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正向渗透和微滤在一体式渗透-微滤膜生物反应器系统中的作用。

The role of forward osmosis and microfiltration in an integrated osmotic-microfiltration membrane bioreactor system.

机构信息

Strategic Water Infrastructure Laboratory, School of Civil, Mining and Environmental Engineering, University of Wollongong, Wollongong, NSW 2522, Australia.

Strategic Water Infrastructure Laboratory, School of Chemistry, University of Wollongong, Wollongong, NSW 2522, Australia.

出版信息

Chemosphere. 2015 Oct;136:125-32. doi: 10.1016/j.chemosphere.2015.04.082. Epub 2015 May 15.

Abstract

This study investigates the performance of an integrated osmotic and microfiltration membrane bioreactor (O/MF-MBR) system for wastewater treatment and reclamation. The O/MF-MBR system simultaneously used microfiltration (MF) and forward osmosis (FO) membranes to extract water from the mixed liquor of an aerobic bioreactor. The MF membrane facilitated the bleeding of dissolved inorganic salts and thus prevented the build-up of salinity in the bioreactor. As a result, sludge production and microbial activity were relatively stable over 60 days of operation. Compared to MF, the FO process produced a better permeate quality in terms of nutrients, total organic carbon, as well as hydrophilic and biologically persistent trace organic chemicals (TrOCs). The high rejection by the FO membrane also led to accumulation of hydrophilic and biologically persistent TrOCs in the bioreactor, consequently increasing their concentration in the MF permeate. On the other hand, hydrophobic and readily biodegradable TrOCs were minimally detected in both MF and FO permeates, with no clear difference in the removal efficiencies between two processes.

摘要

本研究考察了集成渗透和微滤膜生物反应器(O/MF-MBR)系统在废水处理和回收方面的性能。O/MF-MBR 系统同时使用微滤(MF)和正向渗透(FO)膜从好氧生物反应器的混合液中提取水。MF 膜有助于去除溶解的无机盐,从而防止生物反应器中盐分的积累。结果,在 60 天的运行过程中,污泥产量和微生物活性相对稳定。与 MF 相比,FO 工艺在养分、总有机碳以及亲水性和具有生物持久性的痕量有机化学品(TrOCs)方面产生了更好的渗透质量。FO 膜的高截留率也导致亲水性和具有生物持久性的 TrOCs 在生物反应器中积累,从而导致其在 MF 渗透物中的浓度增加。另一方面,在 MF 和 FO 渗透物中均检测到痕量的疏水性和易生物降解的 TrOCs,两种工艺的去除效率没有明显差异。

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