Water flows at a rate of 0035 m3s in a horizontal pipe whose
Solution
16-2
Q=0.035 m3/s
Flow area of 15 cm pipe=A1=0.017671 m2
A2=0.005027 m2
Velocities
V1=Q/A1=1.924 ft/s
V2=Q/A2=6.963 ft/s
From frictionless Bernoulli equation (with water density 1000 kg/m3)
P1/1000g+V12/2g=P2/1000g+V2\'2/2g where V2\'= velocity considering frictionless flow
But P1=480 kPa
P2=445 kPa
Hence
V2\'2=2x9.81x[(4.81-4.45)x105/1000x9.81+1.9242/(2x9.81)]
=73.7 m2/s2
Hence irreversible head loss
(V2\'2-V22)/2g/(kinetic energy correction factor
=(73.7-6.9632)/(2x9.81x1.05)
=1.22 mWC
16-3
Total head at pump suction (in gage pressure)
=Ps= Total head at bottom of tank =20 m, since velocity is negligible at bottom of tank
Total head at exit of nozzle
Pd= 27m , since presssure is atmospheric at exit of nozzle
Hence the pressure rise supplied by pump
=Pd-Ps=27-20=7 m

