Journal of Industrial and Engineering Chemistry, Vol.12, No.3, 489-493, May, 2006
WastewaterTreatment by Anaerobic Digestion Coupled with Membrane Processing
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Treatment of starch waste by an anaerobic digester-membrane system was studied. The starch waste was immersed into a hollow fiber membrane unit, of area 0.17 m2, with themembrane pore size varying from 0.03 to 0.15 μm. The hydraulic retention time (HRT) of the anaerobic digester ranged from 1.5 to 10 days and this variation had a significant effect on the treatment efficiency; in contrast, whereas the membrane size had no significant effect. The gas production was ca. 0.74 m3/kg chemical oxygen demand (COD) treated. The COD removal efficiency was ca. 80∼ 95 %, depending on the HRT. The effluent from the anaerobic filter, having a total COD in the range 4500 ∼ 5200 mg/L, was treated by crossflow ultrafiltration (UF) units. Experiments performed with different membrane pore sizes indicated that a membrane with a molecular weight cut-off (MWCO) size of 106 showed a higher COD removal efficiency in the range of 83∼ 87 %, while maintaining a steady flux of 120 130 L/m2h. The scope of this study scope was also expanded to investigate the long term clogging effect of the membrane.
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