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Prevention of UF membrane fouling in drinking water treatment by addition of H_2O_2 during membrane backwashing

机译:在膜反冲洗过程中加入H_2O_2可防止饮用水处理中超滤膜结垢

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Although conventional coagulation pre-treatment can mitigate the fouling of ultrafiltration (UF) membrane when treating raw waters, it is insufficient to restrict the development of irreversible fouling and reversible fouling to a low level. In this paper we demonstrate that the intermittent addition of H2O2 into the membrane tank during backwash events (after coagulation pre-treatment) successfully prevented the development of any significant membrane fouling. Laboratory-scale tests were undertaken using two membrane systems operated in parallel over 60 days, one serving as a reference coagulation-ultrafiltration (CUF) process, and the other receiving the H2O2 (CUF-H2O2), with a decreasing dose in three successive phases: 10, 5 and 2 mg/L. The results showed that the addition of H2O2 (via a separate dosing tube) during a 1 min backwash process (at 30 min intervals) reduced the growth of bacteria in the membrane tank, and the associated concentrations of soluble microbial products (SMP, including protein and polysaccharide). This resulted in a much reduced cake layer, which contained significantly less high MW organic matter (50%), such as EPS, thereby improving the interaction between particles in the cake layer and/or particles and the membrane surface. There was also less organic matter, of all MW fractions, adsorbed in the membrane pores of the CUF-H2O2 system. The addition of H2O2 in the membrane tank appeared to alter the nature of the organic matter with a conversion of hydrophobic to hydrophilic fractions, which induced less organics adsorption within the hydrophobic PVDF membrane pores, and a reduced bonding ability for particles. There was no physico-chemical evidence of any deterioration of the membrane from exposure to H2O2, which indicates the feasibility of applying this novel method of fouling control for full-scale UF based water treatment processes. (C) 2018 Elsevier Ltd. All rights reserved.
机译:尽管常规的混凝预处理可以在处理原水时减轻超滤(UF)膜的结垢,但不足以将不可逆结垢和可逆结垢的产生限制在较低水平。在本文中,我们证明了在反冲洗过程中(凝结预处理后)将H2O2间歇地添加到膜罐中,可以成功地防止任何明显的膜污染。使用两个在60天内并行运行的膜系统进行了实验室规模的测试,其中一个用作参考混凝-超滤(CUF)工艺,另一个用于接收H2O2(CUF-H2O2),并且在三个连续阶段中剂量逐渐降低:10、5和2 mg / L。结果表明,在1分钟的反冲洗过程中(间隔30分钟)添加H2O2(通过单独的定量管)可减少膜罐中细菌的生长,并降低相关的可溶性微生物产物(SMP,包括蛋白质)的浓度和多糖)。这导致滤饼层大大减少,其包含明显更少的高分子量有机物(> 50%),例如EPS,从而改善了滤饼层中的颗粒和/或颗粒与膜表面之间的相互作用。在所有MW馏分中,吸附在CUF-H2O2系统膜孔中的有机物也较少。在膜罐中加入H2O2似乎会改变有机物的性质,将疏水性部分转化为亲水性部分,从而导致疏水性PVDF膜孔中有机物的吸附减少,并降低了颗粒的结合能力。没有任何物理化学证据表明膜暴露于H2O2会导致膜变质,这表明将这种新型结垢控制方法应用于大规模基于UF的水处理工艺的可行性。 (C)2018 Elsevier Ltd.保留所有权利。

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