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Operational Conditions for Anaerobic Digesters

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Presentation on theme: "Operational Conditions for Anaerobic Digesters"— Presentation transcript:

1 Operational Conditions for Anaerobic Digesters
Quanbao Zhao Washington State University 8/1/2013

2 Operational Conditions
Temperature pH Hydraulic retention time (HRT) Solid retention time (SRT) Toxicants Flow and Mix

3 Temperature

4 Mesophilic condition Medium temperature loving bacteria/archae
Preferred temperature range: 20 and 45 °C (68 and 113, °F) Best performance: 38°C (100 °F) Moderate degradation rate Moderate biogas production rate Moderate heat demand

5 Thermophilic condition
Heat-loving bacteria/archea Preferred temperature: °C (113 - 252 °F) Typical temperature: 55°C (131°F) High degradation rate High biogas production rate High heat demand, ammonia inhibition

6 Phychrophilic condition
Cold-loving bacteria/archae Preferred temperature: 0°C to +25°C (32-68 °F) Low degradation rate Low biogas production rate No heat demand

7 pH

8 pH Optimum pH for the methanogens: 6.5-8.0
Optimum pH for the acid-forming bacteria: Buffering system in the digester: bicarbonate/carbonate, ammonium/ammonia, Phosphate Why pH drops in the digester? Volatile fatty acid accumulation What happens if pH goes higher than 8? Ammonia inhibition

9 Hydraulic retention time

10 Hydraulic retention time (HRT)
HRT means how long the liquid will stay in the reactor before it comes out. HRT=Volume of the reactor/Flow rate of the influent; Unit: day. Proper HRT is important to fully digest the organic materials in the waste. Dairy manure: above 20 days Longer HRT -> Larger reactor volume -> Higher construction cost

11 Solid Retention Time

12 Solid retention time (SRT)
Solid retention time is the average time microbes remain in the digester How to keep a high SRT: Sludge recirculation Reactor design: UASB, ASBR For CSTR, SRT= HRT if no recycle the sludge For CSTR, SRT> HRT if recycle the sludge

13 Toxicants 1 Volatile fatty acids (VFAs) Metals Hydrogen Sulfide (H2S)
Acetic acid, Propionic acid, Butyric acid etc. Inhibit methanogens, could cause the fail Methods for detection: titration, gas chromatography Metals Heavy metals: Copper, Chromium, Cadmium, Nickel et al. Light metals: Aluminum, Potassium, Sodium, Calcium and Magnesium. Hydrogen Sulfide (H2S)

14 Toxicants 2 Ammonia Organic chemicals
Free ammonia is the major problem High pH release free ammonia from ammonium Organic chemicals Long chain fatty acids phenols

15 Flow and Mix Problems: Sand/heavy solids will build up at the bottom Grease/fiber will build up at the top Mixing is a key factor to enhance the kinetics and prevent settling/crusting Remove sand before feeding into the digester


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