Anaerobic%20Digestion%20and%20Biogas - PowerPoint PPT Presentation

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Anaerobic%20Digestion%20and%20Biogas

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Anaerobic Digestion and Biogas Terminology and designs Total Solids, Volatile Solids Total Solids (TS)= Dry weight of substrate Volatile Solids (VS)= Combustible ... – PowerPoint PPT presentation

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Title: Anaerobic%20Digestion%20and%20Biogas


1
Anaerobic Digestion and Biogas
  • Terminology and designs

2
Total Solids, Volatile Solids
  • Total Solids (TS) Dry weight of substrate
  • Volatile Solids (VS) Combustible proportion
    of TS, organic matter
  • Non-volatile Solids (Ash) Minerals
    etc. left over from combustion

3
Total Solids, Volatile Solids
Total Solids
Ash
4
COD/BOD
  • Chemical/Biochemical Oxygen Demand
  • Measures amount of oxygen required to degrade a
    substrate
  • Used widely in aerobic water treatment
  • Characterizes wastewaters and organic feedstocks
  • Estimates energy content of substrate

5
BMP
  • Biochemical Methane Potential Assay
  • Developed as correlative test of BOD in anaerobic
    systems
  • Realistic measure of total methane potential of a
    feestock
  • Can determine non-biodegradable materials in
    feedstock

6
Organic loading rate
  • Rate at which feedstock is fed to the digester
    (i.e. g VS / L reactor)
  • Varies by feedstock, reactor type, temperature,
    etc.
  • Too low too large of reactor
  • Too high overload reactor, acidification

7
Hydraulic Retention Time
  • How long substrate remains in active volume (i.e.
    turnover rate)
  • Optimized for higher biogas/ reactor volume ratio
  • Too high Unnecessarily large reactor
  • Too low Reduced biogas output, washout microbes

8
Temperature
  • Anaerobic metabolism much more sensitive to
    temperature than aerobic
  • Methanogens more affected than acidogens
  • Leads to unbalanced pH at low temps.
  • Loading rate reduced at low temps.

9
Mesophilic vs. Thermophilic
  • Temperature classes for microbes in digester
  • Mesophilic (30-40C), Thermophilic (50-60C)
  • Different microbial communities operate at each
    temp. class
  • Most digesters operate at mesophilic

10
pH
  • Very important parameter
  • Optimum 7.0, acceptable 6.0-8.0
  • Methanogens cannot function at low pH.
  • Ammonia toxicity above 8.0
  • Slow recovery after sustained drop in pH.

11
Different digester types
  • Batch vs. Continuous
  • Two phase
  • CSTR
  • UASB
  • Fixed-film

12
Batch vs. continuously fed
  • Batch Digester loaded once, emptied once fully
    degraded
  • Continuously fed Digester regularly loaded
    (usually daily), effluent produced at each loading

13
Two phase digestion
  • Single phase- all in one reactor
  • Two phase- acidogenesis and methanogenesis
    separated
  • Benefits
  • Increased over-all efficiency (short HRT of
    acidogenic reactor)
  • More pH control of methanogenic reactor

14
Two phase digestion
15
CSTR
  • Continuously-Stirred Tank Reactor
  • Simple but effective design

16
UASB
  • Up-flow Anaerobic Sludge Blanket
  • Frequently used for sewage
    wastewater

17
Fixed Film Reactor
  • Increased substrate-bacteria contact
  • Utilizes biofilms
  • Short HRT
  • Decreased size
  • Used as DRU

18
Digesters in developing nations
Small scale digester, rural India
Bag digester, Costa Rica
19
Digesters in agriculture
Covered Lagoon, Tulare, CA
Corn sillage digester, Neumunster, Germany
20
Digesters in industrial settings
Lübek mechanical biological treatment plant,
Germany
Mechanical biological treatment plant, Tel Aviv,
Israel
21
Digesters as architectural features?
Appleton Wastewater Treatment Plant, Appleton,
Wisconsin
Reading Sewage Treatment Works, Reading, United
Kingdom
22
Questions?
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