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首页> 外文期刊>Desalination: The International Journal on the Science and Technology of Desalting and Water Purification >Variations in backwash efficiency during colloidal filtration of hollow-fiber microfiltration membranes
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Variations in backwash efficiency during colloidal filtration of hollow-fiber microfiltration membranes

机译:中空纤维微滤膜胶体过滤过程中反洗效率的变化

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A series of filtration experiments was performed systematically to investigate physical and chemical factors affecting the efficiency of backwashing during microfiltration of colloidal suspensions.In this study,all experiments were conducted in dead-end filtration mode utilizing an outside-in,hollow-fiber module with a nominal pore size of 0.1mum.Silica particles (mean diameter=0.14mum) were used as model colloids.Using a flux decline model based on the Happel 's cell for the hydraulic resistance of the particle layer,the cake structure was determined from experimental fouling data and then correlated to backwash efficiency.Modeling of experimental data revealed no noticeable changes in cake layer structure when feed particle concentration and operating pressure increased.Specifically,the packing density of the cake layer (1-cake porosity) in the cake layer ranged from 0.66 to 0.67,which corresponds well to random packing density.However,the particle packing density increased drastically with ionic strength.The results of backwashing experiments demonstrated that the efficiency of backwashing decreased significantly with increasing solution ionic strength,while backwash efficiency did not vary when particle concentration and operating pressure increased.This finding suggests that backwash efficiency is closely related to the structure of the cake layer formed during particle filtration.More densely packed cake layers were formed under high ionic strength,and consequently less flux was recovered per given backwash volume during backwashing.
机译:系统地进行了一系列过滤实验,以研究影响胶体悬浮液微滤过程中反冲洗效率的物理和化学因素。标称孔径为0.1mum.silica颗粒(平均直径=0.14μm)用作模型胶体。使用基于Happel池的通量下降模型计算颗粒层的水力阻力,从实验结垢数据,然后将其与反洗效率相关。实验数据的建模显示,当进料颗粒浓度和操作压力增加时,滤饼层结构没有明显变化。具体来说,滤饼层中滤饼层的堆积密度(1-滤饼孔隙率)范围从0.66到0.67,非常适合随机堆积密度。但是,粒子堆积密度急剧增加反洗实验结果表明,反洗效率随溶液离子强度的增加而显着降低,而反冲效率在颗粒浓度和工作压力增加时没有变化。这一发现表明反洗效率与结构密切相关。在高离子强度下会形成更多紧密堆积的滤饼层,因此在反洗过程中每给定的反洗体积回收的助焊剂较少。

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