Ans a) Apply Bernoulli equation between point C located at water surface elevation of tank and at point A respectively,
/
+
/2g +
=
/
+
/2g +
+ Hf
Since, point C is open to atmosphere, pressure is only
atmospheric hence, gauge pressure
= 0
Velocity at surface is negligible so, Vc = 0
Elevation from datum,
= h and
= 0
Velocity at point A = Flow rate / Area
Flow rate = 1500 gal/min or 3.33 cfs
Area = (/4)
Diameter at point A = 10 in or 0.833 ft
=> Area = (/4)
= 0.5447 sq.ft
=> Velocity at point A,
= 3.33 / 0.5447 = 6.11 ft/s or 1.86 m/s
Frictional head loss, Hf = 6.94 m
Putting values in Bernoulli equation,
0 + 0 + h = (-35.5/9.81) +
/ (2 x 9.81) + 0 + 6.94
=> h = -3.62 + 0.176 + 6.94
=> h = 3.5 m
Hence, required height 'h' = 3.5 m
Ans b) Apply Bernoulli equation between point A and B respectively,
/
+
/2g +
+ Hp =
/
+
/2g +
+
Given, pressure difference,
-
= 551 kPa
Velocity at point B = Flow rate / Area
Diameter at point B = 8 in or 0.75 ft
=> Area = (/4)
= 0.441 sq.ft
=> Velocity at point A,
= 3.33 / 0.441 = 7.55 ft/s or 2.3 m/s
Hp is Head added by pump
Elevation ,
= 0 and
= 7.62 m
is frictional head loss between A and B
Also,
= f L
/ 2 g D
To determine friction factor, calculate Reynold number (Re)
Re = V D /
Pipe diameter = 8 in or 0.20 m
Kinematic viscosity of water =
m2/s
=> Re = 2.3 x 0.20 /
=> Re = 460000
Roughness of steel pipe = 0.045 mm
Relative roughness,e/D = 0.045 / 200 = 0.000225
According to Moody diagram for Re = 460000 and e/D = 0.0000225, friction factor (f) = 0.016
=>
= 0.016(792.5)
/(2
x 9.81 x 0.20)
=>
= 17.1 m
Putting values in Bernoulli equation,
=>
/ (2 x 9.81) + 0 + Hp = (551 / 9.81) +
/ (2 x 9.81) + 7.62 + 17.1
=> 0.176 + Hp = 56.16 + 0.27 + 24.72
=> Hp = 81 m or 265.75 ft
We know, power (P) =
Q Hp
=> P = 62.4 x 3.33 x 265.75
=> P = 55221 lb ft/s or 100.4 hp
Hence, power delivered by pump to water is 100.4 hp
The figure below shows a portion of a fire protection system in which a pump draws...
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