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입자상 알루미늄과 입자상 철 충전복극조에 의한 음식물쓰레기 배출수 전해처리
김정섭,박숭조 東亞大學校 附設 環境問題硏究所 2008 硏究報告 Vol.29 No.1
In case of electrolytic treatment of waste food effluent for 150 minute at 7V with a bipolar packecl bed cell loaded with granular aluminum, removal efficiency of COD, NaCl, T-N and T-P were 66.4, 66.5, 58.2 and 77.0 %. When electrolytic treating of waste food effluent for 150 minute at 7V with a BPBC loaded with granular iron removal efficiency of COD, NaCl, T-N and T-P were 80.3, 65.7, 59.3 and 67.2 %. We confirmed that optimum cell voltage of BPBC with filled granular aluminum or granular iron for electrolytic treating of waste food effluent was 7V. And Charge loading rate was 200 F/m3in BPBC filled with granular iron and granular aluminum and removal efficiency of COD, NaCl, TSS, Turbidity, T-N and T-P were 71.1, 66.4, 94.7, 89.1, 58.2, and 77.1%.
입자상 알루미늄과 입자상 철 충전복극조에 의한 음식물쓰레기 배출수 전해처리
김정섭,박숭조 동아대학교 환경문제연구소 2008 硏究報告 Vol.30 No.1
In case of electrolytic treatment of waste food effluent for 150 minute at 7V with a bipolar packecl bed cell loaded with granular aluminum, removal efficiency of COD, NaCl, T-N and T-P were 66.4, 66.5, 58.2 and 77.0 %. When electrolytic treating of waste food effluent for 150 minute at 7V with a BPBC loaded with granular iron removal efficiency of COD, NaCl, T-N and T-P were 80.3, 65.7, 59.3 and 67.2 %. We confirmed that optimum cell voltage of BPBC with filled granular aluminum or granular iron for electrolytic treating of waste food effluent was 7V. And Charge loading rate was 200 F/m3in BPBC filled with granular iron and granular aluminum and removal efficiency of COD, NaCl, TSS, Turbidity, T-N and T-P were 71.1, 66.4, 94.7, 89.1, 58.2, and 77.1%.