Start-up, Optimization, and Performance Testing of a 77 MGD Integrated Fixed Film Activated Sludge (IFAS) Process to Meet a 5 mg/L Nitrogen Limit

2013 ◽  
Vol 2013 (13) ◽  
pp. 3886-3910
Author(s):  
David Michelsen ◽  
David Peterson ◽  
Michael Wilson ◽  
Joshua P. Boltz ◽  
Theresa Cote ◽  
...  
2013 ◽  
Vol 2013 (13) ◽  
pp. 3861-3885
Author(s):  
David Michelsen ◽  
David Peterson ◽  
Michael Wilson ◽  
Joshua P. Boltz ◽  
Theresa Cote ◽  
...  

2018 ◽  
Vol 11 (6) ◽  
pp. 891-905 ◽  
Author(s):  
Ryan Scott ◽  
Aibin Zhan ◽  
Emily A. Brown ◽  
Frédéric J. J. Chain ◽  
Melania E. Cristescu ◽  
...  

2015 ◽  
Vol 72 (10) ◽  
pp. 1840-1850 ◽  
Author(s):  
Nitin Kumar Singh ◽  
Absar Ahmad Kazmi ◽  
Markus Starkl

The present study summarizes the start-up performance and lessons learned during the start-up and optimization of a pilot-scale plant employing integrated fixed film activated sludge (IFAS) process treating actual municipal wastewater. A comprehensive start-up was tailored and implemented to cater for all the challenges and problems associated with start-up. After attaining desired suspended biomass (2,000–3,000 mg/L) and sludge age (∼7 days), the average biological oxygen demand (BOD) and chemical oxygen demand (COD) removals were observed as 77.3 and 70.9%, respectively, at optimized conditions, i.e. hydraulic retention time (HRT), 6.9 h; return sludge rate, 160%. The influent concentrations of COD, BOD, total suspended solids, NH3-N, total nitrogen and total phosphorus were found to be in the range of 157–476 mg/L, 115–283 mg/L, 152–428 mg/L, 23.2–49.3 mg/L, 30.1–52 mg/L and 3.6–7.8 mg/L, respectively, and the minimum effluent concentrations were achieved as ∼49 mg/L, 23 mg/L, 35 mg/L, 2.2 mg/L, 3.4 mg/L and 2.8 mg/L, respectively, at optimum state. The present system was found effective in the removal of pathogenic bacteria (Escherichia coli, 79%; Salmonella spp., 97.5%; Shigella spp., 92.9%) as well as coliforms (total coliforms, 97.65%; faecal coliforms, 80.35%) without any disinfection unit. Moreover it was observed that the time required for the stabilization of the plant was approximately 3 weeks if other parameters (sludge age, HRT and dissolved oxygen) are set to optimized values.


1999 ◽  
Vol 09 (PR3) ◽  
pp. Pr3-71-Pr3-76 ◽  
Author(s):  
M. Romero ◽  
V. Fernández ◽  
M. Sánchez

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