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Problems Most likely causes Recommended action
Gas yield has dropped
•Drop in quality of substrates
•Drop of temperature
•Compounds inhibition
•Non-homogenous substrates
•Drop of methanogenic bacteria
•Assure substrates mixing and quality
•Check heating system
•Check level of potential inhibitor compounds
•Add digestate from another digester if the methanogenic bacteria as drop
Methane concentration
dropped
•Drop in quality of substrates
•Drop of temperature
•Compounds inhibition
•Assure substrates mixing and quality
•Check heating system
•Check level of potential inhibitor compounds
Foaming problem
•A new substrates with high protein content has been added
•Air is introduced in the digestion
•Temperature is changing
•Reduce or stop feeding
•Analyze substrates
•Reduce air introduction
WHAT ARE THE PROBLEMS THAT CAN OCCUR IN BIOGAS PLANTS?
AMMONIA(NH3)
Ammonia is a compound of nitrogen and hydrogen that is produced during the digestionprocess. Factors such as temperature,
input composition, ph, and bacteria acclimation influencethe effect of ammonia on thisprocess.
WHAT TO KEEP AN EYE ON:
The operator should make sure the ammonia concentration stays under 2000 ppm or between 50 to
200 mg /L to avoid biogas plant problems. Concentration levels that are between 1500 and 3000 mg /L
can inhibit the process and cause digestion failure. However, mesophilic digesters can support more
than 3000 ppm if it is well acclimated to ammonia. Ammonia levels that are higher than 3000 mg /L
can be toxic for the process.
When the operator notices the concentration of ammonia is climbing , he should reduce the organic
loading rate.
ALKALINITY (ALK)
The capacityof water to neutralizeacids in the biogasplantis called alkalinity(ALK). We measure ALK in milligramsof equivalent
calciumcarbonate per liter.It is used to measure carbonates, bicarbonates,hydroxides, and, sometimes, borates, silicates, and
phosphates
WHAT TO KEEP AN EYE ON:
The operator should make sure the ALK stays between 1500 and 5000 mg /L. The buffering
capacity of the digester content influences the stability of the digestion process. It should
also be noted that small ph variations can affect methanogens. Acid producers can function
with a wide range of ph
RATIO BETWEEN VOLATILE ACIDS AND ALKALINITY
The operator can calculatethe ratio between volatileacidsand alkalinityto control the digestionprocess better.
WHAT TO KEEP AN EYE ON:
The operator can use the following formula to calculate this ratio:
If the ratio is:
•Below 0.35: Digester operations are proper
•Between 0.1 and 0.35: The digester is well-operated
•+ 0.35: The digester experiences issues like increased organic loading, hydraulic overloading or others.
OXYGEN
The anaerobicdigestionprocess produces some oxygen even though it occurs in the absence of it.
WHAT TO KEEP AN EYE ON:
The anaerobic digestion process requires below 0.1 ppm of oxygen in the environment,
which is very little.
VOLATILE FATTY ACIDS (VFA)
Volatilefatty acids,or organicacids, shows the health of the digester. Vfas are also used as food for the methane formers. They
are measured in milligramsof equivalentacetic acid and are soluble in water. The production of VFA varies according to the
number of solids suppliedto the digester.
WHAT TO KEEP AN EYE ON:
The concentration of volatile fatty acids should be below 2000 ppm. A higher concentration can
off-balance the biology of the system and be toxic. The digester can overload, and the operator
can experience other biogas plant problems when the concentration is over 300 ml/L.
ORGANIC LOADING
The operator can measure organic loadingbased on the mass or weight of volatilesolidsper unit of digester volume per day, or
kg/m3 x d and lb/100 ft3 x d.
WHAT TO KEEP AN EYE ON:
The organic loading of anaerobic digestion systems can range between 1.6 and 6.4 kg /m 3 x d,
or 100 and 400 lb/100 ft3 x d. In any case, however, the operator should supply the digesters
at a consistent and constant rate.
FOAMING
The production of foam during the anaerobicdigestionprocess can decrease its performance and cause safety issues, damaged
equipment,and/or structures.
WHAT TO KEEP AN EYE ON:
The operator should pay attention to the mixing, temperature variations in the digester
and/or incorrect or inconsistent supplying if there is foam. It should also be noted that the
transfer of filaments from the liquid process stream to the digesters can create foam.
HEAVY METAL
Heavy metals like copper can enter the digester because of industrialusers. Traces of heavy metal is beneficialfor the anaerobic
digestion process. However, a higher concentration can be toxic to the process.
WHAT TO KEEP AN EYE ON:
The soluble concentration of heavy metal should stay below 0.5 mg /L.
Thank You

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python.pptx

  • 1. Problems Most likely causes Recommended action Gas yield has dropped •Drop in quality of substrates •Drop of temperature •Compounds inhibition •Non-homogenous substrates •Drop of methanogenic bacteria •Assure substrates mixing and quality •Check heating system •Check level of potential inhibitor compounds •Add digestate from another digester if the methanogenic bacteria as drop Methane concentration dropped •Drop in quality of substrates •Drop of temperature •Compounds inhibition •Assure substrates mixing and quality •Check heating system •Check level of potential inhibitor compounds Foaming problem •A new substrates with high protein content has been added •Air is introduced in the digestion •Temperature is changing •Reduce or stop feeding •Analyze substrates •Reduce air introduction WHAT ARE THE PROBLEMS THAT CAN OCCUR IN BIOGAS PLANTS?
  • 2. AMMONIA(NH3) Ammonia is a compound of nitrogen and hydrogen that is produced during the digestionprocess. Factors such as temperature, input composition, ph, and bacteria acclimation influencethe effect of ammonia on thisprocess. WHAT TO KEEP AN EYE ON: The operator should make sure the ammonia concentration stays under 2000 ppm or between 50 to 200 mg /L to avoid biogas plant problems. Concentration levels that are between 1500 and 3000 mg /L can inhibit the process and cause digestion failure. However, mesophilic digesters can support more than 3000 ppm if it is well acclimated to ammonia. Ammonia levels that are higher than 3000 mg /L can be toxic for the process. When the operator notices the concentration of ammonia is climbing , he should reduce the organic loading rate.
  • 3. ALKALINITY (ALK) The capacityof water to neutralizeacids in the biogasplantis called alkalinity(ALK). We measure ALK in milligramsof equivalent calciumcarbonate per liter.It is used to measure carbonates, bicarbonates,hydroxides, and, sometimes, borates, silicates, and phosphates WHAT TO KEEP AN EYE ON: The operator should make sure the ALK stays between 1500 and 5000 mg /L. The buffering capacity of the digester content influences the stability of the digestion process. It should also be noted that small ph variations can affect methanogens. Acid producers can function with a wide range of ph
  • 4. RATIO BETWEEN VOLATILE ACIDS AND ALKALINITY The operator can calculatethe ratio between volatileacidsand alkalinityto control the digestionprocess better. WHAT TO KEEP AN EYE ON: The operator can use the following formula to calculate this ratio: If the ratio is: •Below 0.35: Digester operations are proper •Between 0.1 and 0.35: The digester is well-operated •+ 0.35: The digester experiences issues like increased organic loading, hydraulic overloading or others.
  • 5. OXYGEN The anaerobicdigestionprocess produces some oxygen even though it occurs in the absence of it. WHAT TO KEEP AN EYE ON: The anaerobic digestion process requires below 0.1 ppm of oxygen in the environment, which is very little.
  • 6. VOLATILE FATTY ACIDS (VFA) Volatilefatty acids,or organicacids, shows the health of the digester. Vfas are also used as food for the methane formers. They are measured in milligramsof equivalentacetic acid and are soluble in water. The production of VFA varies according to the number of solids suppliedto the digester. WHAT TO KEEP AN EYE ON: The concentration of volatile fatty acids should be below 2000 ppm. A higher concentration can off-balance the biology of the system and be toxic. The digester can overload, and the operator can experience other biogas plant problems when the concentration is over 300 ml/L.
  • 7. ORGANIC LOADING The operator can measure organic loadingbased on the mass or weight of volatilesolidsper unit of digester volume per day, or kg/m3 x d and lb/100 ft3 x d. WHAT TO KEEP AN EYE ON: The organic loading of anaerobic digestion systems can range between 1.6 and 6.4 kg /m 3 x d, or 100 and 400 lb/100 ft3 x d. In any case, however, the operator should supply the digesters at a consistent and constant rate.
  • 8. FOAMING The production of foam during the anaerobicdigestionprocess can decrease its performance and cause safety issues, damaged equipment,and/or structures. WHAT TO KEEP AN EYE ON: The operator should pay attention to the mixing, temperature variations in the digester and/or incorrect or inconsistent supplying if there is foam. It should also be noted that the transfer of filaments from the liquid process stream to the digesters can create foam.
  • 9. HEAVY METAL Heavy metals like copper can enter the digester because of industrialusers. Traces of heavy metal is beneficialfor the anaerobic digestion process. However, a higher concentration can be toxic to the process. WHAT TO KEEP AN EYE ON: The soluble concentration of heavy metal should stay below 0.5 mg /L.