There is a strong interest in biological processes for drinking water treatment stemming from recent regulations on pathogenic protozoa and disinfection by-products. By operation of filters in the biological mode, it is possible to obtain a water with low assimilable organic carbon (AGC) and hence prevent significant growth of biofilms in the distribution systems. Since granular activated carbon (GAC) biological filters accumulate both biological and non-biological particles on the filter bed, the differences in the detachment of these groups of particles during backwashing will be an important aspect of operation of these filters.
Principal Investigator: A. Amirtharajah (Georgia Institute of Technology)
Principal Investigator: Rasheed Ahmad (Georgia Institute of Technology)
Sponsor: GWRI
Start Date: 1994-04-01; Completion Date: 1996-03-01;
Keywords: Water Treatment, Biofilms, Microbial Detachment, Hydrophobicity, Hydrophobic Interaction, Biological Filtration, Backwashing, Bed Expansions, Air Scour
Description:
There is a strong interest in biological processes for drinking water treatment stemming from recent regulations on pathogenic protozoa and disinfection by-products. By operation of filters in the biological mode, it is possible to obtain a water with low assimilable organic carbon (AGC) and hence prevent significant growth of biofilms in the distribution systems. Since granular activated carbon (GAC) biological filters accumulate both biological and non-biological particles on the filter bed, the differences in the detachment of these groups of particles during backwashing will be an important aspect of operation of these filters. The objectives of present study include determination of effluent quality of biological filters, comparison of biological particle detachment with non-biological particles during filter backwashing, determination of the impact of different fluidized bed expansions on bacterial detachment, impact of water wash by fluidization, air scqur and chlorinated backwash on filtration performance and analysis of these experimental results in terms of a microscopic force model. The filtration and backwashing experiments were completed in a packed glass column with GAC/sand media and an indigenous bacterial population. The operation of a biological filter was simulated by using filter influent water from the nearby Water Treatment Plant with the addition of a carbon source. In biological filters, the effluent microbial counts were considerably higher than that of influent. To develop a valid microscopic force model for microbial detachment, the hydrophobic force must be included in the total force calculations. Hydrophobic colloids produce a deeper primary minimum as compared to hydrophilic colloids. Consequently, hydrophobic bacteria are far more strongly attached to the GAC surface as compared to hydrophilic clay particles. During backwash of a biological filter, the maximum turbidity occurs close to zero time in contrast to the maximum microbial detachment which occurs later. A sixty percent bed expansion produced maximum bacterial removal. Water washed filters even at optimum porosity build up excessive headloss over successive filter runs. The biological filters backwashed with a combination of air plus subfluidization water flow at collapse-pulsing followed by water wash with 20% bed expansion produced not only lower headloss but also little headloss build up over successive runs.