Comparison of quasisteady-state performance of the DEAMOX process under intermittent and continuous feeding and different nitrogen loading rates

2007 ◽  
Vol 2 (7) ◽  
pp. 894-900 ◽  
Author(s):  
Sergey Kalyuzhnyi ◽  
Marina Gladchenko ◽  
Arnold Mulder ◽  
Bram Versprille
2020 ◽  
Vol 169 ◽  
pp. 115279 ◽  
Author(s):  
Wei Li ◽  
Jin-long Zhuang ◽  
Yuan-yuan Zhou ◽  
Fan-gang Meng ◽  
Da Kang ◽  
...  

1996 ◽  
Vol 191 (2) ◽  
pp. 321-322 ◽  
Author(s):  
J. Tober ◽  
C. Fritz ◽  
E. LaBrecque ◽  
P. J. Behr ◽  
I. Valiela

2020 ◽  
Vol 311 ◽  
pp. 123521 ◽  
Author(s):  
Angélica Chini ◽  
Camila Ester Hollas ◽  
Alice Chiapetti Bolsan ◽  
Bruno Venturin ◽  
Gabriela Bonassa ◽  
...  

2012 ◽  
Vol 66 (12) ◽  
pp. 2630-2637 ◽  
Author(s):  
A. Mulder ◽  
A. I. Versprille ◽  
D. van Braak

The feasibility of sustainable nitrogen removal was investigated in a two stage biofilm configuration consisting of a MBBR (Moving Bed Biofilm Reactor) and a Deamox reactor (Biobed-EGSB). The MBBR is used for nitrification and the denitrifying ammonium oxidation (Deamox) is aimed at a nitrogen removal process in which part of the required nitrite for the typical anammox reaction originated from nitrate. Anaerobic pre-treated potato wastewater was supplied to a MBBR and Deamox reactor operated in series with a bypass flow of 30%. The MBBR showed stable nitrite production at ammonium-loading rates of 0.9–1.0 kg NH4-N/m3 d with ammonium conversion rates of 0.80–0.85 kg NH4-N/m3 d. The nitrogen-loading rate and conversion rate of the Deamox reactor were 1.6–1.8 and 1.6 kg N/m3 d. The maximum ammonium removal capacity in the Deamox reactor was 0.6 kg NH4-N/m3 d. The removal efficiency of soluble total nitrogen reached 90%. The Deamox process performance was found to be negatively affected during decline of the operating temperature from 33 to 22 °C and by organic loading rates with a chemical oxygen demand (COD)/NO2-N ratio >1.


1994 ◽  
Vol 121 (1) ◽  
pp. 175-185 ◽  
Author(s):  
P. Peckol ◽  
B. DeMeo-Anderson ◽  
J. Rivers ◽  
I. Valiela ◽  
M. Maldonado ◽  
...  

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