dc.contributor.author |
Mantziaras, ID |
en |
dc.contributor.author |
Stamou, A |
en |
dc.contributor.author |
Katsiri, A |
en |
dc.date.accessioned |
2014-03-01T01:35:36Z |
|
dc.date.available |
2014-03-01T01:35:36Z |
|
dc.date.issued |
2011 |
en |
dc.identifier.issn |
1615-7591 |
en |
dc.identifier.uri |
https://dspace.lib.ntua.gr/xmlui/handle/123456789/21114 |
|
dc.subject |
Alternating oxidation ditch system |
en |
dc.subject |
Mathematical model |
en |
dc.subject |
Nitrogen optimization |
en |
dc.subject |
Operational cycle |
en |
dc.subject |
Wastewater treatment |
en |
dc.subject.classification |
Biotechnology & Applied Microbiology |
en |
dc.subject.classification |
Engineering, Chemical |
en |
dc.subject.other |
Calibration and verification |
en |
dc.subject.other |
Carbon oxidation |
en |
dc.subject.other |
EU directives |
en |
dc.subject.other |
Mass balance |
en |
dc.subject.other |
Operational cycle |
en |
dc.subject.other |
Oxidation ditch |
en |
dc.subject.other |
Pilot system |
en |
dc.subject.other |
Pilot testing |
en |
dc.subject.other |
Simulation systems |
en |
dc.subject.other |
Time length |
en |
dc.subject.other |
Computer simulation |
en |
dc.subject.other |
Denitrification |
en |
dc.subject.other |
Mathematical models |
en |
dc.subject.other |
Nitrogen |
en |
dc.subject.other |
Optimization |
en |
dc.subject.other |
Oxidation |
en |
dc.subject.other |
Sewage lagoons |
en |
dc.subject.other |
Wastewater |
en |
dc.subject.other |
Wastewater treatment |
en |
dc.subject.other |
Nitrogen removal |
en |
dc.subject.other |
alternating oxidation ditch system |
en |
dc.subject.other |
article |
en |
dc.subject.other |
calibration |
en |
dc.subject.other |
controlled study |
en |
dc.subject.other |
denitrification |
en |
dc.subject.other |
effluent standard |
en |
dc.subject.other |
mathematical model |
en |
dc.subject.other |
nitrification |
en |
dc.subject.other |
nitrogen removal |
en |
dc.subject.other |
performance measurement system |
en |
dc.subject.other |
priority journal |
en |
dc.subject.other |
process design |
en |
dc.subject.other |
process optimization |
en |
dc.subject.other |
reaction time |
en |
dc.subject.other |
simulation |
en |
dc.subject.other |
system analysis |
en |
dc.subject.other |
waste component removal |
en |
dc.subject.other |
waste water management |
en |
dc.subject.other |
Carbon |
en |
dc.subject.other |
Denitrification |
en |
dc.subject.other |
Models, Theoretical |
en |
dc.subject.other |
Nitrification |
en |
dc.subject.other |
Nitrogen |
en |
dc.subject.other |
Oxidation-Reduction |
en |
dc.subject.other |
Sewage |
en |
dc.subject.other |
Time Factors |
en |
dc.subject.other |
Waste Disposal, Fluid |
en |
dc.subject.other |
Water Purification |
en |
dc.title |
Effect of operational cycle time length on nitrogen removal in an alternating oxidation ditch system |
en |
heal.type |
journalArticle |
en |
heal.identifier.primary |
10.1007/s00449-010-0508-5 |
en |
heal.identifier.secondary |
http://dx.doi.org/10.1007/s00449-010-0508-5 |
en |
heal.language |
English |
en |
heal.publicationDate |
2011 |
en |
heal.abstract |
This paper refers to nitrogen removal optimization of an alternating oxidation ditch system through the use of a mathematical model and pilot testing. The pilot system where measurements have been made has a total volume of 120 m3 and consists of two ditches operating in four phases during one cycle and performs carbon oxidation, nitrification, denitrification and settling. The mathematical model consists of one-dimensional mass balance (convection-dispersion) equations based on the IAWPRC ASM 1 model. After the calibration and verification of the model, simulation system performance was made. Optimization is achieved by testing operational cycles and phases with different time lengths. The limits of EU directive 91/271 for nitrogen removal have been used for comparison. The findings show that operational cycles with smaller time lengths can achieve higher nitrogen removals and that an ""equilibrium"" between phase time percentages in the whole cycle, for a given inflow, must be achieved. © 2011 Springer-Verlag. |
en |
heal.publisher |
SPRINGER |
en |
heal.journalName |
Bioprocess and Biosystems Engineering |
en |
dc.identifier.doi |
10.1007/s00449-010-0508-5 |
en |
dc.identifier.isi |
ISI:000290537200008 |
en |
dc.identifier.volume |
34 |
en |
dc.identifier.issue |
5 |
en |
dc.identifier.spage |
597 |
en |
dc.identifier.epage |
606 |
en |