Experiences of nitrogen and phosphorus removal in deep-bed filters at henriksdal sewage works in Stockholm

1998 ◽  
Vol 37 (9) ◽  
pp. 193-200
Author(s):  
L. Jonsson

Deep-bed down-flow two-media filters were used in pilot plant studies with filtration of secondary settled wastewater. FeSO4 or FeCl5 was applied as a precipitation agent, and NaAc·3H2O was chosen as a carbon source when denitrification was desired. The concentration of PO4-P in the filtrate from the pilot plant study never exceeded 0.05 mg PO4-P/l when iron salts were dosed. The curves showing the concentration of P-tot and PO4-P in the filtrate as a function of the quotient between the dosage of iron and the concentration of PO4-P in the influent to the filter followed approximately an exponential relationship. The total nitrogen reduction over the filter bed increased from an average of 2.3 mg (NO3+NO2)-N/l at the beginning of each experiment to an average of 4.3 mg (NO3+NO2)-N/l towards the end of the test. When only secondary settled wastewater, suspended solids, primary settled wastewater, iron salts, or sodium acetate was added, at a hydraulic load of 10 m/h, the time before clogging became 100 h, 10–15 h, 20–40 h, respectively. Almost the entire pressure drop was located on the surface of the filter bed and 0.25 metre down in the expanded clay layer.

2013 ◽  
Vol 68 (2) ◽  
pp. 400-405 ◽  
Author(s):  
Min Pan ◽  
Tianhu Chen ◽  
Zhenhu Hu ◽  
Xinmin Zhan

Biological nitrogen and phosphorus removal was investigated in an intermittently aerated sequencing batch reactor (IASBR) and a sequencing batch reactor (SBR). The removal efficiencies of ammonium-nitrogen (NH4+-N) were 100% in both reactors in steady operation state. The total nitrogen (TN) removal efficiencies were 90.4% in the IASBR and 79.3% in the SBR, while the total phosphorus (TP) removal efficiencies were 88.8% in the IASBR and 82.3% in the SBR. The efficiencies of simultaneous nitrification and denitrification (SND) were 90.4% in the IASBR and 79.3% in the SBR, indicating that the IASBR was more efficient than the SBR in SND. The sludge in the IASBR had a P release capability of 16.6 mg P/g VSS (volatile suspended solids) but only 7.5 mg P/g VSS in the SBR.


2012 ◽  
Vol 518-523 ◽  
pp. 2980-2985
Author(s):  
Qiong Wan ◽  
Qian Feng ◽  
Dang Cong Peng ◽  
Shi Ping Jing

The volume ratio of anaerobic/anoxic/aerobic was an important factor for the removal of nitrogen and phosphorus in the A2/O process. A pilot plant of A2/O process was built in Xi’an to do the research about the influence on nitrogen and phosphorus removal when the volume ratio of anaerobic/anoxic/aerobic was changed. When the HRT was 10.1h and the volume rate of anaerobic/anoxic/aerobic was 1/1.7/2.4, the removal rate of COD didn’t raise substantially than that of normal volume ratio A2/O process, the removal rate average value of TN and phosphorus were 61.5% and 85.4% respectively. On this condition, the HRT in aerobic zone shorted to 4.7h, energy was saved about 33.8% in comparing with that of conventional volume ratio A2/O process.


1997 ◽  
Vol 35 (1) ◽  
pp. 145-152 ◽  
Author(s):  
Y. Hamamoto ◽  
S. Tabata ◽  
Y. Okubo

Technology to simultaneously remove nitrogen and phosphorus from wastewater by carrying out aerobic and anaerobic operations in a single reactor has been developed by the authors. The Intermittent Cyclic Process can be used with two reactors, operating at opposite stages, to receive and treat influent on an uninterrupted basis. Research has been carried out in the: laboratory; pilot plant; and in a 540 m3 full scale wastewater plant. Experiments with aeration time ratios (aeration time to total cycle time) from 0.125 to 1 have been made, and 0.125 yielded the best nitrogen and phosphorus removal results in the laboratory study. In the pilot plant average nitrogen and phosphorus removal rates of 86% and 82% were achieved. In over three years of operation, the full-scale plant realized rates of 87% and 74% respectively. Performance has further improved with our recently developed controller which uses “fuzzy logic” to automatically determine optimal mixing and aeration periods. Measurements of DO, pH, ORP, and reactor water level are constantly relayed to the fuzzy controller. Average nitrogen and phosphorus removal rates in the full-scale plant were 96% and 93%. The study demonstrates that the fuzzy controller is practical and enhances nitrogen and phosphorus removal.


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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