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The MBR Book: Principles and Applications of Membrane

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Main permeate<br />

header<br />

Permeate pump<br />

ZeeWeed ® membrane<br />

cassettes<br />

Air separator<br />

Air header<br />

Figure 5.26 A single train <strong>of</strong> 16 cassettes<br />

Permeate header<br />

Case studies 239<br />

the on cycle), equating to a SAD m <strong>of</strong> 0.29 Nm 3 /h per m 2 . This is sufficient to maintain<br />

a mean net flux <strong>of</strong> 17–19 LMH <strong>and</strong> a TMP <strong>of</strong> 0.1–0.2 bar, yielding a permeability <strong>of</strong><br />

�144 LMH/bar. <strong>The</strong> SAD p is thus 15–17 m 3 air per m 3 . <strong>The</strong> typical totalised flow<br />

through the membrane per month is �1Mm 3 , <strong>and</strong> the typical maximum totalised<br />

daily flow <strong>of</strong> �40 800 m 3 .<br />

Maintenance cleaning in situ is conducted weekly using 500 mg/L NaOCl at pH<br />

8–8.5. <strong>The</strong> chemical is back-pulsed slowly through the membrane, whilst still<br />

immersed in the mixed liquor, for a period <strong>of</strong> 45 min. Only two recovery cleans, that<br />

is ex situ chemical cleaning by soaking the membranes in 1000 mg/L NaOCl for 6 h,<br />

were performed over the first 30 months <strong>of</strong> operation, with none conducted over the<br />

first year.<br />

To date, there have been no operational problems with this plant, other than one<br />

foaming incident which dem<strong>and</strong>ed dosing with anti-foaming agent during the first<br />

2 months during start-up <strong>of</strong> the system (Côté et al., 2004). Effluent quality has met<br />

or exceeded expectations for SS, BOD, Ammonia-N <strong>and</strong> TN. <strong>The</strong> high-quality <strong>MBR</strong><br />

effluent is blended with effluent from the conventional trains A <strong>and</strong> C, allowing the<br />

overall plant to meet present discharge st<strong>and</strong>ards. <strong>The</strong> <strong>MBR</strong> effluent quality is also <strong>of</strong><br />

high-enough quality to be considered for reuse as irrigation water.<br />

5.3.1.3 Nordkanal wastewater treatment works at Kaarst<br />

Background <strong>and</strong> plant description <strong>The</strong> plant at Kaarst in Germany, owned <strong>and</strong> operated<br />

by the Erftverb<strong>and</strong> (Erft Association), treats wastewater from the nearby towns <strong>of</strong><br />

Kaarst, Korschenbroich <strong>and</strong> Neuss. It was installed <strong>and</strong> commissioned in January<br />

2004 following the success <strong>of</strong> the group’s first <strong>MBR</strong> plant at Rödingen, a smaller plant<br />

which was commissioned in 1999 (Table 5.14). As <strong>of</strong> November 2005, the Kaarst<br />

plant was the largest <strong>MBR</strong> plant in the world, with a population equivalent <strong>of</strong><br />

80 000 <strong>and</strong> a capacity <strong>of</strong> 48 MLD.<br />

<strong>The</strong> site has five buildings which, respectively, house the sludge mechanical dewatering<br />

process, the fine screens, the coarse screen, the <strong>MBR</strong> <strong>and</strong> the process controls.<br />

Additional installations include lidded sludge <strong>and</strong> sludge liquor holding tanks, a grit

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