Question

EXAMPLE 1-1 Apply the energy equation to the situation sketched in Fig. 1-10 Solution. T upper reservoir to the free surface at position 2 of the lower reservoir. The results, wit!h cach loss term identified, are he energy equation will be applied from the free surface at position I of the 4 K, Y 2g (entrance) (pipe (eibow) friction)Water Ly, De Fittings rwentory·Example 1-11: FIGURE 1-10 Example 1- System sketch for 2 reducing elton 1 engle vaive (pipe elow) (pipe (l (exit) friction) friction) From Fig. 1-10, we obtain and from the continuity equation for incompressible steady flow, we find that which, for circular pipes, becomes Substitution of the preceding into the energy equation yields after applying some algebra Until additional information is specified, we cannot proceed any further than this

to solve one design problem. You can use a programming language you are comfortable with (python, C++, Java etc.)

Question -1 specify the nominal size of clean commercial pipes required for a flow rate of 0.2 ft3/sec if the following are given

Da=Db=Dc

La=200ft

Lb=40ft

Lc=160ft

H=75 ft

0 0
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Answer #1

Ans:

For this system we use the equation :

H = v2/2g[ ka + f/D(La + Lb + Lc) + 2Kb + Kv + Ke ]

For the loss coefficients,

Ka = 0.78

Kb = 30 fT

Kv = 55 fT

Ke = 1

The final equation : 75 = V2/2g[ 400f/D + 115 fT + 1.78 ]

Where fT = the turbulent friction factor

Here We use the diameter as the iteration variable and compute the head

D (ft)

ϵ/D

V (ft/s)

ReD (*105)

F

fT

[ 400f/D + 115 fT + 1.78 ]

H (ft)

0.1

0.00150

25.46

1.819

0.0228

0.023

95.625

963.65

0.2

0.00075

6.37

9.095

0.0213

0.018

46.45

29.30

0.15

0.00100

11.32

1.213

0.0216

0.020

61.68

122.88

0.14

0.00107

12.99

1.299

0.0218

0.020

66.36

174.10

0.145

0.00103

12.10

1.254

0.0217

0.020

63.94

145.54

0.147

0.00102

11.78

1.237

0.0216

0.020

58.77

126.79

0.146

0.00103

11.95

1.246

0.0217

0.020

63.53

141.053

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