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• Information about the volume <strong>of</strong> accumulated sludge is important for planning <strong>of</strong> desludging<br />

operations. With the current <strong>reactor</strong> design, desludging would only take place from the upflow<br />

side <strong>of</strong> the <strong>reactor</strong>; hence volume <strong>of</strong> sludge calculated only from the upflow compartments<br />

provides sufficient indication <strong>of</strong> the desludging requirements for the system.<br />

Table 5.3: Results <strong>of</strong> regression <strong>analysis</strong> on solids accumulation in the <strong>pilot</strong>-<strong>scale</strong> ABR during<br />

operation at Kingsburgh WWTP<br />

Phase Calculated<br />

quantity<br />

II Sludge volume m 3 settled<br />

sludge/year<br />

III Sludge volume m 3 settled<br />

sludge/ year<br />

IV Sludge volume m 3 settled<br />

sludge/ year<br />

IV<br />

III/IV<br />

Mass <strong>of</strong> total<br />

solids (dry)<br />

Ratio <strong>of</strong> sludge<br />

volume slopes:<br />

Phase III/Phase IV<br />

Units Average slope <strong>of</strong><br />

regression [Confidence<br />

interval on slope]<br />

kg dry<br />

solids/year<br />

The volume <strong>of</strong> sludge was calculated as follows:<br />

107<br />

Significance <strong>of</strong><br />

regression (P)<br />

2.49 [-1.13, 6.12] 0.128<br />

(not significant)<br />

3.46 [2.28, 4.64] 0.00125<br />

(significant)<br />

0.901 [0.602, 1.20] 5.87 × 10 -6<br />

(highly significant)<br />

60.7 [33.5,87.8] 2.54× 10 -4<br />

(highly significant)<br />

No. <strong>of</strong> observations<br />

used<br />

in regression<br />

- 3.84 [2.55, 6.06] - -<br />

Vt<br />

,<br />

settled sludge =<br />

⎛<br />

y<br />

⎞ ( ) ⎛<br />

y<br />

⎞<br />

⎜∑<br />

( w l)<br />

i ⎟ ⋅ c/s area <strong>of</strong> up - flow compartment<br />

= ⎜∑<br />

i ⎟ ⋅ ⋅<br />

⎝ i ⎠<br />

⎝ i ⎠<br />

Eq. 5-3<br />

where y i is the height <strong>of</strong> settled sludge in compartment i and w and l are the width and length<br />

respectively <strong>of</strong> the upflow side <strong>of</strong> each compartment.<br />

There is a clear difference in the height <strong>of</strong> the beds between the different operating periods, with Phase<br />

II (Figure 5.15) characterised by significantly lower sludge beds than in Phase III and Phase IV.<br />

5.6.1.1 Phase II: Solids levels<br />

There were many sludge washout incidents during Phase II. In these instances, high flow through the<br />

<strong>reactor</strong> (due to poor control <strong>of</strong> feed rate, or sudden emptying following blockage <strong>of</strong> the outlet) caused<br />

high internal flows with high upflow velocities, and carryover <strong>of</strong> sludge. Greatest settled sludge bed<br />

height was usually found in compartment 2, although the difference between compartments was<br />

generally not great. Figure 5.15(b) seemed to show a slight increase in volume <strong>of</strong> sludge with time<br />

during Phase II. However, a regression <strong>analysis</strong> showed that there was no significant increase in<br />

accumulated sludge volume with time, due to the small number <strong>of</strong> observations and the significant<br />

scatter in the data (Table 5.3). Furthermore, such a correlation would not provide any indication <strong>of</strong><br />

sludge volume accumulation rates under stable operation due to the many sludge washout events in<br />

this phase.<br />

5.6.1.2 Phase III: Solids levels<br />

A gradual increase in the overall sludge bed height with time is observed in Phase III.<br />

Figure 5.16(b) shows a consistent increase in sludge bed volume from day 53 onwards. (In the period<br />

5<br />

6<br />

20<br />

17

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