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Modelling of an alternating oxidation ditch system

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dc.contributor.author Stamou, A en
dc.contributor.author Katsiri, A en
dc.contributor.author Mantziaras, I en
dc.contributor.author Boshnakov, K en
dc.contributor.author Koumanova, B en
dc.contributor.author Stoyanov, S en
dc.date.accessioned 2014-03-01T02:41:36Z
dc.date.available 2014-03-01T02:41:36Z
dc.date.issued 1999 en
dc.identifier.issn 0273-1223 en
dc.identifier.uri https://dspace.lib.ntua.gr/xmlui/handle/123456789/30560
dc.subject Alternating oxidation ditch system en
dc.subject ASM1 model en
dc.subject Dispersion en
dc.subject DO profiles en
dc.subject Mathematical model en
dc.subject.classification Engineering, Environmental en
dc.subject.classification Environmental Sciences en
dc.subject.classification Water Resources en
dc.subject.other Alternating oxidation ditch systems en
dc.subject.other Boundary conditions en
dc.subject.other Denitrification en
dc.subject.other Mass transfer en
dc.subject.other Mathematical models en
dc.subject.other Nitrification en
dc.subject.other Oxidation en
dc.subject.other Pilot plants en
dc.subject.other Sedimentary rocks en
dc.subject.other Sewage aeration en
dc.subject.other Sewage treatment plants en
dc.subject.other Activated sludge process en
dc.subject.other carbon en
dc.subject.other activated sludge en
dc.subject.other aeration en
dc.subject.other calibration en
dc.subject.other conference paper en
dc.subject.other denitrification en
dc.subject.other dispersion en
dc.subject.other effluent standard en
dc.subject.other mathematical model en
dc.subject.other nitrification en
dc.subject.other oxidation en
dc.subject.other waste water management en
dc.title Modelling of an alternating oxidation ditch system en
heal.type conferenceItem en
heal.identifier.primary 10.1016/S0273-1223(99)00076-1 en
heal.identifier.secondary http://dx.doi.org/10.1016/S0273-1223(99)00076-1 en
heal.language English en
heal.publicationDate 1999 en
heal.abstract This paper presents a mathematical model for an alternating oxidation ditch system, performing carbon oxidation-nitrification, denitrification and settling. The model consists of I-dimensional mass balance (convection-dispersion) equations, based on the IAWPRC activated sludge model No 1. The data used for the calibration and the application of the model an collected from a pilot plant The present work consists of 3 parts. In the first part a brief description of the pilot plant is made. The second part deals with a short presentation of the basic equations and the boundary conditions of the model. The calibration and application of the model with the corresponding conclusions me contained in the third part. In the calibration, the values of the dispersion coefficient, E, and the correction factors a and beta of the equation of the aeration equipment (rotors) have been determined equal to E=170000 m(2) day(-1), beta=0.85 and alpha=0.3 and 0.825, for the operation of the rotors in the low and high speed respectively. The application of the model shows that predicted effluent concentration values an in a very good agreement with experiments. (C) 1999 IAWQ Published by Elsevier Science Ltd. AII rights reserved. en
heal.publisher PERGAMON-ELSEVIER SCIENCE LTD en
heal.journalName Water Science and Technology en
dc.identifier.doi 10.1016/S0273-1223(99)00076-1 en
dc.identifier.isi ISI:000079678400022 en
dc.identifier.volume 39 en
dc.identifier.issue 4 en
dc.identifier.spage 169 en
dc.identifier.epage 176 en


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