In: Mechanical Engineering
You are asked to design a piping system to fill an Olympic size swimming pool. The nominal dimensions of the pool are 164 ft long, 82 ft wide and 6 ft deep, and the filling is to take place in 6 hours. The 60 F water supply is contained in a reservoir 75 ft below the nominal elevation of the pool and contains 500 feet of 6-inch diameter cast iron pipe with 4 standard 90° elbows and 1 (fully open) gate valve. The roughness of the pipe is expected to increase as e = e0 + at, where e0 is the roughness value when the pipe is new and a = 0.000168 ft/yr. What size pump (in hp) should be chosen in order for the design to last 20 years?
Given that the size of the pool
length = 164 ft
breadth = 82 ft
Depth = 6 ft
Volume = 80688 ft 3.
Time = 6 hours = 21600 sec
Volume flow rate = Volume / time = 80688 / 21600 = 3.74 ft3/ s
Head = 75 ft
Length of pipe = 500 ft
Number of 90 degree elbows = 4 , K value = 0.75 [ 2*.75 = 1.5]
one Gate valve fully open , k value = 0.17
hmajor_loss = f (l / dh) (v2 / 2 g)
Finding the value of f
We have to find the Reynolds number
Re = D *V / kinematic viscosity
Kinematic viscosity at 60F = 1.210 x10-5 ft2/s
D = 6 inches = 0.5 ft
Velocity = Volume flow rate / Area
Area = * (0.5/2) 2 = 0.19635 ft2.
Velocity = 3.74 / 0.19635 = 19.05 ft/ s
Re = 0.5* 19.05 / 1.210 x 10-5. = 787190 flow is turbulant
k = 0.25 mm for cast iron
d = diameter = 6 inches = 152.4 mm
k/d = 0.002
f value from moodys chart 0.006
Now Hf = f ( L/D ) ( V2/2g) = 0.006 * [ (500/0.5) ( 19.052 / (2* 32.17405)] = 0.006* 5639.677 = 33.84 ft
g= 32.17405 ft/s2
H minor = k * ( V2/2g)
Number of 90 degree elbows = 4 , K value = 0.75 [ 2*.75 = 1.5]
one Gate valve fully open , k value = 0.17
k = 1.5+0.17 = 1.67
H minor = k * ( V2/2g) = 1.67 * ( 19.052 / (2* 32.17405) = 9.45 ft
Total head loss = 33.84 + 9.45 = 43.26 ft
Required head = altitude + head loss = 75 + 43.26 = 118.26 ft
Calculation by roughness
given e = e0 + a *t
e0= 0.010 inches = 0.0008333333 ftroughness of cast iron pipe
e= 0.0008333333 + (0.000168 *20) = 0.0042
f = 0.036 for a turbulant flow the value of f varies from 0.006 to 0.06
Now Hf = f ( L/D ) ( V2/2g) = 0.036 * [ (500/0.5) ( 19.052 / (2* 32.17405)] = 0.006* 5639.677 = 203.04 ft
Total head required = 75 + 203.04 + 9.45 = 287.5 ft.