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长期运行厌氧渗透膜生物反应器处理低浓度废水过程中,通过化学清洗恢复污染正向渗透膜的渗透性。

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

机构信息

Jiangsu Key Laboratory of Anaerobic Biotechnology, School of Environmental and Civil Engineering, Jiangnan University, Wuxi 214122, PR China.

Jiangsu Key Laboratory of Anaerobic Biotechnology, School of Environmental and Civil Engineering, Jiangnan University, Wuxi 214122, PR China.

出版信息

Water Res. 2017 Oct 15;123:505-512. doi: 10.1016/j.watres.2017.07.011. Epub 2017 Jul 5.

Abstract

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 (HO) 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 HO 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% HO at 25 °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.

摘要

厌氧渗透膜生物反应器(AnOMBR)因其能够同时回收沼气和水而在废水处理中受到越来越多的关注。然而,在 AnOMBR 的长期运行过程中,正向渗透(FO)膜的污染问题非常严重。在这里,我们旨在通过化学清洗来恢复污染 FO 膜的渗透性。具体来说,在新型微滤(MF)辅助厌氧膜生物反应器(AnMF-OMBR)中,我们寻找了一种优化的化学清洗程序来清洗污染的薄膜复合聚酰胺 FO(TFC-FO)膜。结果表明,柠檬酸、乙二胺四乙酸二钠(EDTA-2Na)、盐酸(HCl)、十二烷基硫酸钠(SDS)和氢氧化钠(NaOH)的清洗效率都低于 15%,而过氧化氢(HO)可以通过氧化有机污染物的官能团和将胶体和微生物絮体分解成细小颗粒,有效地从 TFC-FO 膜表面去除污染物(几乎 100%)。然而,当使用高清洗浓度和长时间时,会观察到 HO 对 TFC-FO 膜的损害。在这种情况下,通过共焦激光扫描显微镜(CLSM)和扫描电子显微镜(SEM)图像以及通量恢复率,选择了污染 TFC-FO 膜的最佳清洗条件,包括清洗浓度和时间。结果表明,污染 TFC-FO 膜的最佳清洗程序是在 25°C 下使用 0.5%的 HO 清洗 6 小时,之后清洗过的 TFC-FO 膜在 AnMF-OMBR 的运行过程中具有与新膜相同的性能,包括水通量和对有机物和磷的截留率。

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