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Question of Save & Exit Submit It is proposed to run a pump at 880 rpm to pump water at 20°C through the system of the image
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Answer #1

Ans)  Apply Bernoulli equation between point 1 and 2 located at water surface elevation of lower and upper reservoir respectively,

P1/\gamma + V1 / 2g + Z1 + Hp = P2/\gamma + V22 / 2g + Z2 + Hf

Since,both point 1 and 2 are open to atmosphere, pressure is only atmospheric,hence gauge pressure, P1 = P2 = 0

Velocity at surface is negligible so, V1 = V2 = 0

Elevation, Z1 = 4 m and Z2 = 11 m

Hp is pump head

Hf = Head loss due to friction  

  Hence, above equation reduces to,

0 + 4 + Hp = 0 + 11 + Hf

=> Hp= 7 + Hf...................................(1)

Also, Hf = 8 f L Q^2 / (\pi^2 g D^5 )

Assume fully developed turbulent flow to determine friction factor, f

f = 1 / [1.14 + 2Log(D/e)]^2

Riughness of steel pipe (e) = 0.046 mm

=> f = 1 / [1.14 + 2Log(200/0.046)]^2

=> f = 0.014

Hence, Hf = 8 (0.014)(40) Q^2 / (\pi^2 x 9.81 x 0.2^5 )

=> Hf = 144.74 Q^2

Putting values in equation 1,

Hp = 7 + 144.74 Q^2

The above equation is system head curve equation where Q is in m3/s and Hp is in meter

Q (gal/min) Q (m3/s) Hp (m) Hp (ft)
0 0 7 23
2000 0.126 9.30 30.50
4000 0.252 16.20 53.15
6000 0.378 27.68 90.81
8000 0.504 43.76 143.57
10000 0.63 64.44 211.41

Now plot the system curve on given pump performance curve as shown below :

Now, we know the point of intersection of performance curve and system curve is operating point.Hence,

Operating discharge = 5600 gpm or 12.43 cfs or 745.8 ft^3 /min

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