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Lecture - 3
Analysis of factors affecting biogas
yield
Factors
• Total solids content
• pH
• Temperature
• C/N ratio
• Retention time
• Uniform Feeding & Type
• Loading rate
• Seeding
• Mixing / Agitation
• Toxicity
• Pressure - low
• Design of the plant
Total Solids Content
pH
• Acetate and fatty acids : lower the pH of digester liquor
- ion bicarbonate equilibria of the carbon dioxide in the digester exert
substantial resistance to pH change
- buffer capacity or buffer intensity : quantified by the amount of
strong acid (or base) added to the solution in order to bring about a
change in pH
• Presence of bicarbonate helps prevent : low pH
pH = 6.3 + log[HCO3/dissolved CO2]
Temperature
• Cryophiles (Psychrophiles)
- Occupies the area of cryophilic digestive regime
- 12°C and 24°C
• Mesophiles
- Occupies the area of mesophilic digestive regime
- 22°C and 40°C
• Thermophiles
- Occupies the area of thermophilic digestive regime
- 50°C and 60°C
Temperature
Rate of reaction doubles for every 10°C rise in
temperature up to an optimum and then
declines rapidly
C/N ratio
• Carbon & Nitrogen : nutrients for efficient anaerobic digestion
• Carbon : energy source
• Nitrogen: building the cell structures
• C:N ratio = 25-30:1
• If N concentration is too high (>1,700 mg/l of NH4-N)
• pH is high
- Growth of bacteria is inhibited due to toxicity caused by
high levels of (uncharged) ammonia
• Methanogens : adapt to 5,000 - 7,000 mg/l of NH4 - N given
the pre -requisite that the uncharged ammonia (NH3
controlled by pH) level does not exceed 200 - 300 mg/l
Retention time
• Average time spent by the input slurry inside the digester
before it come out
• 20 – 120 days – depends on design & operating temperature
• In India : 40 -50 days
• Cold climates : 100 days
LR = k (TS / HRT)
k = 7
Loading Rate
• Waste material fed / unit volume of digester capacity
• Gas production : m3 / kg of volatile solids
• 1 kg of cow dung – 0.04 m3 of biogas
• Based on gas requirement
• Uniform feeding
• Under feeding & Over feeding
Seeding
• Introduction of enriched anaerobic bacteria
- for start up
• Anaerobic bacteria proceeds
- acid forming bacteria : abundant
- methane forming bacteria : lesser
• Improper mix of feedstock : change in pH
- excessive formation of volatile fatty acids
CO2 + Ca (OH)2 = CaCO3 + H2O
Mixing / Agitation
• Mixing devices
• Feeding daily
• Effective and rapid digestion with much decreased retention time
• Solid sub-layers undergo improved digestion with significant
utilization
• Completely destroys the undesired pathogens as well as the seeds
of weeds
• Liquid isolation from solid fractions is highly feasible
• Removing metabolites (gas removal)
• Bringing fresh material in contact with bacteria
• Reducing scum formation and sedimentation
• Preventing temperature gradients in the digester
• Avoiding the formation of blind spots (short cuts)
• Excessive stirring disturbs the symbiotic relationship between
the different bacteria species
Toxicity
• Volatile acid concentration reaches a value of 200 ppm
• Ammonical nitrogen concentration exceeds a value of 1500 ppm
• Ammonia, volatile acids, and heavy metals
• Nitrogen, phosphorus, magnesium, sodium, potassium, manganese,
calcium and cobalt
• Inhibition indicators
a. Reduction in methane yield over time
- indicated by two or more consecutive decreases of more
than 10% in daily yield at a constant loading rate
b. Increase in volatile acids concentration over time
- generally occurring when the total volatile acids (expressed
as acetic acid) exceed the normal range of about 250 to 500 milligrams
per liter
• Retarded microbial activity
- low quality gas with low methane content
• Reasons
- excessive acid formation : presence of high level
acid forming bacteria
- high acid contents in feed
- delays in addition of fresh feeds
- delayed withdrawal of digested sludge
- improper feed composition
Design of the Plant
KCIV Biogas Plant Deenabandhu Biogas Plant
Reference
• Mittal, K.M. 1996. Biogas system: principles and
applications. New age international (P) Ltd., New
Delhi. P:No: 151-177.

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Factors affecting biogas yield

  • 1. Lecture - 3 Analysis of factors affecting biogas yield
  • 2. Factors • Total solids content • pH • Temperature • C/N ratio • Retention time • Uniform Feeding & Type • Loading rate • Seeding • Mixing / Agitation • Toxicity • Pressure - low • Design of the plant
  • 4. pH • Acetate and fatty acids : lower the pH of digester liquor - ion bicarbonate equilibria of the carbon dioxide in the digester exert substantial resistance to pH change - buffer capacity or buffer intensity : quantified by the amount of strong acid (or base) added to the solution in order to bring about a change in pH • Presence of bicarbonate helps prevent : low pH pH = 6.3 + log[HCO3/dissolved CO2]
  • 5. Temperature • Cryophiles (Psychrophiles) - Occupies the area of cryophilic digestive regime - 12°C and 24°C • Mesophiles - Occupies the area of mesophilic digestive regime - 22°C and 40°C • Thermophiles - Occupies the area of thermophilic digestive regime - 50°C and 60°C
  • 6. Temperature Rate of reaction doubles for every 10°C rise in temperature up to an optimum and then declines rapidly
  • 7. C/N ratio • Carbon & Nitrogen : nutrients for efficient anaerobic digestion • Carbon : energy source • Nitrogen: building the cell structures • C:N ratio = 25-30:1 • If N concentration is too high (>1,700 mg/l of NH4-N) • pH is high - Growth of bacteria is inhibited due to toxicity caused by high levels of (uncharged) ammonia • Methanogens : adapt to 5,000 - 7,000 mg/l of NH4 - N given the pre -requisite that the uncharged ammonia (NH3 controlled by pH) level does not exceed 200 - 300 mg/l
  • 8. Retention time • Average time spent by the input slurry inside the digester before it come out • 20 – 120 days – depends on design & operating temperature • In India : 40 -50 days • Cold climates : 100 days LR = k (TS / HRT) k = 7
  • 9. Loading Rate • Waste material fed / unit volume of digester capacity • Gas production : m3 / kg of volatile solids • 1 kg of cow dung – 0.04 m3 of biogas • Based on gas requirement • Uniform feeding • Under feeding & Over feeding
  • 10. Seeding • Introduction of enriched anaerobic bacteria - for start up • Anaerobic bacteria proceeds - acid forming bacteria : abundant - methane forming bacteria : lesser • Improper mix of feedstock : change in pH - excessive formation of volatile fatty acids CO2 + Ca (OH)2 = CaCO3 + H2O
  • 11. Mixing / Agitation • Mixing devices • Feeding daily • Effective and rapid digestion with much decreased retention time • Solid sub-layers undergo improved digestion with significant utilization • Completely destroys the undesired pathogens as well as the seeds of weeds • Liquid isolation from solid fractions is highly feasible
  • 12. • Removing metabolites (gas removal) • Bringing fresh material in contact with bacteria • Reducing scum formation and sedimentation • Preventing temperature gradients in the digester • Avoiding the formation of blind spots (short cuts) • Excessive stirring disturbs the symbiotic relationship between the different bacteria species
  • 13. Toxicity • Volatile acid concentration reaches a value of 200 ppm • Ammonical nitrogen concentration exceeds a value of 1500 ppm • Ammonia, volatile acids, and heavy metals • Nitrogen, phosphorus, magnesium, sodium, potassium, manganese, calcium and cobalt • Inhibition indicators a. Reduction in methane yield over time - indicated by two or more consecutive decreases of more than 10% in daily yield at a constant loading rate b. Increase in volatile acids concentration over time - generally occurring when the total volatile acids (expressed as acetic acid) exceed the normal range of about 250 to 500 milligrams per liter
  • 14. • Retarded microbial activity - low quality gas with low methane content • Reasons - excessive acid formation : presence of high level acid forming bacteria - high acid contents in feed - delays in addition of fresh feeds - delayed withdrawal of digested sludge - improper feed composition
  • 15. Design of the Plant KCIV Biogas Plant Deenabandhu Biogas Plant
  • 16. Reference • Mittal, K.M. 1996. Biogas system: principles and applications. New age international (P) Ltd., New Delhi. P:No: 151-177.