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from the clarified zone between the sludge and scum layers. The outlet is usually fitted with an<br />

effluent screen and/or a tee-piece to retain larger solids that would otherwise be carried out in the<br />

effluent to the soak-away, contributing to clogging and eventual system failure. Inspection ports and<br />

manholes are provided in the tank cover to allow access for the periodic removal <strong>of</strong> tank contents,<br />

including the accumulated scum and sludge.<br />

Compartmentalised tanks such as that shown in Figure 2.6, or tanks placed in series are reported to<br />

provide better suspended solids removal than single-compartment tanks alone, although results from<br />

different studies vary.<br />

Septic tanks are reported to remove 60 to 80% <strong>of</strong> non-soluble material in <strong>domestic</strong> wastewater. Solid<br />

and colloidal material is hydrolysed and acidified, producing volatile fatty acids that are only partially<br />

converted to CH4, and exit in the effluent stream. Biological oxygen demand (BOD) removal is<br />

typically in the order <strong>of</strong> 30 to 50% for a septic tank operating at a 48 h retention time. Actual<br />

performance <strong>of</strong> the septic tank will depend on the ambient temperature, operating hydraulic retention<br />

time and presence <strong>of</strong> inert or micro-organism-inhibiting chemicals in the influent. Table 2.3 presents<br />

septic tank effluent characteristics from a number <strong>of</strong> systems, before secondary treatment in a soakaway<br />

or other system.<br />

Soak-away systems provide a degree <strong>of</strong> wastewater treatment and dispersal through soil purification<br />

processes and ground water recharge. The performance is dependent on the treatment efficiency <strong>of</strong> the<br />

septic tank, the method <strong>of</strong> wastewater distribution and loading to the soil infiltrative surface, and the<br />

properties <strong>of</strong> the vadose and saturated zones underlying the infiltrative surface. Considerable data on<br />

the treatment efficiency <strong>of</strong> soak-away systems are available in the trade literature (USEPA, 2002).<br />

High removal rates <strong>of</strong> BOD, suspended solids, faecal coliforms and surfactants have been observed<br />

within a few metres <strong>of</strong> unsaturated, aerobic soil. Phosphorus and metals are removed through<br />

adsorption, ion-exchange and precipitation reactions, although the retention capacity <strong>of</strong> the soil has a<br />

limit that depends on specific soil properties including soil mineralogy, organic content, pH, redox<br />

potential, and cation exchange capacity. Pathogen survival rates have been found to vary with a<br />

number <strong>of</strong> factors including initial pathogen load, temperature, humidity and solar radiation.<br />

Table 2.4 shows typical pathogen survival times in fresh water, sewage and unsaturated soil at 20 ºC<br />

to 30 ºC (Feachem et al., 1983). Bacterial and protozoan pathogens have relatively short survival times<br />

(less than a month), but viruses and helminth eggs (e.g. Ascaris spp.) can survive for considerably<br />

longer periods.<br />

31

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