Effect of dynamic loading on biological nutrient removal in a pilot-scale liquid-solid circulating fluidized bed bioreactor.

A pilot-scale liquid-solid circulating fluidized bed (LSCFB) bioreactor was employed for biological nutrient removal from municipal wastewater at the Adelaide Pollution Control Plant, London, Ontario, Canada. Lava rock particles of 600 μm were used as a biomass carrier media. The system generated effluent characterized by <1.0 mg NH4 —N/L , <6.0 mg NO3 —N/L , <1.0 mg PO4 —P/L , <10 mg TN/L, and <10 mg SBOD/L at an influent flow of 5  m3 /d , without adding any chemicals for phosphorus removal and secondary clarification for suspended solids removal. The impact of the dynamic loading on the LSCFB effluent quality and its nutrient removal efficiencies were monitored by simulating wet weather condition at a maximum peaking factor of 3 for 4 h. The achievability of effluent characteristics of 1.1 mg NH4 —N/L , 4.6 mg NO3 —N/L , 37 mg COD/L, and 0.5 mg PO4 —P/L after 24 h of the dynamic loading emphasize the favorable response of the LSCFB to the dynamic loadings and the sustainability of performance without l...

[1]  Mogens Henze,et al.  The Activated Sludge Model No. 2: Biological Phosphorus Removal , 1995 .

[2]  B. Rusten,et al.  The innovative moving bed biofilm reactor/solids contact reaeration process for secondary treatment of municipal wastewater , 1998 .

[3]  G. Nakhla,et al.  Load maximization of a liquid-solid circulating fluidized bed bioreactor for nitrogen removal from synthetic municipal wastewater. , 2008, Chemosphere.

[4]  W. Shieh,et al.  Evaluation of intrinsic and inhibition kinetics in biological fluidized bed reactors , 1995 .

[5]  M. Dahab,et al.  Nitrate removal characteristics of high performance fluidized-bed biofilm reactors. , 2004, Water research.

[6]  Michael K Stenstrom,et al.  Oxygen transfer in a full-depth biological aerated filter. , 2008, Water environment research : a research publication of the Water Environment Federation.

[7]  Poul Harremoës,et al.  Hydrolysis of organic wastewater particles in laboratory scale and pilot scale biofilm reactors under anoxic and aerobic conditions , 1998 .

[8]  H. D. Stensel,et al.  Wastewater Engineering: Treatment and Reuse , 2002 .

[9]  Glen T. Daigger,et al.  Biological wastewater treatment. , 2011 .

[10]  W. Gujer,et al.  Activated sludge model No. 3 , 1995 .

[11]  T. Stephenson,et al.  Performance of floating and sunken media biological aerated filters under unsteady state conditions , 1999 .

[12]  V. Borregaard Experience with nutrient removal in a fixed-film system at full-scale wastewater treatment plants , 1997 .

[13]  J. P. Steyer,et al.  Modeling and experiments on the influence of biofilm size and mass transfer in a fluidized bed reactor for anaerobic digestion , 1998 .

[14]  David J. Sample,et al.  Research Needs in Urban Wet Weather Flows , 1999 .

[15]  S. Dentel,et al.  Simultaneous nitrification-denitrification in a fluidized bed reactor , 1998 .

[16]  Derin Orhon,et al.  Metabolic model for acetate uptake by a mixed culture of phosphate‐ and glycogen‐accumulating organisms under anaerobic conditions , 2003, Biotechnology and bioengineering.

[17]  M. Gómez,et al.  Influence of hydraulic loading and air flowrate on urban wastewater nitrogen removal with a submerged fixed-film reactor. , 2003, Journal of hazardous materials.

[18]  Solids routing in an activated sludge process during hydraulic overloads , 1996 .

[19]  F. J. Morales,et al.  Operational Optimisation of Pilot Scale Biological Nutrient Removal at the Ciudad Real (Spain) Domestic Wastewater Treatment Plant , 2004 .

[20]  Jesse Zhu,et al.  Simultaneous carbon, nitrogen and phosphorous removal from municipal wastewater in a circulating fluidized bed bioreactor. , 2006, Chemosphere.

[21]  Nabin Chowdhury,et al.  Pilot‐scale Experience with Biological Nutrient Removal and Biomass Yield Reduction in a Liquid‐solid Circulating Fluidized Bed Bioreactor , 2010, Water environment research : a research publication of the Water Environment Federation.

[22]  G. Nakhla,et al.  Simultaneous Carbon and Nitrogen Removal in Anoxic-Aerobic Circulating Fluidized Bed Biological Reactor (CFBBR) , 2004, Environmental technology.

[23]  Kelley Oj Agency for International Development. , 1973 .

[24]  O. O'Nagy,et al.  Modelling and dynamic simulation of a moving bed bioreactor using respirometry for the estimation of kinetic parameters , 2007 .

[25]  J. Bolton,et al.  Procedure to Quantify Biofilm Activity on Carriers used in Wastewater Treatment Systems , 2006 .

[26]  C. W. Randall,et al.  Performance of IFAS wastewater treatment processes for biological phosphorus removal. , 2005, Water research.

[27]  G. H. Nancollas,et al.  The growth of nonstoichiometric apatite from aqueous solution at 37°C , 1990 .

[28]  J J Heijnen,et al.  A structured metabolic model for anaerobic and aerobic stoichiometry and kinetics of the biological phosphorus removal process , 1995, Biotechnology and bioengineering.

[29]  Max Maurer,et al.  Kinetics of biologically induced phosphorus precipitation in waste-water treatment , 1999 .

[30]  Daniel A. Okun,et al.  Guidelines for water reuse. , 1992 .

[31]  P. Cooper,et al.  Biological Nutrient Removal: Design Snags, Operational Problems and Costs , 1995 .

[32]  J J Heijnen,et al.  Wastewater treatment with particulate biofilm reactors. , 2000, Journal of biotechnology.