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The innovative Osmotic Membrane Bioreactor (OMBR) for reuse of wastewater

机译:用于废水回用的创新型渗透膜生物反应器(OMBR)

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An innovative osmotic membrane bioreactor (OMBR) is currently under development for thenreclamation of wastewater, which combines activated sludge treatment and forward osmosis (FO)nmembrane separation with a RO post-treatment. The research focus is FO membrane fouling andnperformance using different activated sludge investigated both at laboratory scale (membrane area ofn112 cm2) and at on-site bench scale (flat sheet membrane area of 0.1m2). FO performance onnlaboratory-scale (i) increased with temperature due to a decrease in viscosity and (ii) was independentnof the type of activated sludge. Draw solution leakage increased with temperature and varied forndifferent activated sludge. FO performance on bench-scale (i) increased with osmotic driving force,n(ii) depended on the membrane orientation due to internal concentration polarization and (iii) wasninvariant to feed flow decrease and air injection at the feed and draw side. Draw solution leakage couldnnot be evaluated on bench-scale due to experimental limitation. Membrane fouling was not found onnlaboratory scale and bench-scale, however, partially reversible fouling was found on laboratory scale fornFO membranes facing the draw solution. Economic assessment indicated a minimum flux ofn15 L.mu00022hu00021 at 0.5M NaCl for OMBR-RO to be cost effective, depending on the FO membrane price.
机译:目前正在开发一种创新的渗透膜生物反应器(OMBR),用于废水的回收,该工艺将活性污泥处理和正渗透(FO)膜分离与RO后处理相结合。研究重点是在实验室规模(膜面积n112 cm2)和现场工作台规模(平板膜面积0.1m2)上使用不同的活性污泥对FO膜的结垢和性能进行研究。在实验室规模的FO性能(i)由于粘度降低而随温度增加而增加(ii)与活性污泥的类型无关。汲取溶液的泄漏量随温度的升高而增加,并且不同的活性污泥也有所不同。实验台上的FO性能(i)随着渗透驱动力的增加而增加,n(ii)由于内部浓度极化而取决于膜取向,并且(iii)进料流量减少和进料侧和吸料侧的空气注入均不变。由于实验的局限性,无法在实验室规模上评估抽水溶液的泄漏。在实验室规模和实验室规模上均未发现膜结垢,但是,在实验室规模中,面向吸液的fornFO膜发现部分可逆结垢。经济评估表明,对于OMBR-RO,在0.5M NaCl处的最低通量为n15 L.mu00022hu00021,要使其具有成本效益,这取决于FO膜的价格。

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