Division of Environmental Engineering, Hokkaido University, N13W8, Kita-ku, Sapporo 060-8628, Japan.
Division of Environmental Engineering, Hokkaido University, N13W8, Kita-ku, Sapporo 060-8628, Japan.
Water Res. 2022 Aug 1;221:118810. doi: 10.1016/j.watres.2022.118810. Epub 2022 Jul 2.
Considerable attention has been paid in recent years to the recovery and effective utilization of organic matter in municipal wastewater for the establishment of a circular economy. Direct membrane filtration (DMF) of municipal wastewater using microfiltration (MF) or ultrafiltration (UF) membranes to retain and concentrate the organic matter in municipal wastewater could be a practical option for this purpose. However, severe membrane fouling and high concentrations of organic matter remaining in the DMF permeate are concerns to be addressed. Application of a simple pretreatment using fixed biofilms was investigated to address these issues. In this study, experiments were carried out at an existing municipal wastewater treatment plant. A moving bed biofilm reactor (MBBR) process operated under a very short HRT of 1 h and DO concentration of 0.5 mg/L selectively degraded low-molecular-weight dissolved organic matter in municipal wastewater without degradation of membrane-recoverable suspended and colloidal organic matter. Application of the pretreatment did not reduce the amount of organic carbon recovered by DMF using an MF membrane (approximately 70% of the influent COD being recovered), while it dramatically mitigated the membrane fouling probably due to the alteration of characteristics of dissolved organic matter in wastewater. The pretreatment also reduced the concentration of organic matter in the DMF permeate by 41%: COD concentration in the DMF permeate was as low as 40 mg/L. With the established MBBR pretreatment, performances of MF (0.1 µm) and UF (molecular weight cut-off: 150,000) membranes for DMF were compared in parallel. It was found that the increase of the recoverable amount of organic matter by using UF was marginal (about 5%), whereas fouling in UF was much more severe than that in MF. The severe fouling in UF was caused by inorganic colloids such as FeS that could pass through MF membranes but be retained by UF membranes. Based on the results obtained in this study, it is concluded that MF is more suitable than UF for efficient DMF.
近年来,人们高度关注从城市废水中回收和有效利用有机物,以建立循环经济。使用微滤(MF)或超滤(UF)膜直接对城市废水进行膜过滤(DMF)以截留和浓缩城市废水中的有机物,这可能是一种实用的选择。然而,膜严重污染和 DMF 渗透物中有机物浓度高是需要解决的问题。本研究采用固定生物膜的简单预处理方法来解决这些问题。在本研究中,在现有的城市污水处理厂进行了实验。在非常短的 HRT(1 小时)和 DO 浓度(0.5 mg/L)下运行的移动床生物膜反应器(MBBR)工艺选择性降解了城市废水中的低分子量溶解有机物,而不会降解膜可回收的悬浮和胶体有机物。预处理并没有减少 MF 膜(约 70%的进水 COD 被回收)回收的有机碳量,同时由于废水中溶解有机物特性的改变,膜污染程度显著降低。预处理还将 DMF 渗透物中的有机物浓度降低了 41%:DMF 渗透物中的 COD 浓度低至 40mg/L。在建立的 MBBR 预处理工艺基础上,对 MF(0.1 µm)和 UF(分子量截止值:150,000)膜用于 DMF 的性能进行了平行比较。结果发现,使用 UF 增加可回收有机物的量效果不大(约 5%),而 UF 的污染比 MF 更严重。UF 的严重污染是由无机胶体如 FeS 引起的,这些胶体可以通过 MF 膜,但被 UF 膜截留。根据本研究的结果,可以得出结论,MF 比 UF 更适合高效 DMF。