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The MBR Book: Principles and Applications of Membrane

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66 <strong>The</strong> <strong>MBR</strong> <strong>Book</strong><br />

to provide a hydraulic resistance <strong>of</strong> around twice that <strong>of</strong> a UF membrane (Choi et al.,<br />

2005b). Interestingly, the DOC rejection <strong>of</strong> both membranes was similar following<br />

2 h <strong>of</strong> operation, indicating the dynamic membrane layer formed on the membranes<br />

to have provided the perm-selectivity rather than the membrane substrate itself.<br />

Conventional wisdom considers smaller pores to afford greater protection <strong>of</strong> the<br />

membrane by rejecting a wider range <strong>of</strong> materials, with reference to their size, thus<br />

increasing cake (or fouling layer) resistance. Compared to that formed on membranes<br />

having larger pores, the layer is more readily removed <strong>and</strong> less likely to leave<br />

residual pore plugging or surface adsorption. It is the latter <strong>and</strong> related phenomena<br />

which cause irreversible <strong>and</strong> irrecoverable fouling. However, when testing membranes<br />

with pores ranging from 0.4 to 5 �m, G<strong>and</strong>er et al. (2000) conversely observed greater<br />

initial fouling for the larger pore-size membranes <strong>and</strong> significant flux decline when<br />

smaller pore-size membrane were used over an extended period <strong>of</strong> time, though these<br />

authors used isotropic membranes without surface hydrophilicisation.<br />

Characterisation <strong>of</strong> the distribution <strong>of</strong> MW compounds present in the supernatant<br />

<strong>of</strong> <strong>MBR</strong>s operated with membranes <strong>of</strong> four pore sizes (ranging from 0.1 to<br />

0.8 �m) has also been presented (Lee et al., 2005). Although providing a lower fouling<br />

rate, the 0.8 �m pore-size <strong>MBR</strong> nonetheless had a slightly higher supernatant<br />

concentration <strong>of</strong> most <strong>of</strong> the macromolecules. According to these results, it seems<br />

unlikely for the small differences in MW distribution to cause significant variation in<br />

fouling rates observed between the four <strong>MBR</strong> systems. In another study based on<br />

short-term experiments, sub-critical fouling resistance <strong>and</strong> fouling rate increased<br />

linearly with membrane resistance ranging from 0.4 to 3.5 � 10 9 m �1 , corresponding<br />

to membrane pore size from 1 down to 0.01 �m (Le-Clech et al., 2003c). <strong>The</strong>se<br />

results suggest that a dynamic layer is created <strong>of</strong> greater overall resistance for the<br />

more selective membranes operating under sub-critical conditions, <strong>and</strong> supports the<br />

notion that larger pores decrease deposition onto the membrane at the expense <strong>of</strong><br />

internal adsorption. Long-term trials have revealed that progressive internal deposition<br />

eventually leads to catastrophic increase in resistance (Cho <strong>and</strong> Fane, 2002; Le-Clech<br />

et al., 2003b; Ognier et al., 2002a), as discussed in Section 2.1.4.6. Tests conducted<br />

using a very porous support for the formation <strong>of</strong> a dynamic membrane have yielded<br />

reasonable removal efficiencies <strong>and</strong> permeabilities (Wu et al., 2004), <strong>and</strong> full-scale<br />

installations now exist based on this approach (Section 5.2.5).<br />

Porosity/pore size distribution/roughness <strong>Membrane</strong> roughness <strong>and</strong> porosity were<br />

identified as possible causes <strong>of</strong> differing fouling behaviour observed when four MF<br />

membranes with nominal pore sizes between 0.20 <strong>and</strong> 0.22 �m were tested in parallel<br />

(Fang <strong>and</strong> Shi, 2005). <strong>The</strong> track-etched membrane, with its dense structure<br />

<strong>and</strong> small but uniform cylindrical pores, provided the lowest resistance due to its<br />

high surface isoporosity whereas the other three membranes were more prone to<br />

pore fouling due to their highly porous network. Although all membranes were <strong>of</strong><br />

similar nominal pore size, the PVDF, mixed cellulose esters (MCE) <strong>and</strong> PES membranes<br />

resulted in relative pore resistance <strong>of</strong> 2, 11 <strong>and</strong> 86% <strong>of</strong> the total hydraulic<br />

resistance respectively. It was suggested that membrane microstructure, material<br />

<strong>and</strong> pore openings all affected <strong>MBR</strong> fouling significantly (Fang <strong>and</strong> Shi, 2005). Comparison<br />

between two microporous membranes prepared by stretching demonstrated

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