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efore this, there were two incidents that may have caused washout <strong>of</strong> sludge, on day 14 and day 36.<br />

these incidents resulted in reduction <strong>of</strong> the sludge bed volume and thus data before day 36 were not<br />

included in the regression.) The regression considers 53 days <strong>of</strong> stable operation from day 53 to day<br />

106. The regression was found to be significant (Table 5.3) and the sludge volume increased at a rate<br />

in the 95% confidence interval from 6.2 to 12.7 ℓ/d.<br />

In Phase III, there were few sludge washout incidents and there was a much less even distribution <strong>of</strong><br />

sludge between compartments (Figure 5.16 a). The average sludge bed height was more than double<br />

that observed in Phase II, and the highest sludge bed was usually observed in compartment 1.<br />

5.6.1.3 Phase IV: Solids levels<br />

In Phase IV, the flow rate and applied OLR were reduced. Operation was stable as a result <strong>of</strong><br />

improvements in the control algorithm, and few incidents <strong>of</strong> any kind were observed. There were no<br />

significant sludge washout incidents. The average height <strong>of</strong> the sludge beds (Figure 5.17 b) increased<br />

at a slower rate than in Phase III, and the shape <strong>of</strong> the pr<strong>of</strong>iles also changed, with higher settled sludge<br />

beds in the earlier compartments (Figure 5.17 a). Figure 5.17 (b) presents the calculated sludge<br />

volume in the upflow compartments <strong>of</strong> the <strong>pilot</strong>-<strong>scale</strong> ABR for Phase IV operation with a linear<br />

regression between time and sludge load. The linear regression was highly significant (Table 5.3) and<br />

the regressed slope <strong>of</strong> sludge volume accumulation was found to fall in the 95% confidence interval<br />

from 1.6 to 3.3 ℓ/d.<br />

For Phase IV, total solids data were also available for the average concentration in the upflow side <strong>of</strong><br />

each compartment.<br />

ABR solids load<br />

[kg dry solids]<br />

60<br />

50<br />

40<br />

30<br />

20<br />

10<br />

0<br />

May04<br />

Jun04<br />

Jul04<br />

0 50 100 150 200<br />

Phase IV: Time [d]<br />

Figure 5.18: Phase IV: Mass <strong>of</strong> total solids (dry) in the upflow compartments <strong>of</strong> the <strong>pilot</strong>-<strong>scale</strong><br />

ABR showing linear regression line with 95% confidence interval on the<br />

regression (------).<br />

A total solids load was calculated for the <strong>pilot</strong>-<strong>scale</strong> ABR analogous to the total settled sludge volume<br />

according to Eq. 5-4:<br />

TS<br />

t<br />

( C ⋅Y<br />

) ⎞<br />

⋅ ( c/s<br />

area <strong>of</strong> up - flow compartment)<br />

=<br />

⎛ ( C ⋅Y<br />

) ⎞<br />

⋅ ( w ⋅ l)<br />

=<br />

⎛<br />

⎜<br />

∑<br />

⎝<br />

⎠<br />

⎝<br />

∑ TS , i i,<br />

max ⎟<br />

⎜ TS , i i,<br />

max<br />

i<br />

i<br />

108<br />

Eq. 5-4<br />

Where CTS,i is the average total solids concentration in a mixed core sample from compartment i, Yi,max<br />

is the maximum height <strong>of</strong> compartment i and w and l are compartment width and length respectively.<br />

Aug04<br />

Sep04<br />

⎟<br />

⎠<br />

Oct04<br />

0.1

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