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The MBR Book: Principles and Applications of Membrane

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Case studies 215<br />

area <strong>of</strong> 15 840 m 2 . This plant operates under similar aeration conditions as that <strong>of</strong><br />

Porlock <strong>and</strong> also operates with manual diffuser flushing with no diffuser air-scour.<br />

<strong>The</strong> most recent Kubota <strong>MBR</strong> plants installed for sewage treatment in the UK have<br />

an automated diffuser maintenance programme, whereby they are periodically flushed<br />

with water <strong>and</strong> air-scoured. It is generally recognised by the operator that these plants<br />

require careful maintenance to suppress clogging (or sludging), since the filling <strong>of</strong> the<br />

channels with sludge represents a very significant constraint to the viable operation <strong>of</strong><br />

these plant. To this end, more conservative peak fluxes <strong>of</strong> 27 LMH appear to be appropriate,<br />

though mean operating fluxes are much lower, coupled with rigorously cleaned<br />

aerators to maintain the aeration rate, <strong>and</strong> thus air-scour, in the membrane flow<br />

channels.<br />

5.2.1.3 Daldowie<br />

Sludge liquor <strong>and</strong> treatment <strong>The</strong> plant at Daldowie is a sludge liquor treatment plant<br />

owned <strong>and</strong> operated by Scottish Water. Sludge liquor is the aqueous fraction <strong>of</strong><br />

sewage sludge which has undergone dewatering by processes such as belt pressing,<br />

rotary drum vacuum filtration <strong>and</strong> centrifugation following conditioning with coagulant<br />

<strong>and</strong>/or polymeric flocculant reagents. It may contain up to 25% <strong>of</strong> the TN load<br />

in the original sludge <strong>and</strong> contribute as little as 2% <strong>of</strong> the total influent flow. It is thus<br />

highly concentrated in ammonia (Table 5.3), as well as in dissolved organic matter.<br />

Composition <strong>and</strong> flow are extremely variable <strong>and</strong> dependent on the upstream sludge<br />

h<strong>and</strong>ling <strong>and</strong> treatment processes. Whilst the most economical option is to return<br />

the liquor to the head <strong>of</strong> works, this is not always possible either due to logistical limitations<br />

or due to the excessive load it would place on the existing sewage treatment<br />

process. Under such circumstances, a number <strong>of</strong> options for its treatment can be considered<br />

(Table 5.4). Of key importance in choosing the most suitable option are confidence<br />

in a robust solution, cost <strong>and</strong> environmental factors such as the impact <strong>of</strong> the<br />

wastes generated. Speed <strong>of</strong> start-up may also be <strong>of</strong> importance if the plant will only<br />

run seasonally.<br />

Plant design <strong>and</strong> operation As is <strong>of</strong>ten the case for this duty, the choice <strong>of</strong> technology<br />

at Daldowie was seen as being between a sequencing batch reactor (SBR) <strong>and</strong> an<br />

<strong>MBR</strong>. However, the large fluctuations in organic loading arising from periodical<br />

releases <strong>of</strong> poor-quality effluent from the centrifuges <strong>and</strong> the belt presses meant that<br />

operation <strong>of</strong> an SBR was seen as being more problematic than the <strong>MBR</strong>. This was<br />

Table 5.3 Sludge liquor properties<br />

Parameter Average concentration Range (mg/L)<br />

(mg/L)<br />

BOD 1221 162–3004<br />

COD 941 470–1411<br />

NH 4-N 750 162–1218<br />

SS 1442 50–5000<br />

Alkalinity 2200 1900–2500<br />

pH 7.2 7–7.5

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