ANAEROBIC DEGRADATION OF CORNSTARCH IN WASTE-WATER IN 2 UPFLOW REACTORS

Wastewater containing high concentrations of cornstarch was treated in two 8.5-L, upflow reactors: upflow anaerobic sludge blanket (UASB) an d a modified anaerobic filter (AF). Both reactors were operated in par allel at 37 degrees C and pH 6.8-7.9 over 510 d with increased loading s of chemical oxygen demand (COD). Results showed that, in spite of ha ving different sludge concentration profiles, both reactors, with 12 h of hydraulic retention time, removed an average of 95.3% of COD from wastewater containing up to 45,000 mg-COD . L(-1) (loading rates up to 90 g-COD . L(-1) . d(-1)). At loading rates up to 75 g-COD . L(-1) . d(-1), only 0.42% and 0.80% of starch particulates remained unhydrolyz ed and were washed out by the effluent from UASB and modified AF react ors, respectively. Of the COD removed, 85.9% was converted to methane and the rest was converted to biomass with a net sludge yield of 0.10 g-VSS . g-COD-1. Both reactors failed at loading rates higher than 90 g-COD . L(-1) . d(-1), because of severe washout of solids. The sludge granules had a methanogenic activity of 1.90-1.92 g-methane-COD . g-V SS-1 . d(-1) and consisted of various trophic bacteria in the order of 10(8)-10(9) m/L.