Application of Swim-bed Technology to Enhance Sludge Characteristics of Activated Sludge Process

Biofringe (BF) carrier material creates swimming motion due to velocity of downflow wastewater, a characteristic of swim-bed technology, and provides a high degree of substrate-biomass contact. In this study, BF fiber material was packed in a plug-flow activated sludge reactor, to investigate its feasibility in improving the sludge settleability and enhancing the pollutant degradation performance of the activated sludge process. High SBOD 5 , SCOD, and ammonium removal efficiencies of 99.1%, 96.5% and 83.6%, respectively were obtained at volumetric loading rate of 4.5 kg–SCOD/m 3 /d. SVI values below 50 m l /g and high settling velocities demonstrated satisfactory settling characteristics of the biomass, which were attributed to the increase in the size of the biomass flocs as a result of use of BF carrier material. Relatively low viscosity of mixed liquor also facilitated sludge settling performance as no sludge bulking problems were encountered throughout the experimental period. Existence of a large amount of protozoa and metazoa observed through microscopic examination was considered to contribute to the low sludge yield compared to conventional activated sludge. Microbial analysis demonstrated microbial community shift between the seed sludge and the sludge sample after 378 days of operation with proteobacteria to be predominant. The results demonstrated that use of swim-bed technology enhanced treatment performance and provided process stability to the conventional activated sludge process.

[1]  S. Judd,et al.  Sludge characteristics and membrane fouling in full-scale submerged membrane bioreactors , 2008 .

[2]  M. Fujita Development of Nitrification Model Using Molecular Techniques , 2008 .

[3]  Christelle Wisniewski,et al.  Physical properties of activated sludge in a submerged membrane bioreactor and relation with membrane fouling , 2007 .

[4]  T. Mino,et al.  Temporal Variation in Maximum Cell-Specific Nitrification Rates in Municipal Wastewater Treatment Plant and Controlling Factors , 2007 .

[5]  K. Furukawa,et al.  Evaluation of the Swim-Bed Attached-Growth Process for Nitrification of Hanoi Groundwater Containing High Levels of Iron , 2005 .

[6]  Joo-Hwa Tay,et al.  Responses of sludge flocs to shear strength , 2005 .

[7]  J. Rouse,et al.  Swim-bed Technology as an Innovative Attached-growth Process for High-rate Wastewater Treatment , 2004 .

[8]  D. Eikelboom,et al.  Minimization of excess sludge production for biological wastewater treatment. , 2003, Water research.

[9]  A. Tunnacliffe,et al.  Reduction of suspended biomass in municipal wastewater using bdelloid rotifers. , 2003, Water research.

[10]  A. Bollmann,et al.  Growth at Low Ammonium Concentrations and Starvation Response as Potential Factors Involved in Niche Differentiation among Ammonia-Oxidizing Bacteria , 2002, Applied and Environmental Microbiology.

[11]  E R Cornelissen,et al.  Wastewater treatment with the internal MEMBIOR. , 2002, Mededelingen.

[12]  Willy Verstraete,et al.  Reduced sludge production in a two-stage membrane-assisted bioreactor , 2000 .

[13]  R. Canziani,et al.  Pilot-plant experiments with moving-bed biofilm reactors , 1997 .

[14]  J. Kanda Determination of ammonium in seawater based on the indophenol reaction with o-phenylphenol (OPP) , 1995 .

[15]  J. Swings,et al.  Reclassification of Xanthomonas , 1995 .

[16]  A. Uitterlinden,et al.  Profiling of complex microbial populations by denaturing gradient gel electrophoresis analysis of polymerase chain reaction-amplified genes coding for 16S rRNA , 1993, Applied and environmental microbiology.

[17]  Makram T. Suidan,et al.  Anaerobic treatment of phenol by an expanded-bed reactor , 1986 .