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Effect of total solids content on anaerobic co-digestion of pig - - PowerPoint PPT Presentation

Effect of total solids content on anaerobic co-digestion of pig manure and food waste under mesophilic condition Z. Wang, S. Wang, Y. Jiang, Z. Hu, X. Zhan Civil Engineering, College of Engineering & Informatics, National University of


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Effect of total solids content on anaerobic co-digestion of pig manure and food waste under mesophilic condition

  • Z. Wang, S. Wang, Y. Jiang, Z. Hu, X. Zhan

Civil Engineering, College of Engineering & Informatics, National University of Ireland, Galway

Xinmin.zhan@nuigalway.ie

June, 2019

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Fertili zer Digest ate Biog as Biometha ne Electri city Heatin g Gas grid Vehicle fuel Upgrade  Renewable and eco-friendly technology — Anaerobic digestion Feed

Background

Anaero bic digeste r Agricultur e

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Feedstocks

Agricultu ral wastes Municip al bio- wastes Energy crops Industri al wastes and wastewa ter

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 Wet/Liquid AD (with TS < 10%)

 Wet and dry anaerobic digestion  reducing digester size/volume.

 decreasing energy

consumption for heating.

 avoiding high cost of liquid

digestate management.

 producing methane-rich biogas.  low consumption of water.

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Background

 Dry AD(with TS ≥ 15%)

Conventional AD: usually operated with TS 2–6%*

  • High energy input requirement
  • High cost for digestate post-treatment

Deficiencies Increased TS

  • An alternative to solve these problems.
  • More attractive.

A d v a n t a g e s

* Liu et al, 2016

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Background

 Challenges for dry AD

Dry AD system Reduced moisture

  • Mass

transfer limitation

  • High VFA

concentration

  • High

ammonia concentratio n

  • Long start-up time
  • Limited methane production rate
  • Low VS removal efficiency

Inhibitory factors Imbalance between acidogenesis and methanogenesis Suppressed microbial activity Intermediates accumulation Impact

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 Total solids content: 5%, 10%, 15%, 20%.  Substrates: Pig manure and food waste ( PM/FW ratio of 25:25* by VS content ).  Reactors: R1~R12, 2 L Tap bottles (in triplicate at each TS content, 12 totally).  Inoculum: Dewatered anaerobic sludge from a local municipal WWTP.  Condition: Temperature 37.0 ℃; Shaken once by hand every day.

Schematic diagram of anaerobic reactors

CH4 、 CO2 Outlet Mixture substrates Thermometer Constant temperature incubator 37.0 ℃

 Experimental setup

Methods and material

*Jiang et al, 2018

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No. Characteristics Solid fraction

  • f pig manure

Food waste Seed sludge 1 pH 7.57±0.03 4.93±0.02 7.77±0.03 2 Moisture content (MC, %) 77.1±0.01 59.5±0.38 80.0±0.05 3 Total solids (TS, %) 22.90±0.01 40.52±0.38 20.02±0.05 4 Volatile solids (VS, %) 17.93±0.01 39.96±0.30 13.76±0.08 5 VS/TS (%) 78.4 96.2 68.7 6 SCOD (g/L) 40.9 126.8 7.1 7 TCOD (g/L) 197.6 271.4 190.1 8 Total volatile fatty acid (VFA, mg Acetate/L) 24 035.9 8794.0 9 Total ammonia nitrogen (TAN, mg/L) 4156.3 240.2 1793.3 10 Free ammonia nitrogen calculated (FAN, mg/L) 85.76 0.01 57.94

Physicochemical properties of PM and FW and seed sludge

 Characteristics of Substrates

Methods and material

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Biomethane production

  • 20%-TS digesters obtained a relatively-low SMY
  • Prolonged lag phase with the increase of TS, especially with 20%-TS
  • Two peaks occurred during digestion

Results and discussion

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Optimum pH: 6.8~7.2

  • A lower pH value around 7.5 occurred in R4-20% before day 25.
  • pH values were all within the acceptable range of 6.5-8.5.
  • More time was needed for R4-20% before reaching a constant TS

4 Results and discussion

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TAN concentration

  • The release of ammonia proceeded rapidly at the beginning

according to the steep increment tendency

  • At fjsrt several days, FAN increased distinctly due to the rapid

release of ammonia.

  • The inhibition of free ammonia on methanogens occurred in TS-

15% and TS-20% digesters (FAN up to 400 mg-N/L)

Results and discussion

FA N

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VFA concentrations

Results and discussion

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Microbial community analysis

At genus level At the phylum level

Results and discussion

  • Phyla Firmicutes (43.9-49.1%), Proteobacteria (18.6-39.1%), Chloroflexi (3.3-

8.8%) and Planctomycetes (1.9-6.8%) dominated in dry digesters.

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  • No big change in wet AD, Methanothrix was dominant.
  • On day14, microbial community in dry AD is similar with wet AD, and shifting
  • ccurred in dry AD with the incubation time.
  • Methanosarcina was predominant in dry AD, followed by Methanosphaerula and

Methanoculleus.

Results and discussion

At genus level

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Methanogenic pathways

Results and discussion

Wet digestion Dry digestion

  • Hydrogenotrophic methanogenesis gradually increased along

with the incubation time in dry AD.

  • The dominance of Methanosarcina, Methanosphaerula and

Methanoculleus might be responsible for the enhanced resistance capacity in dry AD.

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Conclusion

 20%-TS digesters obtained a relatively-low SMY, and prolonged lag phase.

 Hydrogenotrophic methanogenesis gradually increased and was dominant in the dry AD process.

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Thank you!

Thank to Science Foundation Ireland for financially supporting our research