Question 11.8: Two reservoirs open to atmosphere are connected by a pipe 80...

Two reservoirs open to atmosphere are connected by a pipe 800 metres long. The pipe goes over a hill whose height is 6 m above the level of water in the upper reservoir. The pipe diameter is 300 mm and friction factor f = 0.032. The difference in water levels in the two reservoirs is 12.5 m. If the absolute pressure of water anywhere in the pipe is not allowed to fall below 1.2 m of water in order to prevent vapour formation, calculate the length of pipe in the portion between the upper reservoir and the hill sumit, and also the discharge through the pipe. Neglect bend losses. Draw the equivalent electrical network system.

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Let the length of pipe upstream of C be L1L_{1} and that of the downstream be L2L_{2} (Fig. 11.20a).

 

It is given L1+L2=800L_{1}+L_{2}=800 m

 

Considering the entry, friction and exit losses,

 

the total loss from A to C =hf1=(0.5+0.032L10.3)V22g=h_{f 1}=\left(0.5+\frac{0.032 L_{1}}{0.3}\right) \frac{V^{2}}{2 g} (11.47)

 

the total loss from C to B =hf2=(1+0.032L20.3)V22g=h_{f 2}=\left(1+\frac{0.032 L_{2}}{0.3}\right) \frac{V^{2}}{2 g}

 

Therefore,

 

the total loss from A to B =hf=(0.5+0.032×8000.3+1)V22g=h_{f}=\left(0.5+\begin{array}{c}0.032 \times 800 \\0.3\end{array}+1\right) \begin{array}{l}V^{2} \\2 g\end{array}

 

=86.83V22g=86.83 \frac{V^{2}}{2 g}

 

Applying Bernoulli’s equation between A and B, we have

 

ΔH=hf\Delta H=h_{f}

 

or 12.5=86.83V22g12.5=86.83 \frac{V^{2}}{2 g}

 

which gives V=12.5×2×9.8186.83=1.68V=\sqrt{\frac{12.5 \times 2 \times 9.81}{86.83}}=1.68 m/s

 

Applying Bernoulli’s equation between A and C, we have

 

patmρg=pcρg+V22g+6+hf1\begin{array}{c}p_{ atm } \\\rho g\end{array}=\frac{p_{c}}{\rho g}+\frac{V^{2}}{2 g}+6+h_{f_{1}} (11.48)

 

With the atmospheric pressure

 

patm=760mm of Hgp_{ atm }=760 mm \text { of } Hg

 

=760×13.61000=10.34=\frac{760 \times 13.6}{1000}=10.34 m of water,

 

Equation (11.47) becomes

 

10.34=1.2+6+(1.68)22×9.81+hf110.34=1.2+6+\frac{(1.68)^{2}}{2 \times 9.81}+h_{f 1}

 

which gives hf1=2.99h_{f 1}=2.99 m

 

Using the value of hf1h_{f 1} = 2.99 m, and V = 1.68 m/s in Eq. (11.47) we get

 

(0.5+0.107L1)(1.68)22×9.81=2.99\left(0.5+0.107 L_{1}\right) \frac{(1.68)^{2}}{2 \times 9.81}=2.99

 

or 0.5+0.107L1=20.780.5+0.107 L_{1}=20.78

 

which gives L1=189.53L_{1}=189.53 m

 

Rate of discharge through the pipe

 

Q=π4(0.3)2×1.68=0.119Q=\frac{\pi}{4}(0.3)^{2} \times 1.68=0.119 m3/sm ^{3} / s

 

The equivalent electrical network of the system is shown in Fig. 11.20b.

1.8

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