dc.contributor.author |
Rathnasiri, PG |
|
dc.contributor.author |
Hayun |
|
dc.contributor.author |
Bakke, R |
|
dc.date.accessioned |
2013-12-30T18:05:42Z |
|
dc.date.available |
2013-12-30T18:05:42Z |
|
dc.date.issued |
2007 |
|
dc.identifier.uri |
http://dl.lib.mrt.ac.lk/handle/123/9733 |
|
dc.description.abstract |
Anaerobic treatment offers a number of attractive advantages in the treatment of highstrength
organic waste water, but difficulties in maintaining process stability is a
disadvantage. The process is sensitive to changes in environmental and operating
conditions and disturbance in microbial balance often results in failure of the process.
Industrial anaerobic reactor operations seldom can be characterized by true steady state
operations. Stability is paramount in the operation of large scale anaerobic co-digestion
plants which are operated intermittently under varying feed flow patterns and feed
compositions. If instability occurs, variations of biogas compositions will lead to make
operating problems in subsequent operations such as electricity generations. Most of
anaerobic co-digestion processes are run below maximum capacity due to the danger of
failure of overloading. Thus it is needed to conduct lab scale experiments to screen
different options before designing and commissioning large scale processes. |
en_US |
dc.language.iso |
en |
en_US |
dc.title |
Transient response and stability of anaerobic reactors following interm tttant feeding |
en_US |
dc.type |
Conference-Extended-Abstract |
en_US |
dc.identifier.year |
2007 |
en_US |
dc.identifier.conference |
ERU Research for industry |
en_US |
dc.identifier.pgnos |
68-70 |
en_US |
dc.identifier.proceeding |
Proceeding of the 13th annual symposium |
en_US |