Extend the siphon analysis of Example 3.14 to account for friction in the tube, as follows. Let the friction head loss in the tube be correlated as $5.4\left(V_{\text {tube }}\right)^{2} /(2 g),$ which approximates turbulent flow in a 2 -m-long tube. Calculate the exit velocity in $\mathrm{m} / \mathrm{s}$ and the volume flow rate in $\mathrm{cm}^{3} / \mathrm{s},$ and $\mathrm{com}-$ pare to Example 3.14.