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and 4, with decreasing observations <strong>of</strong> these micro-organisms in dispersed sludge <strong>of</strong> later<br />

compartments. This implies that partial phase separation has occurred between the first and subsequent<br />

compartments with hydrolysis and acidogenesis predominating in the first compartment and<br />

establishment <strong>of</strong> acetoclastic methanogenesis thereafter.<br />

These results confirm the hypotheses presented in Sections 5.6.1.4 and 5.6.2 that proposed that high<br />

solids accumulation rates (normalised for OLR) in Phase III compared to those in Phase IV were due<br />

to the establishment <strong>of</strong> a stable <strong>anaerobic</strong> population at the lower flow rate <strong>of</strong> Phase IV. As the<br />

concentrations <strong>of</strong> soluble components in the <strong>pilot</strong>-<strong>scale</strong> ABR are relatively low during the treatment <strong>of</strong><br />

<strong>domestic</strong> sewage, the cause <strong>of</strong> the differences in population stability between the different flow rates<br />

must be due to the higher upflow velocities employed in Phase III resulting in the washout <strong>of</strong><br />

<strong>anaerobic</strong> micro-organisms. Thus it may be concluded that the upflow velocity in each compartment is<br />

a critical design factor that must be considered in conjunction with A-HRT and OLR when sizing a<br />

<strong>baffled</strong> <strong>reactor</strong> for the treatment <strong>of</strong> <strong>domestic</strong> sewage.<br />

5.8 SUMMARY OF OPERATION AT KINGSBURGH WASTEWATER TREATMENT PLANT<br />

Table 5.5 and Table 5.6 (pages 117 and 127) are summaries <strong>of</strong> all inflow and outflow measurements<br />

averaged for operation <strong>of</strong> the <strong>pilot</strong>-<strong>scale</strong> ABR at Kingsburgh WWTP for Phase II, III and IV. In the<br />

sections that follow, the main conclusions drawn from the data presented in this chapter are<br />

summarised.<br />

5.8.1 Outflow characteristics<br />

Substantial reductions in COD were observed in all operating periods, with lowest values (around<br />

130 mgCOD/ℓ) measured in Phase IV. A number <strong>of</strong> factors contributed to the best performance being<br />

observed in Phase IV:<br />

• The ABR was operated at low flow rates, resulting in low upflow velocity and therefore good<br />

solids retention characteristics and development <strong>of</strong> a balanced <strong>anaerobic</strong> population to<br />

facilitate digestion.<br />

• The low feed rate in Phase IV corresponded to a low OLR.<br />

• Significant improvements in management and control <strong>of</strong> the <strong>pilot</strong>-<strong>scale</strong> ABR resulted in fewer<br />

sludge loss incidents<br />

Anaerobic treatment <strong>of</strong> <strong>domestic</strong> wastewater in the ABR caused a net increase in alkalinity and free<br />

and saline ammonia concentrations, and a slight decrease in TKN. A small amount <strong>of</strong> sulphate in the<br />

feed stream was removed by the ABR. Nitrate present in the wastewater was expected to be<br />

completely removed within the first one or two compartments <strong>of</strong> the system. Phosphate in the inflow<br />

stream was not expected to change as a result <strong>of</strong> treatment in the ABR. The ABR outlet stream<br />

therefore contained increased concentrations <strong>of</strong> alkalinity and free and saline ammonia and similar<br />

concentrations <strong>of</strong> phosphate compared to the influent wastewater. No sulphate or nitrate was detected<br />

in the outlet stream.<br />

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