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In-house modifications can result in a reduction of the contaminant load discharged from<br />

a plant but may not result in a reduction of the contaminant concentrations of the effluent.<br />

This is due to the fact that contaminant loadings and effluent flows may be reduced by<br />

similar margins. Therefore, effluents may continue to exceed discharge limitations or may<br />

exceed the limits above which surcharges have to be paid.<br />

7.2.9 Wastewater Treatment<br />

Suppliers and manufacturers of wastewater treatment equipment were requested to<br />

provide cost estimates for equipment required to treat a range of flows. The type of<br />

treatment processes selected included fine screening using 600 mm, 500 mm, and<br />

150 mm screens, and dissolved air flotation (DAF). The cost estimates were used to<br />

calculate the range of treatment costs per discharge flow (see Figure 7.3)<br />

A rule-of-thumb markup of 50% of the original cost estimates to account for taxes and<br />

installation was assumed for the calculations. The results are shown for the flow range<br />

of 100 m 3<br />

/day to 6000 m3/day. Cost estimates for DAF do not include any sludge<br />

dewatering equipment, or the cost of waste disposal. Costs also exclude in-plant<br />

modifications to piping, yard work, power supply, and equipment housing which are site<br />

specific which can easily double the total capital cost.<br />

The efficiencies expected for each individual treatment option, shown in Table 7.3, are<br />

based on file data and literature values, as detailed process evaluations could not be<br />

obtained from the manufacturers/suppliers. The, efficiency of a particular wastewater<br />

treatment system is dependent on the nature of the wastewater to be treated. For<br />

example, with respect to screening, the treatment efficiency is dependent on the size<br />

distribution of the particles in the wastewater. If all particles (suspended solids) present<br />

in the wastewater are larger than the openings of the screen to be used, all particles and<br />

the BOD associated with them can be removed. Conversely, suspended solids removal<br />

may not increase much after the installation of finer screens, if the majority of the solids<br />

are too small to be retained by the screen. In addition, screens will not affect dissolved<br />

substances and the BOD which is associated with them. This dissolved BOD may,<br />

however, be removed by chemically assisted DAF.

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