Evaluation of Alternative Electron Donors in Anoxic Moving Bed Biofilm Reactors (MBBRs) Configured for Post-Denitrification

2008 ◽  
Vol 2008 (13) ◽  
pp. 3180-3197
Author(s):  
Karen A. Bill ◽  
Charles B. Bott ◽  
Phill H. Yi ◽  
Celine Ziobro ◽  
Sudhir N. Murthy
2009 ◽  
Vol 60 (10) ◽  
pp. 2647-2657 ◽  
Author(s):  
K. A. Bill ◽  
C. B. Bott ◽  
S. N. Murthy

The effectiveness of four different electron donors, specifically methanol, ethanol, glycerol, and sulfide (added as Na2S), were evaluated in post-denitrifying bench-scale moving bed biofilm reactors (MBBRs). With the requirement for more wastewater treatment plants to reach effluent total nitrogen levels approaching 3 mg/L, alternative electron donors could promote more rapid MBBR startup/acclimation times and increased cold weather denitrification rates compared to methanol, which has been most commonly used for post-denitrification processes due to low cost and effectiveness. While the application of alternative substrates in suspended growth processes has been studied extensively, fixed film post denitrification processes have been designed to use primarily low yield substrates like methanol. Bench-scale MBBRs were operated continuously at 12°C, and performance was monitored by weekly sampling and insitu batch profile testing. Ethanol and glycerol, though visually exhibited much higher biofilm carrier biomass content, performed better than methanol in terms of removal rate (0.9 and 1.0 versus 0.6 g N/m2/day, respectively.) Maximum denitrification rate measurements from profile testing suggested that ethanol and glycerol (2.2 and 1.9 g N/m2/day, respectively) exhibited rates that were four times that of methanol (0.49 g N/m2/day.) Sulfide also performed much better than either of the other three electron donors with maximum rates at 3.6 g N/m2/day and with yield (COD/NO3-N) that was similar to or slightly less than that of methanol.


2021 ◽  
Vol 414 ◽  
pp. 125535
Author(s):  
Ellen Edefell ◽  
Per Falås ◽  
Elena Torresi ◽  
Marinette Hagman ◽  
Michael Cimbritz ◽  
...  

1992 ◽  
Vol 26 (3-4) ◽  
pp. 703-711 ◽  
Author(s):  
B. Rusten ◽  
H. Ødegaard ◽  
A. Lundar

A novel moving bed biofilm reactor has been developed, where the biofilm grows on small, free floating plastic elements with a large surface area and a density slightly less than 1.0 g/cm3. The specific biofilm surface area can be regulated as required, up to a maximum of approximately 400 m2/m3. The ability to remove organic matter from concentrated industrial effluents was tested in an aerobic pilot-plant with two moving bed biofilm reactors in series and a specific biofilm surface area of 276 m2/m3. Treating dairy wastewater, the pilot-plant showed 85% and 60% COD removal at volumetric organic loading rates of 500 g COD/m3h and 900 g COD/m3h respectively. Based on the test results, the moving bed biofilm reactors should be very suitable for treatment of food industry effluents.


2006 ◽  
Vol 40 (8) ◽  
pp. 1607-1615 ◽  
Author(s):  
Sari Luostarinen ◽  
Sami Luste ◽  
Lara Valentín ◽  
Jukka Rintala

2019 ◽  
Vol 163 ◽  
pp. 114851 ◽  
Author(s):  
F. Morgan-Sagastume ◽  
S. Jacobsson ◽  
L.E. Olsson ◽  
M. Carlsson ◽  
M. Gyllenhammar ◽  
...  

1993 ◽  
Vol 28 (10) ◽  
pp. 351-359 ◽  
Author(s):  
H. Ødegaard ◽  
B. Rusten ◽  
H. Badin

In 1988 the State Pollution Control Authority in Norway made recommendations regarding process designs for small wastewater treatment plants. Amongst these were recommendations for biological/chemical plants where biofilm reactors were used in combination with pretreatment in large septic tanks and chemical post treatment. At the same time the socalled “moving bed biofilm reactor” (MBBR) was developed by a Norwegian company. In this paper, experiences from a small wastewater treatment plant, based on the MBBR and on the recommendations mentioned, will be presented.


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