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一种新型的正向渗透膜生物反应器用于深度浓缩剩余污泥:性能及意义。

A novel forward osmosis reactor assisted with microfiltration for deep thickening waste activated sludge: performance and implication.

机构信息

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

Department of Chemical Engineering, University of Bath, Bath, BA2 7AY, UK.

出版信息

Water Res. 2021 May 1;195:116998. doi: 10.1016/j.watres.2021.116998. Epub 2021 Mar 2.

Abstract

Waste activated sludge (WAS) treatment has gained growing interests for its increasingly capacity and high process cost. Sludge thickening is generally the first process of the WAS treatment. However, traditional sludge thickening approach was restrained by large footprint, low thickening efficiency, and tendency of releasing phosphorus. Here, we reported a novel microfiltration (MF) membrane assisting forward osmosis (FO) process (MF-FO) for sludge thickening. The MF-FO reactor achieved a sludge thickening of the mixed liquor suspended solids (MLSS) concentration from approximately 7 to 50 g/L after 10-day operation. More importantly, the effluent quality after FO filtration was superior with total organic carbon (TOC), ammonia nitrogen (NH-N), nitrate nitrogen (NO-N) and total phosphorus (TP) of 1.94 ± 0.46, 0.02 ± 0.07, 4.55 ± 1.59 and 0.24 ± 0.26 mg/L, respectively. Additionally, the integration of MF membrane successfully controlled the salinity of the MF-FO reactor in a low range of 1.6-3.1 mS/cm, which mitigated the flux decline of FO membrane and thus prolonged the operating time. In this case, the flux decline of FO membrane in the MF-FO reactor was mainly due to the membrane fouling. Furthermore, the fouling layer on the FO membrane surface was a gel layer mainly composed of biofoulants and organic foulants when the MLSS concentration was less than 30 g/L, while it turned to a cake layer when the MLSS concentration exceeded 30 g/L. Results reported here demonstrated that the MF-FO reactor is a promising WAS thickening technology for its excellent thickening performance and high effluent quality of FO membrane.

摘要

污泥(WAS)处理因其日益增加的处理能力和高处理成本而受到越来越多的关注。污泥浓缩通常是 WAS 处理的第一道工序。然而,传统的污泥浓缩方法受到占地面积大、浓缩效率低和释放磷的倾向的限制。在这里,我们报道了一种用于污泥浓缩的新型微滤(MF)膜辅助正向渗透(FO)工艺(MF-FO)。MF-FO 反应器在 10 天的运行后,将混合液悬浮固体(MLSS)浓度从约 7 增加到 50 g/L。更重要的是,FO 过滤后的出水质量更好,总有机碳(TOC)、氨氮(NH-N)、硝酸盐氮(NO-N)和总磷(TP)分别为 1.94±0.46、0.02±0.07、4.55±1.59 和 0.24±0.26 mg/L。此外,MF 膜的集成成功地将 MF-FO 反应器的盐度控制在 1.6-3.1 mS/cm 的低范围内,减轻了 FO 膜的通量下降,从而延长了运行时间。在这种情况下,MF-FO 反应器中 FO 膜的通量下降主要是由于膜污染。此外,当 MLSS 浓度低于 30 g/L 时,FO 膜表面的污垢层主要是由生物污垢和有机污垢组成的凝胶层,而当 MLSS 浓度超过 30 g/L 时,它会变成滤饼层。这里报道的结果表明,MF-FO 反应器是一种很有前途的 WAS 浓缩技术,具有出色的浓缩性能和 FO 膜的高出水质量。

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