$1.(25$ pt$)$ The pump delivers water at $68$ deg F $($ $=1\mathrm{.}937$slug$/$ft$3$

$,$

$=2\mathrm{.}09$x$105$ lbf$-$s$/$ft$2)$ from the lower reservoir to the upper reservoir at a rate of

$1000$ gpm$.$ Both reservoirs are open to the atmosphere through vents. The pipe is

commercial steel, $6$ in Schedule $40($inner diameter $6\mathrm{.}065$ in$).$ The total combined

length of suction and discharge pipes is $200$ ft$.$ The pipe system has one globe

valve and $3$ standard $90$ deg elbows. Assume the entrance to the pipe from the

lower reservoir to be $$inward projecting$.$ Note that $$ft$$ for the expressions in the

loss coefficients table are not length. They are a factor that multiplies the number

to get K$.$ Use ft$=0\mathrm{.}018$

$($a$)(5$pt$)$ State all minor losses and give the loss coefficient for each. Sum the loss

coefficients and give total loss coefficient.

$($b$)(5$ pt$)$ Calculate the total friction loss $($major and minor$).$

$($c$)(10$ pt$)$ For the conditions given in the figure below, compute the head, hp $,$ delivered

by the pump.

$($d$)(5$ pt$)$ Compute the power added to the fluid by the pump in horsepower and the

power that must be supplied by the motor if the pump efficiency is $75$ percent.