초록
본 연구에서는 폐기물 자원화 공정에서 발생하는 음폐수를 UF 분리막을 결합한 혐기성 소화 파일럿 에서 처리하면서 혐기성 소화효율, 바이오가스 생산량과 운전인자를 도출하였다. 운전방식은 막내부에서 외부로 고액분리가 이루어지는 가압식이었으며, 투과 플럭스는 15∼20 LMH, 막간 차압은 $1{\sim}3 kgf/cm^2$였다. 분리막 운전은 직접순환방식으로 운전한 결과, 메탄조의 수질악화로 간접순환방식으로 운전하였다. 유입수의 TCOD 와 SCOD 는 각각 113 g/L, 62 g/L 이었고, 유출수의 TCOD 와 SCOD는 각각 25 g/L, 12 g/L 이었다. TCOD 및 SCOD 제거효율은 각각 77% 및 81%였다. 하지만 UF 공정을 추가했을 때는 제거효율이 93% 및 86%로 증가하였다.
In this study, Anaerobic Membrane Bioreactor(AnMBR) treating food waste leachate was operated to investigate treatment efficiency of anaerobic process, operational parameters and production of biogas. AnMBR was operated under the condition of filtration type of inside-out mode. AnMBR was operated under the condition that range of permeate flux was from 15 to 20 LMH and range of transmembrane pressure was from 1 to $3 kgf/cm^2$. It was not good that AnMBR was performed under direct connection between anaerobic reactor and external UF module. so, this connection method changed to indirect connection using buffer tank was placed between anaerobic reactor and UF external module. TCOD and SCOD values were that influent were about 113 g/L, 62 g/L and effluent were 25 g/L, 12 g/L, respectively. also TCOD and SCOD removal efficiency were 77% and 81%, respectively. but after added UF process, COD and SCOD removal efficiency was increased to 93% and 86%, respectively.
