WWW-YES-2011 France Anaerobic Co-digestion of Brown Water and Food - - PowerPoint PPT Presentation

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WWW-YES-2011 France Anaerobic Co-digestion of Brown Water and Food - - PowerPoint PPT Presentation

WWW-YES-2011 France Anaerobic Co-digestion of Brown Water and Food Waste for Energy Recovery Presented by: Lim Jun Wei Supervisor: A/Prof. Wang Jing-Yuan Nanyang Technological University, Singapore http://www3.ntu.edu.sg/r3c/ 06 10 June,


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WWW-YES-2011 France

Anaerobic Co-digestion of Brown Water and Food Waste for Energy Recovery

Presented by: Lim Jun Wei Supervisor: A/Prof. Wang Jing-Yuan Nanyang Technological University, Singapore http://www3.ntu.edu.sg/r3c/ 06 – 10 June, 2011

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Housing Development Board (HDB) Flats

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Residues and Resource Reclamation Centre (R3C) Core Capabilities

  • Waste to Materials

– Converting wastes into new and useful materials (e.g., plastic waste into biodegradable PHA polymer, incineration bottom ash into stabilized carbonated ash product for high value usage, etc.)

  • Waste to Energy

– Harnessing energy from urban biomass, sewage sludge, agricultural residues, micro-algae, etc.

  • Contaminated Site Remediation

– Develop solutions and technologies for remediating contaminated sites Established in May 2009 to spearhead research efforts in developing sustainable waste management technologies

Plastic waste to PHA Ashes to construction material Rooftop microalgae cultivation for biofuel production Food waste plant for biogas production

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Waste is not waste

  • Waste is a misplaced resource
  • Waste residues can be converted into reusable/new materials,

energy, and other products with value

  • Natural resources are limited and depleted
  • Waste can be potential sources for resource recovery
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Issues of Current Waste Management

  • We have not used resources efficiently
  • The centralized waste management approach is energy-consuming;

it was ok but not for the future

  • Liquid waste: activated sludge process (water flushing + aeration +

nitrification and de-nitrification + sludge dewatering + …)

  • Solid waste: collection and transportation (energy consuming) +

emissions from incineration and landfilling (land contamination)

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CRP Project CRP Project: Communities as Renewable Resource Recovery Centers

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Kitchen basin Separation toilet I + II Garbage grinder Kitchen waste Storage tank Yellow water Storage tank Brown water Storage tank Kitchen waste Sewer system Separation toilet + Storage tank Wash basin + Garbage grinder

Separation of Brown Water, Yellow Water, and Kitchen Waste

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CRP Project CRP Project: Communities as Renewable Resource Recovery Centers

  • 300 residents / HDB block
  • 21 kg VS
  • 43 kg COD
  • 65% VS removal
  • 10 m3 methane
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Research Objectives and Scopes

  • To develop a three-phase AD system to optimize the production of

methane from the co-digestion of Food Waste and Brown Water

  • Partial-aerobic hydrolysis reactor, an anaerobic acetogenic UASB reactor

and a methanogenic UASB reactor Brown water Brown water Anaerobic co Anaerobic co‐ ‐digestion digestion

  • CH

CH

4 4

production potential production potential

  • Key variables/parameters

Key variables/parameters

  • Lab

Lab‐ ‐scale test scale test

  • Process optimization

Process optimization

Biogas Biogas Food waste Food waste +

Sept – Dec 2010 Sept – Dec 2010 Jan – May 2011 Jan – May 2011 Jun 2011 Jun 2011 Jun’11 – May’12 Jun’11 – May’12 2014 2014

  • 3 Modules
  • Literature Review
  • Preliminary Study
  • 3 Modules
  • Literature Review
  • Preliminary Study – Batch,

Methane Potential Tests WWW-YES 2011 France

  • Literature Review
  • Continuous, three-phase AD systems
  • Enhance hydrolysis
  • Optimizing substrates of methanogens

Qualifying Exam Further studies

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Four Steps in Anaerobic Digestion

Particulate organic material Particulate organic material

Proteins Proteins Carbohydrates Carbohydrates Lipids Lipids Amino Acids Sugars Amino Acids Sugars Fatty Acids Fatty Acids VFAs, alcohols, lactate, H2 , CO2 , NH3 /NH4

+, H2

S VFAs, alcohols, lactate, H2 , CO2 , NH3 /NH4

+, H2

S Acetate Acetate Hydrogen Hydrogen Methane Methane

  • 1. Hydrolysis
  • 2. Acidogenesis
  • 3. Acetogenesis
  • 4. Aceticlastic

methanogenesis Hydrogenotrophic methanogenesis Adapted from Gujer and Zehnder (1983)

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Batch Study on Anaerobic Co-digestion of Brown Water and Food Waste

Substrate(s) Organic Loading (g VS/L) F/I ratio Brown Water 0.3, 0.5, 1.0, 2.5 0.12, 0.20, 0.40, 1.0 Food Waste 0.3, 0.5, 1.0, 2.5 0.12, 0.20, 0.40, 1.0 Brown Water + Food Waste 1.0, 1.0, 1.0, 2.0 0.40, 0.40, 0.40, 0.80 Seed Sludge = 20% (v/v) Working Volume = 70mL BW:FW mixing ratio (in terms of VS added) = 1:1, 3:7, 7:3, 1:1

Experimental Design

1 2 3

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Materials and Methodologies

1. Collection and treatment of samples 2. Sample Preparation 3. Measuring gas production 4. Analytical Methods

1

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Materials and Methodologies

1. Collection and treatment of samples 2. Sample Preparation 3. Measuring gas production 4. Analytical Methods

Inoculum Substrate X 10 sets

Working Vol.= 70 mL

Mix Well Prepare 1 L mixture

Conditions: Batch –30 days Anaerobic 35°C Continuous mixing

Tap Water

  • Analytical Tests (every 7 days/ at the end of study)
  • pH
  • TS, VS
  • Biogas Composition – %CO2, %CH4
  • COD
  • VFA

2 3 4

Intermittent pressure release method

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Results (Biogas Yield)

Co-Digestion Co-Digestion 1gVS/L substrates 1gVS/L substrates Brown Water Brown Water Food Waste Food Waste

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Results (pH)

Brown Water Brown Water Food Waste Food Waste Co-Digestion Co-Digestion

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Results (Total VFA)

Brown Water Brown Water Food Waste Food Waste Co‐Digestion Co‐Digestion

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Results (Individual VFA)

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Conclusions on Batch Study

Brown water / Food waste Tests

  • At least 90% of final biogas yield & VS reductions achieved in 21 days
  • Methane content: 55 – 78%
  • Biogas production potential of BW > FW
  • F/I of 0.4 – 1.0

Co-Digestion Tests

  • Varying mixing ratio has little effect on biogas yields
  • Acetic acid accumulation towards the end of digestion period
  • Requires longer degradation time
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Future Work

Synergistic relationship between BW & FW in co-digestion Continuous system Phase separation

  • Reduce HRT in each phase
  • Minimize VFA accumulation effects

Single-phase Fed-batch Two-phase Continuous

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Acknowledgements

  • Gujer, W., Zehnder, A.J.B. 1983. Conversion processes in anaerobic digestion.

Wat Sci Tech 15(8-9), 127-167

  • National Research Foundation of Singapore (NRF-CRP-2009-02)
  • National Environment Agency, Jurong Town Corporation, and Housing

Development Board (Singapore)

  • Lionapex, SembCorp, and Keppel (Singapore)
  • Technical University of Hamburg and Harborg (Germany)
  • National Chung Kung University (Taiwan)
  • Nanyang Technological University (Singapore)
  • R3C-NEWRI
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