The MBR Book: Principles and Applications of Membrane
The MBR Book: Principles and Applications of Membrane
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