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New page: <!-- table at top of page with logo, picture, Application level, Management level, and input-output tables --> {{santable| sys1=1| sys2=[[Blackwater Treatment System...
<!-- table at top of page with logo, picture, Application level, Management level, and input-output tables -->
{{santable|
sys1=[[Single Pit System |1]]|
sys2=[[Blackwater Treatment System with Infiltration|5]]|
sys3=[[Blackwater Treatment System with Sewerage|6]]|
sys4=[[(Semi-) Centralized Treatment System |7]]|
sys5=[[Sewerage System with Urine Diversion |8]]|
sys6=|
sys7=|
sys8=|
pic=Upflow_anaerobic_sludge_blanket_reactor1.png|
ApplHousehold=|
ApplNeighbourhood=X|
ApplCity=XX|
ManHousehold=|
ManShared=|
ManPublic=XX|
Input1=Blackwater|Input2=Greywater |Input3= | Input4= |Input5=|
Output1= Effluent | Output2= Treated Sludge | Output3= Biogas | Output4= | Output5=
}}
'''The Upflow Anaerobic Sludge Blanket Reactor (UASB) is a single tank process. Wastewater enters the reactor from the bottom, and flows upward. A suspended sludge blanket filters and treats the wastewater as the wastewater flows through it.'''
The sludge blanket is comprised of microbial granules, i.e. small agglomerations (0.5 to 2mm in diameter) of microorganisms that, because of their weight, resist being washed out in the upflow. The microorganisms in the sludge layer degrade organic compounds. As a result, gases (methane and carbon dioxide) are released. The rising bubbles mix the sludge without the assistance of any mechanical parts. Sloped walls deflect material that reaches the top of the tank downwards. The clarified effluent is extracted from the top of the tank in an area above the sloped walls.
After several weeks of use, larger granules of sludge form which in turn act as filters for smaller particles as the effluent rises through the cushion of sludge. Because of the upflow regime, granule-forming organisms are preferentially accumulated as the others are washed out.
The gas that rises to the top is collected in a gas collection dome and can be used as energy (biogas). An upflow velocity of 0.6 to 0.9m/h must be maintained to keep the sludge blanket in suspension.
{{procontable | pro=
- High reduction in organics. <br> - Can withstand high organic loading rates (up to 10kg BOD/m3/d) and high hydraulic loading rates. <br> - Low production sludge (and thus, infrequent desludging required). <br> - Biogas can be used for energy (but usually requires scrubbing first). | con=
- Difficult to maintain proper hydraulic conditions (upflow and settling rate must be balanced). <br> - Long start up time. <br> - Treatment may be unstable with variable hydraulic and organic loads. <br> - Constant source of electricity is required. <br> - Not all parts and materials may be available locally. <br> - Requires expert design and construction supervision.
}}
==Adequacy==
A UASB is not appropriate for small or rural communities without a constant water supply or electricity. A skilled operator is required to monitor and repair the reactor and the pump in case of problems. Although the technology is simple to design and build, it is not well proven for domestic wastewater, although new research is promising.
The UASB reactor has the potential to produce higher quality effluent than Septic Tank|septic tanks]], and can do so in a smaller reactor volume. Although it is a wellestablished process for large-scale industrial wastewater treatment processes, its application to domestic sewage is still relatively new. Typically it is used for brewery, distillery, food processing and pulp and paper waste since the process can typically remove 85% to 90% of Chemical Oxygen Demand (COD). Where the influent is low strength, the reactor may not work properly. Temperature will also affect performance.
==Health Aspects/Acceptance==
UASB is a centralized treatment technology that must be operated and maintained by professionals. As with all wastewater processes, operators should take proper health and safety measures while working in the plant.
==Maintenance==
Desludging is infrequent and only excess sludge is removed once every 2 to 3 years. A permanent operator is required to control and monitor the dosing pump.
==References==
* Elizabeth Tilley et.al (2008). [http://www.eawag.ch/organisation/abteilungen/sandec/publikationen/publications_sesp/downloads_sesp/compendium_high.pdf Compendium of Sanitation Systems and Technologies] ([http://www.eawag.ch/organisation/abteilungen/sandec/publikationen/publications_sesp/downloads_sesp/compendium_low.pdf low res version]). Department of Water and Sanitation in Development Countries ([http://www.sandec.ch/ Sandec]) at the Swiss Federal Institute of Aquatic Science and Technology (Eawag). (Provides a full overview of sanitation systems.)
* Crites, R. and Tchobanoglous, G. (1998). Small and decentralized wastewater management systems. WCB and McGraw-Hill, New York, USA. (Short overview.)
* Lettinga, G., Roersma, R. and Grin, P. (1983). Anaerobic Treatment of Raw Domestic Sewage at Ambient Temperatures Using a Granular Bed UASB Reactor Biotechnology and Bioengineering 25 (7): 1701–1723. (The first paper describing the process.)
* Sasse, L. (1998). DEWATS: Decentralised Wastewater Treatment in Developing Countries. BORDA, Bremen Overseas Research and Development Association, Bremen, Germany. (Short overview.)
* von Sperlin, M. and de Lemos Chernicharo, CA. (2005). Biological Wastewater Treatment in Warm Climate Regions. Volume One. IWA, London, pp 741–804. (Detailed design information)
* Tare, V. and Nema, A. (n.d). UASB Technology-expectations and reality. United Nations Asian and Pacific Centre for Agricultural Engineering and Machinery. Available: http://unapcaem.org (Assessment of UASB installations in India.)
* Vigneswaran, S., et al. (1986). Environmental Sanitation Reviews: Anaerobic Wastewater Treatment- Attached growth and sludge blanket process. Environmental Sanitation Information Center, AIT, Bangkok, Thailand. (Chapter 5 provides a good technical overview.)
{{santable|
sys1=[[Single Pit System |1]]|
sys2=[[Blackwater Treatment System with Infiltration|5]]|
sys3=[[Blackwater Treatment System with Sewerage|6]]|
sys4=[[(Semi-) Centralized Treatment System |7]]|
sys5=[[Sewerage System with Urine Diversion |8]]|
sys6=|
sys7=|
sys8=|
pic=Upflow_anaerobic_sludge_blanket_reactor1.png|
ApplHousehold=|
ApplNeighbourhood=X|
ApplCity=XX|
ManHousehold=|
ManShared=|
ManPublic=XX|
Input1=Blackwater|Input2=Greywater |Input3= | Input4= |Input5=|
Output1= Effluent | Output2= Treated Sludge | Output3= Biogas | Output4= | Output5=
}}
'''The Upflow Anaerobic Sludge Blanket Reactor (UASB) is a single tank process. Wastewater enters the reactor from the bottom, and flows upward. A suspended sludge blanket filters and treats the wastewater as the wastewater flows through it.'''
The sludge blanket is comprised of microbial granules, i.e. small agglomerations (0.5 to 2mm in diameter) of microorganisms that, because of their weight, resist being washed out in the upflow. The microorganisms in the sludge layer degrade organic compounds. As a result, gases (methane and carbon dioxide) are released. The rising bubbles mix the sludge without the assistance of any mechanical parts. Sloped walls deflect material that reaches the top of the tank downwards. The clarified effluent is extracted from the top of the tank in an area above the sloped walls.
After several weeks of use, larger granules of sludge form which in turn act as filters for smaller particles as the effluent rises through the cushion of sludge. Because of the upflow regime, granule-forming organisms are preferentially accumulated as the others are washed out.
The gas that rises to the top is collected in a gas collection dome and can be used as energy (biogas). An upflow velocity of 0.6 to 0.9m/h must be maintained to keep the sludge blanket in suspension.
{{procontable | pro=
- High reduction in organics. <br> - Can withstand high organic loading rates (up to 10kg BOD/m3/d) and high hydraulic loading rates. <br> - Low production sludge (and thus, infrequent desludging required). <br> - Biogas can be used for energy (but usually requires scrubbing first). | con=
- Difficult to maintain proper hydraulic conditions (upflow and settling rate must be balanced). <br> - Long start up time. <br> - Treatment may be unstable with variable hydraulic and organic loads. <br> - Constant source of electricity is required. <br> - Not all parts and materials may be available locally. <br> - Requires expert design and construction supervision.
}}
==Adequacy==
A UASB is not appropriate for small or rural communities without a constant water supply or electricity. A skilled operator is required to monitor and repair the reactor and the pump in case of problems. Although the technology is simple to design and build, it is not well proven for domestic wastewater, although new research is promising.
The UASB reactor has the potential to produce higher quality effluent than Septic Tank|septic tanks]], and can do so in a smaller reactor volume. Although it is a wellestablished process for large-scale industrial wastewater treatment processes, its application to domestic sewage is still relatively new. Typically it is used for brewery, distillery, food processing and pulp and paper waste since the process can typically remove 85% to 90% of Chemical Oxygen Demand (COD). Where the influent is low strength, the reactor may not work properly. Temperature will also affect performance.
==Health Aspects/Acceptance==
UASB is a centralized treatment technology that must be operated and maintained by professionals. As with all wastewater processes, operators should take proper health and safety measures while working in the plant.
==Maintenance==
Desludging is infrequent and only excess sludge is removed once every 2 to 3 years. A permanent operator is required to control and monitor the dosing pump.
==References==
* Elizabeth Tilley et.al (2008). [http://www.eawag.ch/organisation/abteilungen/sandec/publikationen/publications_sesp/downloads_sesp/compendium_high.pdf Compendium of Sanitation Systems and Technologies] ([http://www.eawag.ch/organisation/abteilungen/sandec/publikationen/publications_sesp/downloads_sesp/compendium_low.pdf low res version]). Department of Water and Sanitation in Development Countries ([http://www.sandec.ch/ Sandec]) at the Swiss Federal Institute of Aquatic Science and Technology (Eawag). (Provides a full overview of sanitation systems.)
* Crites, R. and Tchobanoglous, G. (1998). Small and decentralized wastewater management systems. WCB and McGraw-Hill, New York, USA. (Short overview.)
* Lettinga, G., Roersma, R. and Grin, P. (1983). Anaerobic Treatment of Raw Domestic Sewage at Ambient Temperatures Using a Granular Bed UASB Reactor Biotechnology and Bioengineering 25 (7): 1701–1723. (The first paper describing the process.)
* Sasse, L. (1998). DEWATS: Decentralised Wastewater Treatment in Developing Countries. BORDA, Bremen Overseas Research and Development Association, Bremen, Germany. (Short overview.)
* von Sperlin, M. and de Lemos Chernicharo, CA. (2005). Biological Wastewater Treatment in Warm Climate Regions. Volume One. IWA, London, pp 741–804. (Detailed design information)
* Tare, V. and Nema, A. (n.d). UASB Technology-expectations and reality. United Nations Asian and Pacific Centre for Agricultural Engineering and Machinery. Available: http://unapcaem.org (Assessment of UASB installations in India.)
* Vigneswaran, S., et al. (1986). Environmental Sanitation Reviews: Anaerobic Wastewater Treatment- Attached growth and sludge blanket process. Environmental Sanitation Information Center, AIT, Bangkok, Thailand. (Chapter 5 provides a good technical overview.)
