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• Investigation into COD removal in each compartment shows that the majority <strong>of</strong> COD was<br />

removed in the first compartment (Figure 4.12). Much <strong>of</strong> the removed COD was retained<br />

particulate material that could not move beyond compartment 1 due to the baffle construction.<br />

The sludge bed created also acted as a filter that ensured good contact between organic<br />

material (particulate or soluble) and <strong>anaerobic</strong> micro-organisms. For very low loading rates,<br />

much <strong>of</strong> the <strong>reactor</strong> volume was not used for biological activity. This was as much a function<br />

<strong>of</strong> the lack <strong>of</strong> sludge present in these compartments as <strong>of</strong> the apparent efficiency <strong>of</strong> the first<br />

compartment. When loading rates increased, it was seen that the amount <strong>of</strong> treatment that<br />

occurred in later compartments increased, as did the sludge load. It was also seen that,<br />

although the contribution to overall COD removal <strong>of</strong> later compartments was low, they<br />

fulfilled an important buffering function to ensure that later compartments were not subject to<br />

low pH values caused by acidogenesis in the early compartments (Section 4.5.3 below).<br />

As may be expected, the rate <strong>of</strong> accumulation <strong>of</strong> sludge in the ABR was directly related to the OLR.<br />

The <strong>reactor</strong> was tested up to hydraulic and organic loading rates approaching 20 h and<br />

0.9 kg COD/m 3 .d respectively, although precise figures cannot be calculated due to uncertainty in flow<br />

rate data. The loading rate was substantially less than the value <strong>of</strong> 1.5 kg CODbiodegradable/m 3 /d proposed<br />

by Lettinga (2001) who indicated that 80 % COD removal could be achieved at a HRT as low as 4 h<br />

for <strong>anaerobic</strong> systems for the pre-treatment <strong>of</strong> <strong>domestic</strong> wastewater in tropical climates.<br />

4.5.3 Phase-separation between compartments<br />

A number <strong>of</strong> authors observed a phase-separation phenomenon during the operation <strong>of</strong><br />

compartmentalised <strong>anaerobic</strong> digesters (Sections 2.5.1.4 and 2.2.3). The following observations were<br />

made in this study:<br />

• In situ pH values may have been lower than those measured because <strong>of</strong> the lag between<br />

sampling and <strong>analysis</strong> (Section 4.4.3)<br />

• pH measurements made on samples taken from within compartments show that significant<br />

acidification occurred in the first compartment at longer retention times. It was inferred that<br />

methanogenesis did not proceed at the same rate as acidogenesis, resulting in the accumulation<br />

<strong>of</strong> VFA and lowering <strong>of</strong> the pH value. However subsequent <strong>analysis</strong> indicated that low pH<br />

values may not necessarily have been due to methanogenesis inhibition (Section 6.4)<br />

• Conventional inhibition terms were used to estimate the extent <strong>of</strong> inhibition <strong>of</strong><br />

methanogenesis that may have occurred as a result <strong>of</strong> low pH values. Significant inhibition <strong>of</strong><br />

methanogenesis is expected in compartment 1, although the extent <strong>of</strong> inhibition decreases in<br />

subsequent compartments.<br />

• pH pr<strong>of</strong>iles for the 60 h and 32 h THRT periods were similar, with pH depression observed in<br />

the first compartment. However, in the 20 h T-HRT, low pH values were observed in the first<br />

three compartments. The difference was attributed to different sludge load pr<strong>of</strong>iles in the<br />

different operating periods. The pH value at the <strong>reactor</strong> outflow during the 20 h THRT period<br />

was similar to those observed in the earlier periods.<br />

These results point to a very useful attribute <strong>of</strong> the ABR in the treatment <strong>of</strong> <strong>domestic</strong> wastewater. The<br />

compartmentalisation <strong>of</strong> the ABR provides a degree <strong>of</strong> phase separation such that hydrolysis and<br />

acidification <strong>of</strong> organic material in the early compartments can proceed at pH values that are lower<br />

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