The Treatment of Industrial Wastewater by the Fluidized-Bed Biofilm Reactor

미생물막 유동층 반응기를 이용한 산업폐수 처리에 관하여

Substrate removal efficiency of industrial wastewater from dye plant was investigated with fluidized-bed biofilm reactor(FBBR). Wastewater was diluted by 2, 3 and 6 times for experiment. When F/M ratio was increased 0.2 to 0.3, substrate removal efficiency of wastewater was rapidly decreased in all dilution ratio. Substrate removal efficiency was increased with dilution ratio in same F/M ratio, with hydraulic retention time. In case of 6 times diluted wastewater, below 0.2 F/M ratio, removal efficiency of BOD was $90{\sim}97%$. For reactor design, the parameters such as Y, $k_d$ and r was obtained as follows: $Y=0.3365\;k_d=0.03782\;day^{-1}\;r=0.997$ in 2 times diluted $Y=0.3341\;k_d=0.02750\;day^{-1}\;r=0.996$ in 3 times diluted $Y=0.3365\;k_d=0.03434\;day^{-1}\;r=0.998$ in 6 times diluted

미생물막 유동층 반응기로 염료공장 폐수의 유기물 처리효율을 고찰하였다. 공장폐수를 2배, 3배 및 6배 희석하여 처리하였던 바, 각 희석배율 모두 F/M비가 0.2에서 0.3으로 증가할 때 처리효율이 급격히 낮아졌다. 한편, 같은 F/M비에서는 희석율이 높을수록 처리효율이 높았으며 수리학적 체류시간이 증가함에 따라서 처리효율도 증가하였다. 6배 희석시 F/M비가 0.2 이하에서 BOD 처리효율이 $90{\sim}97%$로 가장 좋았다. 또 반응기 설계를 위한 통역학적 계수 Y, $k_b$값 및 상관계수 r은 2배 희석시 $Y=0.3365\;k_d=0.03782\;day^{-1}\;r=0.997$, 3배 희석시 $Y=0.3341\;k_d=0.0275\;day^{-1}\;r=0.996$ 및 6배 희석시는 $Y=0.5460\;k_d=0.03434\;day^{-1}\;r=0.998$로 나타났다.