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Retentive Thickening of Physical Washing Drainage of Membrane Filtration Processes Using Hollow-Fiber MF Thickener
使用中空纤维MF浓缩机对膜过滤过程中的物理清洗排水进行保留浓缩
在以日本佐美河水为原水的膜水处理系统中,进行了中试试验,以研究一种新型的微滤水浓缩器。膜过滤浓缩机在浸入式死端过滤过程中表现出浓差极化现象,被证明适用于物理清洗滞留水的浓缩,在过滤流速高达0.5 m/天时,平均浊度为100 NTU,最大浊度为400 NTU。新增稠剂使前置膜过滤系统的原水回收率提高了99%以上。然而,超高浊度(超过420 NTU)导致过滤阻力迅速增加。较高的流速(0.5 m/天)比较低的流速(0.3 m/天)保持较低的阻力,因为在较高的流量下,城市水被更快地推向浓缩锥。
粒径分布分析表明,粒径小于3μm的颗粒倾向于留在浓缩池中并积聚,因此附着在膜表面,导致过滤阻力增加。包括5个参考文献、表格、图表。
Pilot plant experiments were performed to investigate a novel microfilterretentate water thickener in a membrane water treatment system which uses Japan's Sagami River water as the raw water source. The membrane filter thickener, which showed the concentration polarization phenomenon in the submerged dead-end filtration process, was proved to be applicable to the thickening of the physical washing retentate water, which has a mean turbidity of 100 NTU and a maximum turbidity of 400 NTU at a filtration flow rate as high as 0.5 m/day. The raw water recovery rate of the preceeding membrane filtration system was increased in excess of 99% by the new thickener. However, extra high turbidity (over 420 NTU) caused a rapid increase in filtration resistance. Higher flow rates (0.5 m/day) maintained lower resistance than lower flow rates (0.3 m/day) becauseturbid water was pushed down to a concentration cone faster at higher flux. Particle size distribution analysis showed that particles finer than 3 um tend to remain and accumulate in the thickening basin, and therefore attach to the surface of membranes and lead to increased filtration resistance. Includes 5 references, tables, figures.