Anaerobic/aerobic treatment of greywater via UASB and MBR for unrestricted reuse

被引:31
作者
Abdel-Shafy, Hussein I. [1 ]
Al-Sulaiman, Ahmed Makki [2 ,3 ]
Mansour, Mona S. M. [4 ]
机构
[1] Natl Res Ctr, Water Res & Polluted Control Dept, Cairo, Egypt
[2] Qadisiyah Univ, Minist Higher Educ & Sci Res, Al Diwaniyah, Iraq
[3] Cairo Univ, Fac Engn, Cairo, Egypt
[4] Egyptian Petr Res Inst, Anal & Evaluat Dept, Cairo, Egypt
关键词
anaerobic/aerobic treatment; greywater; membrane bioreactor; UASB; unrestricted water reuse; WASTE-WATER-TREATMENT; MEMBRANE BIOREACTOR; SYSTEMS; REACTOR;
D O I
10.2166/wst.2014.504
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The aim of the present study was to investigate the efficiency of integrated up-flow anaerobic sludge blanket (UASB) as anaerobic system followed by membrane bioreactor (MBR) as aerobic system for the treatment of greywater for unrestricted reuse. Pilot-scale UASB and MBR units were installed and operated in the NRC, Egypt. Real raw greywater was subjected to UASB and the effluent was further treated with microfiltration MBR. The necessary trans-membrane pressure difference is applied by the water head above the membrane (gravity flow) without any energy input. The average characteristics of the raw greywater were 95, 392, 298, 10.45, 0.4, 118.5 and 28 mg/L for total suspended solids (TSS), chemical oxygen demand (COD), biochemical oxygen demand (BOD), total phosphates, nitrates, oil and grease, and total Kjeldahl nitrogen (TKN), respectively. The pH was 6.71. The UASB treatment efficiency reached 19.3, 57.8, 67.5 and 83.7% for TSS, COD, BOD5 and oil and grease, respectively. When the UASB effluent was further treated with MBR, the overall removal rate achieved 97.7, 97.8, 97.4 and 95.8% for the same parameters successively. The characteristics of the final effluent reached 2.5, 8.5, 6.1, 0.95, 4.6 and 2.3 mg/L for TSS, COD, BOD, phosphates, oil and grease and TKN, respectively. This final treated effluent could cope with the unrestricted water reuse of local Egyptian guidelines.
引用
收藏
页码:630 / 637
页数:8
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