| A | B | C | D | E | F | G | H | I | J | K | L | M | |
|---|---|---|---|---|---|---|---|---|---|---|---|---|---|
1 | Pipe Flow/Friction Factor Calculations I: (S.I. units) | ||||||||||||
2 | Calculation of Head Loss, hL, or Frictional Pressure Drop, DPf, | ||||||||||||
3 | for given flow rate, Q, pipe diam., D, pipe length, L, | ||||||||||||
4 | pipe roughness, e, and fluid properties, r & m. | ||||||||||||
5 | Written by: Harlan Bengtson | ||||||||||||
6 | |||||||||||||
7 | 1. Determine Friction Factor, f, assuming completely turbulent flow [f = 1.14 + 2 log10(D/e)-2] | ||||||||||||
8 | Inputs | Calculations | |||||||||||
9 | |||||||||||||
10 | Pipe Diameter, | D | 1600 | mm | Pipe Diameter, | D | 1.6000 | m | |||||
11 | |||||||||||||
12 | Pipe Roughness, | ε | 0.15 | mm | Friction Factor, | f | 0.01182 | ||||||
13 | |||||||||||||
14 | Pipe Length, | L | 66 | m | Cross-Sect. Area, | A | 2.0106 | m2 | |||||
15 | |||||||||||||
16 | Pipe Flow Rate, | Q | 3.500 | m3/s | Ave. Velocity, | V | 1.7 | m/s | |||||
17 | |||||||||||||
18 | Fluid Density, | ρ | 1000 | kg/m3 | Reynolds number, | Re | 2,142,470 | ||||||
19 | |||||||||||||
20 | Fluid Viscosity, | μ | 0.0013 | N-s/m2 | |||||||||
21 | |||||||||||||
22 | 2. Check on whether the given flow is "completely turbulent flow" | ||||||||||||
23 | (Calculate f with the transition region equation and see if differs from the one calculated above.) | ||||||||||||
24 | f = {-2*log10[((e/D)/3.7)+(2.51/(Re*(f1/2))]}-2 | ||||||||||||
25 | |||||||||||||
26 | Transition Region Friction Factor, f: | f = | 0.0127 | ||||||||||
27 | |||||||||||||
28 | Repeat calc of f using new value of f: | f = | 0.0126 | ||||||||||
29 | |||||||||||||
30 | Repeat again if necessary: | f = | 0.0126 | ||||||||||
31 | |||||||||||||
32 | |||||||||||||
33 | 3. Calculate hL and DPf, using the final value for f calculated in step 2 | ||||||||||||
34 | (hL = f(L/D)(V2/2g) and DPf = rghL) | the Darcy Weisbach equation | |||||||||||
35 | |||||||||||||
36 | Frictional Head Loss, hL | 0.081 | m | ||||||||||
37 | |||||||||||||
38 | Frictional Pressure | ||||||||||||
39 | Drop, DPf | 790 | N/m2 | ||||||||||
40 | |||||||||||||
41 | Frictional Pressure | ||||||||||||
42 | Drop, DPf | 0.79 | kN/m2 | ||||||||||
43 | |||||||||||||
44 | http://upload.wikimedia.org/wikipedia/commons/8/80/Moody_diagram.jpg | ||||||||||||
45 | |||||||||||||
46 | |||||||||||||
47 | References | ||||||||||||
48 | 1. Source for pipe roughness values - http://www.efunda.com/formulae/fluids/roughness.cfm | ||||||||||||
49 | 2. Munson, B. R., Young, D. F., & Okiishi, T. H., Fundamentals of Fluid Mechanics, 4th Ed., New York: John Wiley and Sons, Inc, 2002. | ||||||||||||
50 | 3. Darcy Weisbach equation history - http://biosystems.okstate.edu/darcy/DarcyWeisbach/Darcy-WeisbachHistory.htm | ||||||||||||
51 | |||||||||||||
52 | http://www.brighthub.com/engineering/civil/articles/84765.aspx | ||||||||||||
53 | Read more: http://www.brighthub.com/engineering/civil/articles/84765.aspx#ixzz1OK4uPCo0 | ||||||||||||