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The MBR Book: Principles and Applications of Membrane

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

Table 2.9 Influence <strong>of</strong> shift in MLSS concentration (g/L) on <strong>MBR</strong> fouling<br />

MLSS shift Details Reference<br />

(g/L)<br />

Fouling increase<br />

0.09–3.7 Cake resistance: 21–54 1011 /m <strong>and</strong><br />

�: 18.5–0.7 10<br />

Chang <strong>and</strong> Kim (2005)<br />

8 m/kg<br />

2.4–9.6 Total resistance: 9–22 1011 /m Fang <strong>and</strong> Shi (2005)<br />

7–18 Critical flux: 47–36 LMH (for SRT<br />

<strong>of</strong> 30–100 days)<br />

Han et al. (2005)<br />

2.1–9.6 Critical flux: 13–8 LMH Bin et al. (2004)<br />

1–10 Critical flux: 75–35 LMH Madaeni et al. (1999)*<br />

2–15 “Limiting flux”: 105–50 LMH Cicek et al. (1998)*<br />

1.6–22<br />

Fouling decrease<br />

“Stabilized flux”: 65–25 LMH Beaubien et al. (1996)*<br />

3.5–10<br />

No (or little) effect<br />

Critical flux: �80, �60 LMH Defrance <strong>and</strong> Jaffrin (1999)*<br />

4.4–11.6 No impact between 4 <strong>and</strong> 8 g/L,<br />

Slightly less fouling for 12 g/L<br />

Le-Clech et al. (2003c)<br />

4–15.1 Critical flux decreased from<br />

25 to 22 LMH<br />

Bouhabila et al. (1998)<br />

3.6–8.4 Hong et al. (2002)<br />

*s<strong>MBR</strong><br />

concentration has a negative influence has been reported (30 g/L, according to<br />

Lubbecke et al., 1995). A more detailed fouling trend has been described (Rosenberger<br />

et al., 2005), in which an increase in MLSS reduced fouling at low MLSS levels (�6 g/L)<br />

whilst exacerbating fouling at MLSS concentrations above 15 g/L. <strong>The</strong> level <strong>of</strong> MLSS<br />

did not appear to have a significant effect on membrane fouling between 8 <strong>and</strong> 12 g/L.<br />

In another study <strong>of</strong> MLSS concentration impacts (WERF, 2005), it was concluded that<br />

hydrodynamics (more than MLSS concentration) control the critical flux at MLSS levels<br />

above 5 g/L.<br />

Contradictory trends from data obtained in the same study are apparent. For<br />

example, the cake resistance (R c) has been observed to increase <strong>and</strong> the specific cake<br />

resistance (�, the resistance per unit cake depth) to decrease with increasing MLSS,<br />

indicating that the bulk cake becomes more permeable. Bin et al. (2004) observed<br />

the permeate flux to decrease (albeit at a reduced fouling rate) with increasing<br />

MLSS. This was attributed to the rapid formation <strong>of</strong> a fouling cake layer (potentially<br />

protecting the membrane) at high concentration, while progressive pore blocking<br />

created by colloids <strong>and</strong> particles was thought to take place at lower MLSS concentrations<br />

when the membrane was less well protected. This may well explain the subcritical<br />

fouling behaviour depicted in Fig. 2.14.<br />

Empirical relationships predicting flux from MLSS level have been proposed in<br />

a number <strong>of</strong> papers (Fang <strong>and</strong> Shi, 2005; Krauth <strong>and</strong> Staab, 1993; Sato <strong>and</strong> Ishii,<br />

1991; Shimizu et al., 1996). However, these equations have limited use as they are<br />

generally obtained under very specific conditions <strong>and</strong> are based on a limited number<br />

<strong>of</strong> operating parameters, whilst other parameters are disregarded. A mathematical<br />

expression linking MLSS concentration, EPS <strong>and</strong> TMP with specific cake resistance

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