1800 m 3 /d 500 0 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 Periods Biogas main composition 80 1000 65% CH 4 ; 400 ppm H 2 S 75 800 H 2 S (ppm) 70 600 % CH 4 65 400 60 200 55 0 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 Periods Methane percentage Hydrogen Sulfide concentration

  13. Naxos 2018 6 th IC ‐ SSWM 13 – 16 June 2018 Steady state conditions performance parameters Specific Gas Production 0,8 0,7 0,6 SGP (m 3 /kgVSd) 0,5 0,4 0,3 0,2 0,1 0,0 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 Periods Stable SGP was observed with an average value of 0.5 m 3 /kgVSd

  14. Naxos 2018 6 th IC ‐ SSWM 13 – 16 June 2018 Steady state conditions: process stability parameters 10,0 4000 1000 1000 900 900 3500 9,5 Alkalinity (mgCaCO 3 /l) 800 800 + /l) 3000 9,0 700 700 VFA (mgCOD/l) + (mgN ‐ NH 4 2500 600 600 8,5 pH 2000 500 500 8,0 400 400 1500 N ‐ NH 4 300 300 7,5 1000 200 200 7,0 500 100 100 0 0 6,5 0 17 22 27 32 17 22 27 32 Periods Periods Ammonium concentration VFA pH Partial Alkalinity Total Alkalinity Parameter Mean ± St. Dev. Max Min pH 7.4 ± 0.19 7.7 7.1 Steady state conditions were Alk pH6, mgCaCO 3 /l 2015 ± 258 2326 1387 characterized by stable pH, alkalinity, ammonium and VFA Alk pH4, mgCaCO 3 /l 2932 ± 290 3208 2303 concentrations + , mgN ‐ NH 4 + /l N ‐ NH 4 530 ± 84 726 365 VFA, mgCOD/l 58 ± 23 232 0

  15. Naxos 2018 6 th IC ‐ SSWM 13 – 16 June 2018 Energy consumption and recovery Electric energy consumed and produced 10000 100% 9000 90% 8000 80% EE consumed (kWh/d) Energy coverage (%) 7000 70% 6000 60% 5000 50% 4000 40% 3000 30% 2000 20% 1000 10% 0 0% 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 Periods EE consumption Energy coverage Electric energy is autoproduced through a 185 kW el CHP motor • Energy produced accounts for 50% of the total plant energy demand •

  16. Naxos 2018 6 th IC ‐ SSWM 13 – 16 June 2018 Preliminary LCA study Two different LCA scenarios: past scenario VS present scenario Past scenario: OFMSW composting • Data are expressed in t/d

  17. Naxos 2018 6 th IC ‐ SSWM 13 – 16 June 2018 Preliminary LCA study Two different LCA scenarios: past scenario VS present scenario Present scenario: OFMSW pretreatment → AcoD + Composting • Data are expressed in t/d

  18. Naxos 2018 6 th IC ‐ SSWM 13 – 16 June 2018 Preliminary LCA study Delta "Past" scenario "Present" scenario (Present ‐ Past) Specific electrical Electrical Electrical Electrical consumption, Input, t IN /d consumption, Input, t IN /d consumption, consumption, kWh/t IN kWh/d kWh/d kWh/d Composting 69 138 9515 129 8880 ‐ 635 Wastewater line 0.04 180000 6667 180000 6667 0 Recovered EE, Biogas to Recovered Biogas a Recovered EE, Recovered EE, kWh/t Biogas to CHP CHP, t IN /d EE, kWh/d CHP, t IN /d kWh/d kWh/d Recovered EE 1771 ‐ ‐ 1.89 3345 3345 from CHP kWh/d kWh/d kWh/d Total electrical consumption 16182 12202 ‐ 3979 Global Warming Potential of the Italian electrical mix: 0.437 kg CO 2 eq for the production of 1 kWh (from: IPPC 2001 500a, and IEA 2016) Potential avoided GWP: 1739 kg CO 2 eq. per day

  19. Naxos 2018 6 th IC ‐ SSWM 13 – 16 June 2018 Conclusions OFMSW codigestion with SS ensures: Valorisation of organic wastes through energy recovery • Best territorial service for citizens • Simple operational work • Stable operating condition under SSC • Higher revenues • Slight increase in sludge production • High energy savings due to CHP biogas conversion • Undeniable overall convenience in terms of LCA • Applicable to any WWTP with reduced upgrading costs

  20. Naxos 2018 6 th IC ‐ SSWM 13 – 16 June 2018 THANK THANK YO YOU FO FOR YO YOUR ATTENTI TENTION! N!

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