Permeability recovery of fouled forward osmosis membranes by chemical cleaning during a long-term operation of anaerobic osmotic membrane bioreactors treating low-strength wastewater

被引:62
作者
Wang, Xinhua [1 ]
Hu, Taozhan [1 ]
Wang, Zhiwei [2 ]
Li, Xiufen [1 ]
Ren, Yueping [1 ]
机构
[1] Jiangnan Univ, Sch Environm & Civil Engn, Jiangsu Key Lab Anaerob Biotechnol, Wuxi 214122, Peoples R China
[2] Tongji Univ, Sch Environm Sci & Engn, State Key Lab Pollut Control & Resource Reuse, Shanghai 200092, Peoples R China
基金
中国国家自然科学基金;
关键词
Chemical cleaning; Forward osmosis; Membrane fouling; Hydrogen peroxide; Anaerobic osmotic membrane bioreactor; Wastewater treatment; THIN-FILM COMPOSITE; SLUDGE RETENTION TIME; REVERSE-OSMOSIS; FO MEMBRANE; HYPOCHLORITE DEGRADATION; HYDROGEN-PEROXIDE; TFC POLYAMIDE; DRAW SOLUTES; PERFORMANCE; MICROFILTRATION;
D O I
10.1016/j.watres.2017.07.011
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Anaerobic osmotic membrane bioreactor (AnOMBR) has gained increasing interests in wastewater treatment owing to its simultaneous recovery of biogas and water. However, the forward osmosis (FO) membrane fouling was severe during a long-term operation of AnOMBRs. Here, we aim to recover the permeability of fouled FO membranes by chemical cleaning. Specifically speaking, an optimal chemical cleaning procedure was searched for fouled thin film composite polyamide FO (TFC-FO) membranes in a novel microfiltration (MF) assisted AnOMBR (AnMF-OMBR). The results indicated that citric acid, disodium ethylenediaminetetraacetate (EDTA-2Na), hydrochloric acid (HCl), sodium dodecyl sulfate (SDS) and sodium hydroxide (NaOH) had a low cleaning efficiency of less than 15%, while hydrogen peroxide (H2O2) could effectively remove foulants from the TFC-FO membrane surface (almost 100%) through oxidizing the functional group of the organic foulants and disintegrating the colloids and microbe flocs into fine particles. Nevertheless, the damage of H2O2 to the TFC-FO membrane was observed when a high cleaning concentration and a long duration were applied. In this case, the optimal cleaning conditions including cleaning concentration and time for fouled TFC-FO membranes were selected through confocal laser scanning microscope (CLSM) and scanning electron microscopy (SEM) images and the flux recovery rate. The results suggested that the optimal cleaning procedure for fouled TFC-FO membranes was use of 0.5% H2O2 at 25 degrees C for 6 h, and after that, the cleaned TFC-FO membrane had the same performance as a virgin one including water flux and rejection for organic matters and phosphorus during the operation of AnMF-OMBR. (C) 2017 Elsevier Ltd. All rights reserved.
引用
收藏
页码:505 / 512
页数:8
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