The role of a combined coagulation and disk filtration process as a pre-treatment to microfiltration and reverse osmosis membranes in a municipal wastewater pilot plant

被引:28
作者
Chon, Kangmin [1 ,2 ]
Cho, Jaeweon [3 ]
Kim, Seung Joon [4 ]
Jang, Am [5 ]
机构
[1] Korea Inst Energy Res, Jeju Global Res Ctr, Jeju Si 695971, Jeju Do, South Korea
[2] Gwangju Inst Sci & Technol, Sch Environm Sci & Engn, Kwangju 500712, South Korea
[3] Yonsei Univ, Coll Engn, Dept Civil & Environm Engn, Seoul 120749, South Korea
[4] Kolon Global, Res & Business Dev Ctr, Environm Technol Res Lab, Yongin 449815, Gyeonggi Do, South Korea
[5] Sungkyunkwan Univ, Sch Civil & Architecture Engn, Suwon 440746, Gyeonggi Do, South Korea
基金
新加坡国家研究基金会;
关键词
Combined coagulation-disk filtration; Effluent organic matter; Microfiltration; Municipal wastewater reclamation; Reverse osmosis; NANOFILTRATION HYBRID SYSTEM; ORGANIC-MATTER; FOULING CHARACTERISTICS; ENDOCRINE DISRUPTORS; BORON REMOVAL; ULTRAFILTRATION; RECLAMATION; BIOREACTOR; REUSE; PHARMACEUTICALS;
D O I
10.1016/j.chemosphere.2014.05.042
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
pilot study was conducted to assess the performance of a municipal wastewater reclamation plant consisting of a combined coagulation-disk filtration (CC-DF) process, microfiltration (MF) and reverse osmosis (RO) membranes, in terms of the removal of water contaminants and changes in characteristics of effluent organic matter (EfOM). The CC-DF and MF membranes were not effective for the removal of dissolved water contaminants. However, they could partially reduce the turbidity associated with the cake layer formation by particulate materials on the membrane surfaces. Furthermore, most of water contaminants were completely removed by the RO membranes. Although the CC-DF process could remove approximately 20% of turbidity, the aluminium concentrations considerably increased after the CC-DF process due to the residual coagulants complexed with both carboxylic acid and alcohol functional groups of EfOM. Those aluminium-EfOM complexes had a lower negative charge and higher molecular weight (>0.1 mu m pore size of the MF membranes) compared to non-complexed EfOM. These results indicate that the control of the formation of the aluminium-EfOM complexes should be considered as a key step to use the CC-DF process as a pre-treatment of the MF and RO membranes for mitigation of membrane fouling in the tested pilot plant. (C) 2014 Elsevier Ltd. All rights reserved.
引用
收藏
页码:20 / 26
页数:7
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