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

机译:一种新型前渗透反应器,辅助微滤,用于深厚加厚废物活性污泥:性能和含义

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摘要

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 (NH4+-N), nitrate nitrogen (NO3--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. (C) 2021 Elsevier Ltd. All rights reserved.
机译:废物活性污泥(IS)治疗越来越受到其越来越容易和高的过程成本的兴趣。污泥增稠通常是待处理的第一个方法。然而,传统的污泥增厚方法受到大量占地面积,低增稠效率和释放磷的趋势。在这里,我们报道了一种新型微滤(MF)膜,用于辅助污泥增厚的前渗透(MF-FO)。 MF-FA反应器在10天操作后,通过约7至50g / L获得混合液悬浮固体(MLS)浓度的污泥增厚。更重要的是,过滤后的流出物质与总有机碳(TOC),氨氮(NH4 + -N),硝酸盐氮(NO3-N)和总磷(TP)为1.94 +/- 0.46,0.02 + / - 0.07,4.55 +/- 1.59和0.24 +/- 0.26 mg / L.另外,MF膜的整合成功地控制了低1.6-3.1ms / cm的低范围内的MF-FO反应器的盐度,这减轻了膜的助焊剂下降,从而延长了操作时间。在这种情况下,MF-FO反应器中膜的通量下降主要是由于膜污垢。此外,当MLSS浓度小于30g / L时,FO膜表面上的污垢层主要由生物泵和有机污垢组成,当MLSS浓度超过30g / L时转向滤饼层。结果报告的结果证明了MF-FO反应器是一种很有希望的增厚技术,用于其优异的增厚性能和膜的高流出质量。 (c)2021 elestvier有限公司保留所有权利。

著录项

  • 来源
    《Water Research》 |2021年第1期|116998.1-116998.7|共7页
  • 作者单位

    Jiangnan Univ Sch Environm & Civil Engn Jiangsu Key Lab Anaerob Biotechnol Wuxi 214122 Jiangsu Peoples R China;

    Jiangnan Univ Sch Environm & Civil Engn Jiangsu Key Lab Anaerob Biotechnol Wuxi 214122 Jiangsu Peoples R China;

    Univ Bath Dept Chem Engn Bath BA2 7AY Avon England;

    Jiangnan Univ Sch Environm & Civil Engn Jiangsu Key Lab Anaerob Biotechnol Wuxi 214122 Jiangsu Peoples R China;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    forward osmosis; microfiltration; waste activated sludge; sludge thickening; membrane fouling;

    机译:前进渗透;微滤;废物活性污泥;污泥增厚;膜污垢;

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