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      Anoxic and aerobic values for the yield coefficient of the heterotrophic biomass: determination at full-scale plants and consequences on simulations

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          Abstract

          The present study aims at optimising the nitrification and denitrification phases at intermittently aerated process (activated sludge) removing nitrogen from municipal wastewater. The nitrogen removal performance recorded at 22 intermittently aerated plants was compared to the results obtained from the simulations given by the widely used ASM1. It is shown that simulations with a single value for the heterotrophic yield with any electron acceptor over-predict the nitrate concentration in the effluent of treatment plants. The reduction of this coefficient by 20% for anoxic conditions reduces the nitrate concentration by 10 g N·m-3. It significantly improves the accuracy of the predictions of nitrate concentrations in treated effluents compare to real data. Simulations with dual values (aerobic and anoxic conditions) for heterotrophic yield (modified ASM1) were then used to determine the practical daily aerobic time interval to meet a given nitrogen discharge objective. Finally, to support design decisions, the relevance of a pre-denitrification configuration in front of an intermittently aerated tank was studied. It is shown that when the load of BOD5 is below the conventional design value, a small contribution of the anoxic zone to nitrate removal occurs, except for over-aerated plants. When plants receive a higher load of BOD5, the modified ASM1 suggests that the anoxic zone has a higher contribution to nitrogen removal, for both correctly and over-aerated plants.

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          Most cited references26

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          The effect of temperature and carbon source on denitrification using volatile fatty acids

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            Biological nitrogen removal of high-strength ammonium industrial wastewater with two-sludge system.

            The biological nitrogen removal (BNR) process is the most common method for removing low quantities of ammonium from wastewater, but this is not the usual treatment for high-strength ammonium wastewater. The capacity to biologically remove the nitrogen content of a real industrial wastewater with a concentration of 5000 g N-NH(4)(+) L(-1) is demonstrated in this work. The experimental system used is based on a two-sludge system, with a nitrifying activated sludge and a denitrifying activated sludge. This system treated real industrial wastewater for 450 days, and during this period, it showed the capacity for oxidizing all the ammonium at average nitrification rates between 0.11 and 0.18 g N-NH(4)(+)g VSS(-1)d(-1). Two key process parameters were evaluated: the maximum nitrification rate (MNR) and the maximum denitrification rate (MDR). MNR was determined in continuous operation at three different temperatures: 15 degrees C, 20 degrees C and 25 degrees C, obtaining values of 0.10, 0.21 and 0.37 g N-NH(4)(+) g VSS(-1)d(-1), respectively. Complete denitrification was achieved using two different industrial carbon sources, one containing mainly ethanol and the other one methanol. The MDR reached with ethanol (0.64 g N-NO(x)(-) g VSS(-1)d(-1)) was about 6 times higher than the MDR reached with methanol (0.11g N-NO(x)(-)g VSS(-1)d(-1)).
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              Wastewater denitrification process—the influence of methanol and kinetic analysis

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                Author and article information

                Journal
                wsa
                Water SA
                Water SA
                Water Research Commission (WRC) (Pretoria, Gauteng, South Africa )
                0378-4738
                1816-7950
                January 2009
                : 35
                : 1
                : 103-109
                Affiliations
                [01] orgnameCemagref France
                [03] orgnameWTSim SARL France
                [04] orgnameEnvironment Canada Canada
                [05] orgnameCemagref France
                [02] orgnameCemagref France
                Article
                S1816-79502009000100013 S1816-7950(09)03500113
                7ea9fcd8-92f0-4adb-8a49-e28f0b47cf51

                This work is licensed under a Creative Commons Attribution 4.0 International License.

                History
                : 15 April 2008
                : 15 October 2008
                Page count
                Figures: 0, Tables: 0, Equations: 0, References: 26, Pages: 7
                Product

                SciELO South Africa


                anoxic heterotrophic growth yield,activated sludge,modelling,low temperature,denitrification rate

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