Development of a novel denitrifying phosphorus removal and partial denitrification anammox (DPR + PDA) process for advanced nitrogen and phosphorus removal from domestic and nitrate wastewaters

2021 ◽  
Vol 327 ◽  
pp. 124795
Author(s):  
Peng Wu ◽  
Xingxing Zhang ◽  
Yuguang Wang ◽  
Chaochao Wang ◽  
Liping Ma ◽  
...  
2013 ◽  
Vol 401-403 ◽  
pp. 2084-2087
Author(s):  
Ming Fen Niu ◽  
Si Li ◽  
Hong Jing Jiao ◽  
Jian Wei ◽  
Yuan Yang Sun ◽  
...  

Denitrifying phosphorus removal can be achieved with the same matrix simultaneous nitrogen and phosphorus removal,is a hot topic of abroad study biological wastewater treatment,This is discussed the Influence factors of anoxic tank NO3- load, dissolved oxygen and the volume ratio of aerobic tank and anoxic tank, pH value of wastewater, sludge retention time (SRT), hydraulic retention time (HRT), mixed liquor suspended solids (MLSS) and temperature on denitrifying phosphorus removal, for denitrifying phosphorus removal process simulation, experimental research and practical application provides a reference and basis.


Author(s):  
Shao Po Wang ◽  
Jing Jie Yu ◽  
Fan Kai Su ◽  
Fu Gao ◽  
Li Ping Sun

Abstract This study investigated the influence of the unique internal recirculation characteristics of an oxidation ditch (OD) system, namely, the internal recirculation frequency (IRF) on denitrifying phosphorus removal (DNPR). The ratios of denitrifying polyphosphate-accumulating organisms (DPAOs) to polyphosphate-accumulating organisms (PAOs) under different IRF conditions were measured using a batch experiment. On this basis, the variation of nutrient transformations were studied using the IRF changes by the mass balance method. The results showed that for the OD system that had an anaerobic zone upstream from the circular corridor and set anoxic and aerobic zones along the circular corridor, when the IRF was between 3.4 h−1 and 7.5 h−1, the DPAOs/PAOs ratio reached about 50%. Approximately 20% of the total phosphorus (TP) was removed and over 11% of the total nitrogen (TN) was transformed into nitrogen gas by the DNPR process, and meanwhile the total removal efficiencies of the TP and TN were over 93% and 80%. When the IRF was greater than 11.5 h−1, the TN removal efficiency decreased significantly, and this was not conducive to simultaneous nitrogen and phosphorus removal. The results indicated that OD process would possess a better DNPR potential if the IRF was controlled within the proper scope.


2016 ◽  
Vol 18 (2) ◽  
pp. 251-258 ◽  

<div> <p>Denitrifying polyphosphate accumulating organisms (DNPAOs) are very promising for simultaneous nitrogen and phosphorus removal. While during denitrification, emission of a greenhouse gas, nitrous oxide (N<sub>2</sub>O), may occur. In this study, DNPAOs were enriched in a lab-scale reactor, and N<sub>2</sub>O emission was examined under different electron acceptor conditions. During the anoxic phase, with the uptake of phosphorus, denitrification of nitrate nitrogen (NO<sub>3</sub>-N) was observed without the accumulation of nitrite nitrogen (NO<sub>2</sub>-N). In general, a very low amount of N<sub>2</sub>O was produced with nitrate as the electron acceptor, independent of the applied different nitrate concentrations. However, with nitrite as the electron acceptor, a much higher N<sub>2</sub>O emission occurred. The N<sub>2</sub>O emission factor to the denitrified NO<sub>2</sub>-N was 6.2%, 5.3% and 4.9% at the initial NO<sub>2</sub>-N concentration of 10, 20 and 40 mg l<sup>-1</sup>, respectively. In addition, a much higher N<sub>2</sub>O emission occurred with the co-existence of NO<sub>3</sub>-N and NO<sub>2</sub>-N. The initial organic carbon concentration had no significant effect on N<sub>2</sub>O emission with NO<sub>3</sub>-N as the electron acceptor. When stored organic carbon by DNPAOs was used as the electron donor, N<sub>2</sub>O emission was mainly dependent on the electron acceptor.&nbsp;</p> </div> <p>&nbsp;</p>


2017 ◽  
Vol 14 (2) ◽  
pp. 99-106 ◽  
Author(s):  
Zhengan Zhang ◽  
Shulin Pan ◽  
Fei Huang ◽  
Xiang Li ◽  
Juanfang Shang ◽  
...  

2004 ◽  
Vol 31 (4) ◽  
pp. 349-356
Author(s):  
Li Na ◽  
Li Zhidong ◽  
Li Guode ◽  
Wang Yan ◽  
Wu Shiwei ◽  
...  

2000 ◽  
Vol 41 (9) ◽  
pp. 139-145
Author(s):  
R. Kayser

The German design guideline A 131 “Design of single stage activated sludge plants” was amended in 1999. The main changes of the guideline from 1991 are outlined. The design procedure for plants with nitrogen and phosphorus removal is presented.


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