Use of down-flow hanging sponge (DHS) reactor as a promising post-treatment system for municipal wastewater

被引:49
作者
Mahmoud, Mohamed [1 ]
Tawfik, Ahmed [1 ,2 ]
EI-Gohary, Fatma [1 ]
机构
[1] Natl Res Ctr, Water Pollut Res Dept, Cairo, Egypt
[2] Egypy Japan Univ Sci & Technol EJust, Sch Energy Resources & Environm Engn, Alexandria, Egypt
关键词
Municipal wastewater treatment; DNS reactor; Organic loads; Kinetic modeling; Agricultural reuse; SEWAGE-TREATMENT SYSTEM; ROTATING BIOLOGICAL CONTACTOR; DEVELOPING-COUNTRIES; NITROGEN REMOVAL; DOMESTIC SEWAGE; UASB REACTOR; ANAEROBIC HYBRID; FILTER SYSTEM; SLUDGE; COMBINATION;
D O I
10.1016/j.cej.2011.01.019
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 the treatment of municipal wastewater to be used for irrigation using a technology that is robust and simple to operate with minimum energy consumption. In order to achieve these objectives, two treatment schemes have been investigated. The first scheme consisted of a hybrid up-flow anaerobic sludge blanket (HUASB) reactor followed by a down-flow hanging sponge (DHS) reactor. The second one consisted of a primary sedimentation tank (PST) followed by a DHS reactor. Both systems were fed continuously with raw municipal wastewater. The study lasted for more than 140 days, the results of which revealed that the efficiency of both systems was comparable with regard to carbonaceous and nitrogenous compounds removal. The average removal values of COD(total), COD(soluble), BOD(5total), TSS and TN in the first scheme were 90 +/- 4, 78 +/- 8, 95 +/- 2, 96 +/- 5 and 72 +/- 8%, respectively. However, the residual geometric mean of faecal coliform counts in the final effluent of the first treatment scheme was only 2.7 x 10(2) MPN/100 ml compared to 6.5 x 10(3) MPN/100 ml in the second treatment scheme. In general, available data proved that the DHS reactor can cope with higher organic loads. The performance of DHS reactor was quite good for carbonaceous organic matter and nitrogen removal even at high OLR of 4.8 kg COD/m(3) d. (C) 2011 Elsevier B.V. All rights reserved.
引用
收藏
页码:535 / 543
页数:9
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