A laboratory sequencing batch reactor (SBR), integrating a novel filtration system, was used to treat wastewater from a cheese factory. For an average influent CODtot of 1,000 mg l−1 and at an HRT of 8 d, the SBR-Filtration system yielded an overall efficiency of 94.5% in terms of COD removal, and an effluent suspended solids (SS) concentration close to 0 mg l−1. Throughput fluxes as high as 443 l m-2 h−1 could be reached. No permanent clogging or decrease in permeability of the filtration step was observed over the 12 d testing period. The effect of solids concentration on filtration was assessed by increasing, stepwise, the MLSS concentration in successive stages. The food to microorganism ratio (F/M) was maintained almost constant by increasing the influent load proportionately to the increase in biomass. This was done by adding powdered milk waste to the real wastewater. As a result of rapid increases in influent COD, changes in composition and loading rates, and a lack of nutrients during this phase of experiments, steady state conditions were interrupted. Consequently, the biomass would not flocculate well and the SVI increased. The decrease in filtration efficiency was thought to be due to the transient biological state of the biomass, rather than to the concentration increase itself. An attempt to corroborate this observation was made by systematically decreasing the mixed liquor concentration in the reactor by dilution with water. Flux rates remained constant, regardless of the variation of MLSS concentration.
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