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Effects of particle size segregation on crossflow microfiltration performance: Control mechanism for concentration polarisation and particle fractionation

机译:粒度分离对错流微滤性能的影响:浓度极化和颗粒分级的控制机制

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Although the principal mechanisms of crossflow microfiltration (MF) are well-known, the practical applicability of the resulting microfiltration models is still limited. This can be largely attributed to the lack of understanding of effects of polydispersity in the particulate suspensions, as relevant to concentration polarisation in ME This paper describes an investigation of concentration polarisation behaviour of bidisperse suspensions, in the regime where shear-induced diffusion is the dominant back-transport mechanism. In the transient flux regime, the particle deposition onto the membrane was monitored by means of confocal scanning laser microscopy. As in accordance with the linear dependence of the shear-induced diffusivity on a 2, only the small particles in the bidisperse suspensions were found to deposit onto the membrane. The back-transport flux that was calculated from the deposition rate and the actual permeate flux, was found to be independent of the composition of the suspension, whereas it was equal to the back-transport flux of a monodisperse suspension of the small particles only, with a similar total particle fraction. These results can be explained with the occurrence of particle size segregation in the feed flow, which leads to an enrichment with small particles of the suspension near the membrane. The findings are also shown to be relevant to particle fractionation processes by ME In such fractionation processes, particle size segregation is found to have a strong effect on the separation characteristics such as particle size and fat content of the permeate. A polydisperse suspension could be fractionated using a membrane having a pore size larger than the largest particles present. The fractionation thus results not from size exclusion in the membrane, but from segregation effects in the feed channel. (c) 2005 Elsevier B.V. All rights reserved.
机译:尽管错流微滤(MF)的主要机理是众所周知的,但所得微滤模型的实际适用性仍然有限。这可能是由于缺乏对颗粒悬浮液中多分散性影响的理解,因为与ME中的浓度极化有关。本文描述了在剪切诱导扩散占主导的状态下双分散悬浮液的浓度极化行为的研究。反向传输机制。在瞬态通量状态下,通过共聚焦扫描激光显微镜监测颗粒在膜上的沉积。根据剪切诱导的扩散率对2的线性依赖性,仅发现双分散悬浮液中的小颗粒沉积在膜上。发现由沉积速率和实际渗透通量计算出的反向传输通量与悬浮液的成分无关,而仅等于小颗粒单分散悬浮液的反向传输通量,具有相似的总粒子分数。这些结果可以用进料流中颗粒尺寸的偏析来解释,这导致膜附近悬浮液的小颗粒富集。该发现也被证明与通过ME进行的颗粒分级分离过程有关。在这种分级分离过程中,发现粒度分离对分离特性例如渗透物的粒度和脂肪含量具有强烈的影响。可以使用孔径大于存在的最大颗粒的膜来分离多分散悬浮液。因此,分馏不是由膜中的尺寸排阻引起的,而是由进料通道中的分离作用引起的。 (c)2005 Elsevier B.V.保留所有权利。

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