Slow colloidal aggregation and membrane fouling

被引:49
作者
Aimar, Pierre [1 ,2 ]
Bacchin, Patrice [1 ,2 ]
机构
[1] CNRS, Lab Genie Chim, F-31062 Toulouse, France
[2] UPS, INPT, Univ Toulouse, Lab Genie Chim, F-31062 Toulouse, France
关键词
Membrane; Fouling; Critical flux; Colloids; Stability; Metastability; FLUX-STEP METHOD; CONCENTRATION POLARIZATION; FILTRATION CONDITIONS; ULTRAFILTRATION; MODEL; BIOREACTOR; PARTICLES; SUSPENSIONS; SIMULATION;
D O I
10.1016/j.memsci.2010.05.001
中图分类号
TQ [化学工业];
学科分类号
081705 [工业催化];
摘要
We observed that the concept of critical flux, although established on physical bases, does not describe all typical fouling situations found in membrane filtration. We especially focus on the slow flux decline that is observed in many industrial membrane applications, and that has found several types of explanations that we briefly discuss. In order to get a better understanding of this situation, we have considered the orders of magnitude of the slow aggregation kinetics that are expected to happen within a boundary layer, on an ultrafiltration or microfiltration membrane in operation. The results help to understand that whereas the critical flux is limiting cross-flow filtration of stable colloids, it should be combined to kinetics aspects of slow aggregation in cases of colloids of intermediate stability (metastable). We discuss some consequences on the design and operation of processes using membrane filtration. (C) 2010 Elsevier B.V. All rights reserved.
引用
收藏
页码:70 / 76
页数:7
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