Chen Mingliang, Heijman Sebastiaan G J, Luiten-Olieman Mieke W J, Rietveld Luuk C
Section of Sanitary Engineering, Department of Water Management, Faculty of Civil Engineering and Geosciences, Delft University of Technology, Stevinweg 1, 2628 CN Delft, The Netherlands.
Section of Sanitary Engineering, Department of Water Management, Faculty of Civil Engineering and Geosciences, Delft University of Technology, Stevinweg 1, 2628 CN Delft, The Netherlands.
Water Res. 2022 Jun 1;216:118267. doi: 10.1016/j.watres.2022.118267. Epub 2022 Mar 8.
Ceramic membranes have drawn increasing attention in oily wastewater treatment as an alternative to their traditional polymeric counterparts, yet persistent membrane fouling is still one of the largest challenges. Particularly, little is known about ceramic membrane fouling by oil-in-water (O/W) emulsions in constant flux filtration modes. In this study, the effects of emulsion chemistry (surfactant concentration, pH, salinity and Ca) and operation parameters (permeate flux and filtration time) were comparatively evaluated for alumina and silicon carbide (SiC) deposited ceramic membranes, with different physicochemical surface properties. The original membranes were made of 100% alumina, while the same membranes were also deposited with a SiC layer to change the surface charge and hydrophilicity. The SiC-deposited membrane showed a lower reversible and irreversible fouling when permeate flux was below 110 L m h. In addition, it exhibited a higher permeance recovery after physical and chemical cleaning, as compared to the alumina membranes. Increasing sodium dodecyl sulfate (SDS) concentration in the feed decreased the fouling of both membranes, but to a higher extent in the alumina membranes. The fouling of both membranes could be reduced with increasing the pH of the emulsion due to the enhanced electrostatic repulsion between oil droplets and membrane surface. Because of the screening of surface charge in a high salinity solution (100 mM NaCl), only a small difference in irreversible fouling was observed for alumina and SiC-deposited membranes under these conditions. The presence of Ca in the emulsion led to high irreversible fouling of both membranes, because of the compression of diffusion double layer and the interactions between Ca and SDS. The low fouling tendency and/or high cleaning efficiency of the SiC-deposited membranes indicated their potential for oily wastewater treatment.
陶瓷膜作为传统聚合物膜的替代品,在含油废水处理中受到了越来越多的关注,但膜污染问题仍然是最大的挑战之一。特别是,关于在恒流过滤模式下陶瓷膜被水包油(O/W)乳液污染的情况,人们了解甚少。在本研究中,针对具有不同物理化学表面性质的氧化铝和碳化硅(SiC)沉积陶瓷膜,比较评估了乳液化学性质(表面活性剂浓度、pH值、盐度和Ca)和操作参数(渗透通量和过滤时间)的影响。原始膜由100%氧化铝制成,同时相同的膜也沉积了一层SiC以改变表面电荷和亲水性。当渗透通量低于110 L m h时,SiC沉积膜显示出较低的可逆和不可逆污染。此外,与氧化铝膜相比,它在物理和化学清洗后表现出更高的通量恢复率。进料中十二烷基硫酸钠(SDS)浓度的增加降低了两种膜的污染,但在氧化铝膜中降低的程度更大。由于油滴与膜表面之间静电排斥增强,随着乳液pH值的增加,两种膜的污染都可以减少。由于在高盐溶液(100 mM NaCl)中表面电荷的屏蔽作用,在这些条件下,氧化铝和SiC沉积膜的不可逆污染仅观察到很小的差异。乳液中Ca的存在导致两种膜的不可逆污染都很高,这是由于扩散双电层的压缩以及Ca与SDS之间的相互作用。SiC沉积膜的低污染倾向和/或高清洗效率表明了它们在含油废水处理中的潜力。