9420.pdf
9420.pdf
9420.pdf
You also want an ePaper? Increase the reach of your titles
YUMPU automatically turns print PDFs into web optimized ePapers that Google loves.
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.