Application of microfiltration systems coupled with powdered activated carbon to river water treatment

被引:39
作者
Kim, Han-Seung
Takizawa, Satoshi
Ohgaki, Shinichiro
机构
[1] Myongji Univ, Div Environm Engn & Biotechnol, Yongin, South Korea
[2] Univ Tokyo, Dept Urban Engn, Tokyo 1138656, Japan
关键词
microfiltration; activated carbon; membrane; water reuse; organic removal; advance water treatment;
D O I
10.1016/j.desal.2005.12.064
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A bench scale submerged microfiltration system coupled with high concentration of PAC (powdered activated carbon) was applied in order to purify a river water containing secondary effluent. The system was operated with four different modes: Run-1, -2, -3 and -4. The PAC concentration was set at 0, 4 and 40 g/L with same filtration rate of 1.0 m/d (42 L/m(2)/h) which correspond to Run-1, -2 and -3. In Run-4, the filtration rate was set at 0.5 m/d (21 L/m(2)/h) with PAC concentration of 40 g/L. The effluent turbidity showed below 0.1 NTU for all runs, and the removal rates more than 90% were observed. As for TOC removal, almost no removal of TOC was observed in Run-1 while the higher removal rates were obtained with the higher dosage of powdered activated carbon. Run-3 and 4 with PAC dose of 40 g/L showed the removal of 85% regardless of the filtration rates. Removal of UV254 was similar to that of TOC: removal of 13% at Run-1 and 90% at Run-3 and -4. As for the filtration efficiency, an average filtration time for TMP to reach 60 kPa was checked for each runs. The filtration time of around 5 days was observed in Run-1 and Run-2, 2 days in Run-3 and 60 days in Run-4. According to the results, the effluent water quality got better with higher dose of PAC and the filtration efficiency was enhanced with higher dose of PAC and lower filtration time.
引用
收藏
页码:271 / 277
页数:7
相关论文
共 11 条
[1]   Treatment of domestic wastewater using microfiltration for reuse of wastewater [J].
Ahn, KH ;
Song, KG .
DESALINATION, 1999, 126 (1-3) :7-14
[2]   Interactions between natural organic matter (NOM) and membranes: Rejection and fouling [J].
Amy, G ;
Cho, J .
WATER SCIENCE AND TECHNOLOGY, 1999, 40 (09) :131-139
[3]   Immersed membrane filtration for the production of drinking water: Case studies [J].
Cote, P ;
Mourato, D ;
Gungerich, C ;
Russell, J ;
Houghton, E .
DESALINATION, 1998, 117 (1-3) :181-188
[4]  
FUKUSHIMA T, 1997, J JPN SOC WATER ENV, V20, P397
[5]   The application of membrane technology for water disinfection [J].
Madaeni, SS .
WATER RESEARCH, 1999, 33 (02) :301-308
[6]   Ultra- and microfiltration pilot plant investigations to treat reservoir water [J].
Panglisch, S ;
Dautzenberg, W ;
Kiepke, O ;
Gimbel, R ;
Gebel, J ;
Kirsch, A ;
Exner, M .
DESALINATION, 1998, 119 (1-3) :277-287
[7]   Ammonia oxidation at low temperature in a high, concentration powdered activated carbon membrane bioreactor [J].
Seo, G ;
Takizawa, S ;
Ohgaki, S .
2ND WORLD WATER CONGRESS: DRINKING WATER TREATMENT, 2002, 2 (02) :169-176
[9]   Removal of soluble organics and manganese by a hybrid MF hollow fiber membrane system [J].
Suzuki, T ;
Watanabe, Y ;
Ozawa, G ;
Ikeda, S .
DESALINATION, 1998, 117 (1-3) :119-129
[10]   Ultrafiltration as an advanced tertiary treatment process for municipal wastewater [J].
Tchobanoglous, G ;
Darby, J ;
Bourgeous, K ;
McArdle, J ;
Genest, P ;
Tylla, M .
DESALINATION, 1998, 119 (1-3) :315-321