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KMID : 0382419980240010132
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Korean Journal of Environmental Health Society
1998 Volume.24 No. 1 p.132 ~ p.140
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Integrated System of RBC-Lime Precipiatation for Simultaneous Removal of Organics and Nutrients
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Park Jong-An
Son Bu-Soon
Hur Joon-Moo
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Abstract
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Laboratory-scale experiments were conducted using a three-stage rotating biological contactor unit followed by lime precipitation and sedimentation with effluent recycle to the first stage. The purpose of this study was to evaluate the effects of hydraulic loadings of 0.031~0.076 ㎥/㎡/d and recycle ratio of 1 to 3 on the simultaneous removal of organics and nutrients from domestic wastewater. Lime was added to maintain pH of 10.4~11.0 in the coagulation-flocculation reactor.
Results showed that the highest nitrogen removal rate of 70.5% occurred at the lower hydraulic loading of 0.031 ㎥/㎡/d at a recirculation rate of 300%, and similarly, highest nitrification occurred at the same hydraulic loading and recycle ratio. Concentration of ammonia nitrogen in the effluent was less than 1 mg/ℓ at the same operating conditions for higher nitrogen removal. Whereas, high BOD and COD removal was observed at hydraulic loading rate of 0.054 ㎥/㎡/d, and high removal of organic matter was evident from the consistent low COD and BOD value. Results obtained from the operating condition of higher loading rate, 300% of recycle rate showed the highest removals. Increasing in recycle rate and hydraulic loading rate increased the volatile solids fraction of the sludges generated to the extent of 47% at 0.076 ㎥/㎡/d, hydraulic loading and 300% recirculation rate. Since pH in the flocculator was maintained at the pH of 10.4~11.0, above 90% removal of phosphorus was obtained. Average concentration of suspended solids was always maintained over 40 mg/ℓ in the effluent. Therefore an RBC unit operating at a hydraulic loading near 0.031 ㎥/㎡/d with a recycle rate of 300% is a viable and feasible alternate conditions to produce an effluent with relative low organic matter and phosphorus, provided that there is a neutralization unit to control the pH and SS of the effluent.
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