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Question 15.4: Produce a preliminary design for a sea outfall. The dry weat......

Produce a preliminary design for a sea outfall. The dry weather flow through the outfall is 0.1 m^3 \, s^{-1} and the peak flow is 0.5 m^3 \, s^{-1} . Site investigations show that a sea outfall extending to 2 km seaward would not cause pollution of foreshore and recreational waters. The still water depth there is 15 m. The density of sea water is 1026 kg m^{-3} .
If a minimum dilution of 50 is required, estimate the diameter of the ports, number of ports and the length of the diffuser for still water.

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Cederwall equations (15.35) and (15.36) are used to obtain the following table (choose FD and compute \left.y_0 / D_{ p } \text { for } S_{ m }=50\right) .

Table 1

S_{\mathrm{m}}=0.54\,F D\left(\frac{y_{0}}{D_{\mathrm{p}}F D}\right)^{7/16}\;\;\mathrm{for}\;\;\;\frac{y_{0}}{D_{\mathrm{p}}}\lt 0.5\,F D                (15.35)

S_{\mathrm{m}}=0.54\,F D\left(\frac{0.38y_{0}}{D_{\mathrm{p}}F D}+0.66\right)^{5/3}\ \ \mathrm{for}\ \ \frac{y_{0}}{D_{\mathrm{p}}}≥0.5\,F D.                (15.36)

The diameter of the ports is chosen as 175 mm which is large enough to avoid blockage. The exit velocity is about 2.4 m \, s^{-1} which is less than the highest acceptable velocity of 3 m \, s^{-1} to avoid undue headloss at the exit.
The discharge through the port of 175 mm diameter = 0.06 m^3 \, s^{-1}. Number of ports is 0.5/0.06 = 10 (say). The flow through the ports at DWF = 0.1/10 = 0.01 m^3 \, s^{-1}. The velocity through the ports at DWF

\begin{aligned} & =0.01 /\left(\pi 0.175^2 / 4\right) \\ & =0.4 \,m s ^{-1} . \end{aligned}

Discharge through the ports at peak flow = 0.5/10 = 0.05 m^3 \, s^{-1}. Velocity through the ports at peak flow

\begin{aligned} & =0.05 /\left(\pi \,0.175^2 / 4\right) \\ & =2.1 \,m s ^{-1} \end{aligned}

A velocity of 2.1 m \, s^{-1} is expected to be sufficient to avoid blockage of the ports. Densimetric Froude number

F D=2.1 /(9.81 \times 0.026 \times 0.175)^{0.5}

= 9.9,

y_0 / D_{ p }=15 / 0.175=85.7

From Fig. 15.11, for y_0 / D_{ p }=85.7 \text { and } F D=9.9 ,

w / 2 D_{ p }=15 \text {, }

w = 2 × 15 × 0.17 \simeq6\,{\mathrm{m}}.

The diffuser length = 6 × 10 = 60 m.

Table 1

FD 1 2 5 10 13 15 20 50
y_0 / D_\mathrm{p} 38 49 67 82 88 91 96 100
D_{ \mathrm{p} }( m ) 0.39 0.31 0.22 0.18 0.17 0.165 0.156 0.15
V_{ \mathrm{p} }\left( m s ^{-1}\right) 0.32 0.56 1.2 2.16 2.7 3.1 4.0 9.8
Q_{ \mathrm{p} }\left( m ^3 s ^{-1}\right) 0.038 0.041 0.047 0.057 0.062 0.066 0.076 0.17
15.11

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