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Retrofitting membrane bioreactor (MBR) into osmotic membrane bioreactor (OMBR): A pilot scale study

机译:将膜生物反应器(MBR)改装成渗透膜生物反应器(OMBR):试验规模研究

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摘要

Forward osmosis (FO) technology that has been applied to a membrane bioreactor (MBR) is referred to as osmotic MBR (OMBR). The new concept developed in this study aims at retrofitting (partly or fully) existing MBR into OMBR, thus limiting the investment costs, allowing for more flexible and combined operation of MBR and OMBR and to fulfil water quality needs. Submerged FO modules were developed by modifying Kubota microfiltration (MF) modules commonly used in MBR and fitting them with new generation thin-film composite FO membranes. The similar design and water fluxes of both MF and FO modules allowed for an unbiased comparison of OMBR and MBR. For the first time, stable OMBR operation with water fluxes above 10 L. m-2. h-1 was achieved using synthetic seawater as draw solution. The proof of concept of retrofitting of MBR and OMBR was demonstrated using a 50 L reactor under varying operating conditions. Findings indicated that standalone OMBR operation is challenging due to salinity build-up which impacts bacterial activity and permeation flux. Fouling occurred in the FO modules to the same degree as MF but osmotic backwashing proved to be an efficient cleaning solution for OMBR. The energy reduction benefit of using an osmotic gradient instead of hydraulic pressure to drive permeation was outweighed by the energy required for draw circulation in OMBR. Loss of selectivity of the FO membranes was observed due to superficial (active layer) physical damage. However, the overall high rejection of trace organic contaminants by OMBR (90%), due to high FO membrane rejection and biological degradation, is a great benefit for OMBR implementation in water reuse schemes.
机译:已施加到膜生物反应器(MBR)的前渗透(Fo)技术称为Osmotic MBR(OMBR)。本研究中开发的新概念旨在改装(部分或完全)现有的MBR进入OMBR,从而限制了投资成本,允许更灵活,综合运行MBR和OMBR,并满足水质需求。浸没式FO模块是通过在MBR中进行常用的kubota微滤(MF)模块来开发,并用新一代薄膜复合FO膜配合它们。 MF和FO模块的类似设计和水通量允许对OMBR和MBR进行无偏见的比较。首次,稳定的OMBR运行,水通量超过10 L.M-2。使用合成海水作为绘制解决方案实现H-1。在不同的操作条件下,使用50L反应器证明了MBR和OMBR改造和OMBR的概念证明。调查结果表明,独立的OMBR操作由于盐度积聚而挑战,这会影响细菌活性和渗透通量。 FOULE中发生的污染与MF的程度相同,但被证明是OMBR的有效清洁解决方案。使用渗透梯度代替液压以驱动渗透的能量降低益处被ombr中的循环所需的能量超过渗透。由于浅表(有源层)物理损伤,观察到FO膜的选择性丧失。然而,由于高膜排斥和生物降解,OMBR(& 90%)整体高痕量的痕量有机污染物由OMBR(& 90%)是水再利用方案中的OMBR实施的一个很大的好处。

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