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Influence of Transparent Exopolymer Particles (TEP) Fouling on UF Ceramic Membranes and Associated Flux Recovery after Membrane Cleaning

机译:透明外聚合物颗粒(TEP)结垢对超滤陶瓷膜和膜清洗后相关通量恢复的影响

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Ceramic membranes are robust against high pressure and extreme pH (1-14). Theycan sustain aggressive backwashing fluxes that provide more effective hydrauliccleaning compared to polymeric membranes. Recovery of permeability aftermembrane cleaning (either hydraulically or chemically) is important to maintainsustainable operation. This research aimed to assess the effect of transparentexopolymer particles (TEP) on the fouling of UF ceramic membranes in seawaterapplications. An Anopore ceramic UF membrane (AAO20) with a pore size of 20 nmand a TAMI-UF ceramic membrane with a 12 nm average pore sizes were used with aconstant pressure set-up. Red Seawater collected from Thuwal Saudi Arabia was usedas feed water. Milli Q water was used for hydraulic backwashing (BW) instead ofpermeate to prevent cross contamination. Sodium hypochlorite was used for chemicalenhanced backwashing (CEB) and chemical cleaning (CIP) of AAO20 membranes.Ozonated Milli Q (with 10 mg/l ozone) was used for CEB of TAMI-UF membranesand AAO20 membranes. Filtration cycles of 30-60 minutes were adopted. A highbackwashing flux between 500 - 1500 LMH was applied for BW and CEB for 2minutes. The membrane surfaces (fouled and cleaned) were analysed with SEM, EDXand Epifluorescence Microscopy. The results showed that AAO20 membranesbackwashed with Milli Q attained 10-15% flux recovery. The use of CEB (sodiumhypochlorite 3000 ppm) improved flux recovery to 80% and almost 100% after CIP.TAMI-UF membranes achieved average recovery of 35 % after backwashing andimproved to over 80% with CEB. The low recovery after backwashing was attributedto the presence of TEP retained on the membranes that are hypothesized to be moresticky and difficult to be removed by hydraulic backwashing. TEP showed resistanceagainst hydraulic backwashing resulting into low flux recovery. The use of ozonatedMilli Q and sodium hypochlorite for CEB played an important role in breaking up thestructure of TEP (which exhibited behaviour of attaching other foulants) and henceimproved the flux recovery.
机译:陶瓷膜对高压和极端pH(1-14)具有抵抗力。他们 可以承受侵蚀性的反冲洗通量,从而提供更有效的液压 与聚合物膜相比清洁。渗透率恢复后 膜清洁(液压或化学清洁)对于维护保养非常重要 可持续经营。这项研究旨在评估透明效果 聚合物颗粒(TEP)对海水中超滤陶瓷膜结垢的影响 应用程序。孔径为20 nm的Anopore陶瓷超滤膜(AAO20) 并使用平均孔径为12 nm的TAMI-UF陶瓷膜和 恒定压力设置。使用了从沙特阿拉伯的图瓦尔(Thuwal)收集的红海水 作为给水。 Milli Q水用于液压反冲洗(BW),而不是 渗透以防止交叉污染。次氯酸钠用于化工 增强了AAO20膜的反冲洗(CEB)和化学清洗(CIP)。 臭氧化的Milli Q(含10 mg / l臭氧)用于TAMI-UF膜的CEB 和AAO20膜。过滤周期为30-60分钟。高 BW和CEB分别使用500-1500 LMH之间的反洗通量 分钟。膜表面(结垢和清洁)用SEM,EDX分析 和落射荧光显微镜。结果表明,AAO20膜 用Milli Q反冲洗可达到10-15%的助焊剂回收率。使用CEB(钠 次氯酸盐(3000 ppm)可将通量回收率提高至80%,CIP后几乎达到100%。 TAMI-UF膜在反洗后,平均回收率达到35%。 使用CEB可以提高到80%以上。反洗后回收率低的原因是 保留在假想的膜上的TEP的存在 粘性且难以通过液压反冲洗去除。 TEP显示出抵抗力 防止液压反冲洗,导致通量回收率低。臭氧化的使用 CEB的Milli Q和次氯酸钠在分解CEB中起重要作用 TEP的结构(表现出附着其他污垢的行为),因此 改善了焊剂回收率。

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