Key Laboratory of Drinking Water Science and Technology, Research Center for Eco-Environmental Sciences, Chinese Academy of Sciences, Beijing, 100085, China; University of Chinese Academy of Sciences, Beijing, 100049, China.
Key Laboratory of Drinking Water Science and Technology, Research Center for Eco-Environmental Sciences, Chinese Academy of Sciences, Beijing, 100085, China; University of Chinese Academy of Sciences, Beijing, 100049, China.
J Environ Sci (China). 2020 Apr;90:10-19. doi: 10.1016/j.jes.2019.11.002. Epub 2019 Dec 9.
Cake layer formation is inevitable over time for ultrafiltration (UF) membrane-based drinking water treatment. Although the cake layer is always considered to cause membrane fouling, it can also act as a "dynamic protection layer", as it further adsorbs pollutants and dramatically reduces their chance of getting to the membrane surface. Here, the UF membrane fouling performance was investigated with pre-deposited loose flocs in the presence of humic acid (HA). The results showed that the floc dynamic protection layer played an important role in removing HA. The higher the solution pH, the more negative the floc charge, resulting in lower HA removal efficiency due to the electrostatic repulsion and large pore size of the floc layer. With decreasing solution pH, a positively charged floc dynamic protection layer was formed, and more HA molecules were adsorbed. The potential reasons were ascribed to the smaller floc size, greater positive charge, and higher roughness of the floc layer. However, similar membrane fouling performance was also observed for the negative and positive floc dynamic protection layers due to their strong looseness characteristics. In addition, the molecular weight (MW) distribution of HA also played an important role in UF membrane fouling behavior. For the small MW HA molecules, the chance of forming a loose cake layer was high with a negatively charged floc dynamic protection layer, while for the large MW HA molecules it was high with a positively charged floc dynamic protection layer. As a result, slight UF membrane fouling was induced.
随着时间的推移,超滤(UF)膜饮用水处理中不可避免地会形成滤饼层。虽然滤饼层总是被认为会导致膜污染,但它也可以作为一个“动态保护层”,因为它进一步吸附污染物,并大大降低它们到达膜表面的机会。在这里,在腐殖酸(HA)存在的情况下,研究了预沉积的松散絮体对 UF 膜污染性能的影响。结果表明,絮体动态保护层在去除 HA 方面起着重要作用。溶液 pH 值越高,絮体的电荷越负,由于静电排斥和絮体层的大孔径,HA 的去除效率越低。随着溶液 pH 值的降低,形成带正电荷的絮体动态保护层,更多的 HA 分子被吸附。其潜在原因归因于絮体尺寸较小、正电荷较大以及絮体层的粗糙度较高。然而,由于其松散的特性,负电荷和正电荷的絮体动态保护层也表现出相似的膜污染性能。此外,HA 的分子量(MW)分布也对 UF 膜污染行为起着重要作用。对于小 MW 的 HA 分子,带有负电荷的絮体动态保护层形成松散的滤饼层的机会很高,而对于大 MW 的 HA 分子,带有正电荷的絮体动态保护层形成松散的滤饼层的机会很高。因此,UF 膜的污染程度很轻微。