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Rejection in Pumping Permeate Microfiltration

机译:抽滤渗透微滤中的排斥

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摘要

The pumping permeate regime is a recently developed technique for minimization of fouling. However this procedure, which maintains the flux, may affect rejection. In this study a 0.22 #mu#m microfiltration membrane was challenged with 50 nm gold sol in the pumping permate regime below and beyond the critical flux with prefiltation of 1 #mu#m latex beads. The rejection of colloidal gold was complete in all experiments. Above the critical flux a cake is formed and prevents the particles from passing through the membrane. Below the critical flux, with no cake formation, the particles move away from the membrane due to back-transport which is significant in the pumped permeate regime. Without movement towards the membrane, the particles do not reach it to pass through. Some of the particles which enter the membrane pores remain there due to adsorption.
机译:抽水渗透状态是最近开发的一种用于最小化结垢的技术。但是,这种保持通量的过程可能会影响抑制率。在这项研究中,在泵送渗透液状态下,在临界通量以下和超出临界通量的条件下,通过预过滤1#μ#m乳胶珠,用50 nm金溶胶对0.22#μ#m的微滤膜进行了挑战。在所有实验中胶体金的排斥都是完全的。在临界通量之上,形成饼并防止颗粒穿过膜。在临界通量以下,没有滤饼形成,由于反向输送,颗粒从膜上移开,这在泵送的渗透状态中很重要。如果不朝着膜移动,则颗粒不会到达膜以通过。进入膜孔的一些颗粒由于吸附而保留在那里。

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