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Influence of operating parameters and membrane materials on fouling of ceramic hollow fibre membranes

机译:操作参数和膜材料对陶瓷中空纤维膜结垢的影响

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Fouling is one of the critical issues in membrane filtration, especially in the field of wastewater treatment. In this study sodium alginate was used as model compound for extracellular polymeric substances (EPS) in order to investigate the filtration and fouling characteristics of two newly developed ceramic hollow fibre membranes. The membranes studied have an asymmetrical structure consisting of an Al2O3 support layer, which is covered by an active layer. Two different active layers (Al2O3 and SiC) were studied under various operating conditions (dead-end and cross-flow filtration) by filtering sodium alginate solutions in the presence and absence of calcium ions. Fouling mechanisms taking place in dead-end mode were evaluated according to the cake filtration model. Dead-end filtration experiments revealed a change in fouling mechanisms from pore blocking and cake filtration in the absence of calcium ions to cake filtration only in the presence of calcium ions. Furthermore, cross-flow filtration experiments showed a big influence of calcium ions on the removal of the resulting alginate layer from the membrane surface due to shear forces induced by cross-flow. In the absence of calcium ions, the filtrate flux was found to depend strongly on transmembrane pressure (TMP) and cross-flow velocity, whereas in the presence of calcium ions, the chosen cross-flow velocities (1-3 m/s) were not sufficient to control alginate fouling. Cross-flow experiments without calcium addition revealed a higher flux for SiC membranes compared to Al2O3 membranes. For dead-end filtration experiments, no significant difference was found. (C) 2016 Elsevier B.V. All rights reserved.
机译:结垢是膜过滤中的关键问题之一,特别是在废水处理领域。在这项研究中,海藻酸钠被用作细胞外聚合物(EPS)的模型化合物,以研究两种新开发的陶瓷中空纤维膜的过滤和结垢特性。所研究的膜具有由Al2O3支撑层组成的不对称结构,该支撑层被活性层覆盖。在存在和不存在钙离子的情况下,通过过滤藻酸钠溶液,在各种操作条件下(死端和错流过滤)研究了两种不同的活性层(Al2O3和SiC)。根据滤饼过滤模型评估了死角模式下的结垢机理。死端过滤实验揭示了结垢机理的变化,从不存在钙离子的情况下的孔阻塞和滤饼过滤到仅在存在钙离子的情况下的滤饼过滤。此外,错流过滤实验表明,由于错流引起的剪切力,钙离子对从膜表面去除藻酸盐层的影响很大。在不存在钙离子的情况下,发现滤液通量在很大程度上取决于跨膜压(TMP)和错流速度,而在存在钙离子的情况下,选择的错流速度(1-3 m / s)为不足以控制藻酸盐结垢。没有添加钙的错流实验表明,与Al2O3膜相比,SiC膜的通量更高。对于死端过滤实验,未发现明显差异。 (C)2016 Elsevier B.V.保留所有权利。

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