Difference between revisions of "Anaerobic Digestion"
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| + | '''This system is also called:''' AD, Digestion, | ||
| + | =Importance= | ||
| + | <!--Relay any broader impact--> | ||
=Principles of Operation= | =Principles of Operation= | ||
<!-- Only briefly state anything that the StemNode Diagrams can cover within subsystems. This section is often omitted for specific systems (manuals on a specific make, model, or serial number) --> | <!-- Only briefly state anything that the StemNode Diagrams can cover within subsystems. This section is often omitted for specific systems (manuals on a specific make, model, or serial number) --> | ||
| − | Anaerobic digestion is the conversion of organic matter to biogas which is flammable if the methane content of the biogas is high enough. Bacteria and Archea that perform the individual stages of anaerobic digestion are naturally present in the feces and organic matter that enter the digester or can be introduced from an already functioning digester. The conditions within the digester can | + | Anaerobic digestion is the conversion of organic matter to biogas which is flammable if the methane content of the biogas is high enough. Bacteria and Archea that perform the individual stages of anaerobic digestion are naturally present in the feces and organic matter that enter the digester or can be introduced from an already functioning digester. The conditions within the digester can determine which organisms proliferate. |
| − | The subprocesses of anaerobic digestion are degredation, hydrolysis, acidogenesis, acetogenesis, methanogenesis. Of these, hydrolysis is often the rate limiting step followed by methanogenesis. Typically all subprocesses are carried out concurrently in a single vessel, however large scale facilities are increasingly splitting up the processes in order to provide conditions optimal for each sub-process. For example it is advantageous to split up the acid forming phases (called acid-phase digestion) from the methanogenesis phase because it allows for an overall reduction in reactor volume needed although it increases complexity See [[#Modes of Operation|Modes of Operation]]. | + | The subprocesses of anaerobic digestion are degredation, hydrolysis, acidogenesis, acetogenesis, and methanogenesis. Of these, hydrolysis is often the rate limiting step followed by methanogenesis. Typically all subprocesses are carried out concurrently in a single vessel, however large scale facilities are increasingly splitting up the processes in order to provide conditions optimal for each sub-process. For example it is advantageous to split up the acid forming phases (called acid-phase digestion) from the methanogenesis phase because it allows for an overall reduction in reactor volume needed although it increases complexity (See [[#Modes of Operation|Modes of Operation]]). |
==Modes of Operation== | ==Modes of Operation== | ||
| − | Three different temperature ranges are ideal for anaerobic digestion. Each | + | Three different temperature ranges are ideal for anaerobic digestion. Each temperature range selects for a different set of organisms that carry out the process. These temperatures represent local optimums, however biogas can be successfully produced outside these ranges and the rates of organic matter degredation and biogas production generally increase with increasing temperature. |
| − | '''Psycrophilic digestion''' 15°C (59°F) <br/> | + | '''Psycrophilic digestion''' 15°C (59°F) <br /> |
| − | '''Mesophilic Digestion'''30-38°C (85-100°F) <br/> | + | '''Mesophilic Digestion''' 30-38°C (85-100°F) <br /> |
| − | '''Thermophilic digestion''' 50 to 57°C (122-135°F) <br/> | + | '''Thermophilic digestion''' 50 to 57°C (122-135°F) <br /> |
Psyochrophilic and mesophilic digestion are commonly used at the building scale level, while mesophilic and thermophilic is typically operated at large scale facilities. | Psyochrophilic and mesophilic digestion are commonly used at the building scale level, while mesophilic and thermophilic is typically operated at large scale facilities. | ||
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{| class="wikitable sortable" | {| class="wikitable sortable" | ||
|- | |- | ||
| − | ! rowspan ="2"|Condition | + | ! rowspan="2" |Condition |
| − | ! colspan = "3"|Optimum | + | ! colspan="3" |Optimum |
| − | ! rowspan ="2"|Operating Range | + | ! rowspan="2" |Operating Range |
| − | ! rowspan ="2"|Unit | + | ! rowspan="2" |Unit |
| − | ! rowspan ="2"|Notes | + | ! rowspan="2" |Notes |
|- | |- | ||
!Psycrophilic !! Mesophilic !! Thermophilic | !Psycrophilic !! Mesophilic !! Thermophilic | ||
|- | |- | ||
| Temperature | | Temperature | ||
| − | | style="text-align:right;"| 15 | + | | style="text-align:right;" | 15 |
| − | | style="text-align:right;"| 30-38 | + | | style="text-align:right;" | 30-38 |
| − | | style="text-align:right;"| 50-57 | + | | style="text-align:right;" | 50-57 |
| − | | style="text-align:right;"| 15-57 | + | | style="text-align:right;" | 15-57 |
| °C | | °C | ||
| NA | | NA | ||
|- | |- | ||
| pH | | pH | ||
| − | | colspan = "3" style="text-align:center;" | 7 | + | | colspan="3" style="text-align:center;" | 7 |
| - | | - | ||
| - | | - | ||
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==Maintenance Schedule== | ==Maintenance Schedule== | ||
<!--This section is for expected maintenance. Repairs of unexpected problems should go under the "Typical Failures and Known Solutions" section. Cost data should be omitted since it will change over time--> | <!--This section is for expected maintenance. Repairs of unexpected problems should go under the "Typical Failures and Known Solutions" section. Cost data should be omitted since it will change over time--> | ||
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| + | |||
| + | Times are based on Mesophilic Digestion | ||
{| class="wikitable sortable" | {| class="wikitable sortable" | ||
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! Time to Complete | ! Time to Complete | ||
|- | |- | ||
| − | | | + | | Residence Time of 28 days |
| − | | | + | | Remove Liquid |
| − | | | + | | Operator |
| − | | | + | | N/A |
| + | |- | ||
| + | | Residence Time of 28 days | ||
| + | | Remove Solids | ||
| + | | Operator | ||
| + | | N/A | ||
|} | |} | ||
| − | == | + | ==Failures and Solutions== |
<!--Historical significance of a failure is better suited for Wikipedia or other sites. You are encouraged to link out to these sites from this section --> | <!--Historical significance of a failure is better suited for Wikipedia or other sites. You are encouraged to link out to these sites from this section --> | ||
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| low gas production | | low gas production | ||
| high ammonia | | high ammonia | ||
| − | | Ammonia can penetrate the cell walls of methanogens and inactivate the organisms | + | | Ammonia can penetrate the cell walls of methanogens and inactivate the organisms<ref>{{Cite journal|last=Chen|first=Ye|last2=Cheng|first2=Jay J.|last3=Creamer|first3=Kurt S.|date=2008-07-01|title=Inhibition of anaerobic digestion process: A review|url=https://www.sciencedirect.com/science/article/pii/S0960852407001563|journal=Bioresource Technology|language=en|volume=99|issue=10|pages=4044–4064|doi=10.1016/j.biortech.2007.01.057|issn=0960-8524}}</ref> |
| Reduce inputs until symptoms relieve, dilute with water, or add buffers like CaCO3 | | Reduce inputs until symptoms relieve, dilute with water, or add buffers like CaCO3 | ||
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<!--This only applies to generalized systems (those that do not have a make, model, or serial number). Delete section for specific systems --> | <!--This only applies to generalized systems (those that do not have a make, model, or serial number). Delete section for specific systems --> | ||
| + | '''Household Scale Anaerobic Digesters''' | ||
{| class="wikitable sortable" | {| class="wikitable sortable" | ||
|- | |- | ||
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|- | |- | ||
| − | | Home Biogas | + | | [https://homebiogas.com/ Home Biogas] |
| 2.0 | | 2.0 | ||
| October 2018 | | October 2018 | ||
Latest revision as of 04:24, 28 February 2019
Authors:
This system is also called: AD, Digestion,
Contents
Importance
Principles of Operation
Anaerobic digestion is the conversion of organic matter to biogas which is flammable if the methane content of the biogas is high enough. Bacteria and Archea that perform the individual stages of anaerobic digestion are naturally present in the feces and organic matter that enter the digester or can be introduced from an already functioning digester. The conditions within the digester can determine which organisms proliferate.
The subprocesses of anaerobic digestion are degredation, hydrolysis, acidogenesis, acetogenesis, and methanogenesis. Of these, hydrolysis is often the rate limiting step followed by methanogenesis. Typically all subprocesses are carried out concurrently in a single vessel, however large scale facilities are increasingly splitting up the processes in order to provide conditions optimal for each sub-process. For example it is advantageous to split up the acid forming phases (called acid-phase digestion) from the methanogenesis phase because it allows for an overall reduction in reactor volume needed although it increases complexity (See Modes of Operation).
Modes of Operation
Three different temperature ranges are ideal for anaerobic digestion. Each temperature range selects for a different set of organisms that carry out the process. These temperatures represent local optimums, however biogas can be successfully produced outside these ranges and the rates of organic matter degredation and biogas production generally increase with increasing temperature.
Psycrophilic digestion 15°C (59°F)
Mesophilic Digestion 30-38°C (85-100°F)
Thermophilic digestion 50 to 57°C (122-135°F)
Psyochrophilic and mesophilic digestion are commonly used at the building scale level, while mesophilic and thermophilic is typically operated at large scale facilities.
Operating Requirements and Conditions
| Condition | Optimum | Operating Range | Unit | Notes | ||
|---|---|---|---|---|---|---|
| Psycrophilic | Mesophilic | Thermophilic | ||||
| Temperature | 15 | 30-38 | 50-57 | 15-57 | °C | NA |
| pH | 7 | - | - | - | ||
Ratios of Inputs to Outputs
Mathematic Models
Maintenance and Repair
Maintenance Schedule
Times are based on Mesophilic Digestion
| Frequency | Action | Who Performs? | Time to Complete |
|---|---|---|---|
| Residence Time of 28 days | Remove Liquid | Operator | N/A |
| Residence Time of 28 days | Remove Solids | Operator | N/A |
Failures and Solutions
| Problem | Symptom (s) | Fundamental Cause | Solution |
|---|---|---|---|
| low gas production | low pH | Neutral volatile fatty acids or lactic acid penetrate the cell walls of methanogens and inactivate the organisms | Reduce inputs, especially carbohydrates, until symptoms relieve, or dilute with water, or add buffers like CaCO3 |
| low gas production | high ammonia | Ammonia can penetrate the cell walls of methanogens and inactivate the organisms[1] | Reduce inputs until symptoms relieve, dilute with water, or add buffers like CaCO3 |
| non-flammable gas | high moisture in gas | Moisture is evaporated during burning and can reduce the temperature below the level that a flame can be sustained. | Add a cooling trap where moisture can condense in the gas line |
| non-flammable gas | high CO2 in gas | Biogas must be above ?% methane for combustion. Inadvertent introduction of oxygen can increase CO2 production. | Add a cooling trap where moisture can condense in the gas line |
Methanogens are typically the most sensitive organisms in the process but are the most crucial because they perform the final step of converting acids to methane. Methanogens can be sensitive to high amounts of acid or high amounts ammonia. A low pH indicates high amounts of acid which can occur by putting too much organic matter in the digester. This is especially the case with carbohydrates (e.g. from food waste) which break down quickly to acids causing acid build up. A high pH could The quickest indicator of conditions that are hostile to methanogens is pH, which should be near 7.
Non-flammable gas could be due to too much moisture in the gas or not enough methane in the gas. This is common during digester startup.
Instances of the System
Household Scale Anaerobic Digesters
| Make | Model | Start of Production | End of Production | Number Produced |
|---|---|---|---|---|
| Home Biogas | 2.0 | October 2018 | In Production | - |
System Variations
Visual models
Intellectual Property
Regulations
- ↑ Chen, Ye; Cheng, Jay J.; Creamer, Kurt S. (2008-07-01). "Inhibition of anaerobic digestion process: A review". Bioresource Technology. 99 (10): 4044–4064. doi:10.1016/j.biortech.2007.01.057. ISSN 0960-8524.