Aerobic digestion of starch wastewater in a fluidized bed bioreactor with low density biomass support.
A solid-liquid-gas, multiphase, fluidized bed bioreactor with low density particles was used in this study to treat the high organic content starch industry wastewater. The characteristics of starch wastewater were studied. It shows high organic content and acidic nature. The performance of a three phase fluidized bed bioreactor with low density biomass support was studied under various average initial substrate concentrations, by varying COD values (2250, 4475, 6730 and 8910 mg/L) and for various hydraulic retention times (8, 16, 24, 32 and 40 h) based on COD removal efficiency. The optimum bed height for the maximum COD reduction was found to be 80 cm. Experiments were carried out in the bioreactor at an optimized bed height, after the formation of biofilm on the surface of low-density particles (density=870 kg/m(3)). Mixed culture obtained from the sludge, taken from starch industry effluent treatment plant, was used as the source for microorganisms. From the results it was observed that increase in initial substrate concentration leads to decrease in COD reduction and COD reduction increases with increase in hydraulic retention time. The optimum COD removal of 93.8% occurs at an initial substrate concentration of 2250 mg/L and for the hydraulic retention time of 24h.
Rajasimman
M
M
Department of Chemical Engineering, Annamalai University, Annamalai Nagar, 608002 Tamil Nadu, India. raja_simms@yahoo.com
Karthikeyan
C
C
D001420:Bacteria, Aerobic / Q000378:metabolism*; D018533:Biomass; D019149:Bioreactors; D007220:Industrial Waste; D002365:Manihot; D013997:Time Factors; D014865:Waste Disposal, Fluid / Q000379:methods*; D014873:Water Pollutants / Q000737:chemistry*
D007220:Industrial Waste; D014873:Water Pollutants