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8.3.1: Computing Losses Due to Friction

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    Several equations have been developed to calculate the friction loss in pipelines. A widely used empirical method is the Hazen-Williams Equation. The Hazen-Williams Equation for circular pipes is given by:

    \(h_f = 1054 F\left(\dfrac{Q}{C}\right)^{1.852}\left(\dfrac{1}{d^{4.866}}\right) \) (8.11a)

    or

    \(P_f = 456 F\left(\dfrac{Q}{C}\right)^{1.852}\left(\dfrac{1}{d^{4.866}}\right) \) (8.11b)

    where: hf = friction loss, ft of head/100 ft of pipe,

    Pf = friction loss, psi/100 ft of pipe,

    Q = flow rate (gpm),

    d = inside diameter of the pipe (in),

    C = roughness coefficient, and

    F = outlet factor.

    Friction loss increases as flow velocity increases. This fact is incorporated, but somewhat hidden in Equation 8.11. Equation 8.11 is applicable to essentially all pipelines used in surface and sprinkler irrigation. However, for small diameter pipelines, such as laterals that are used in microirrigation, a more appropriate equation is the Darcy-Weisbach equation which will be applied in Chapter 14. The roughness coefficient, C, accounts for the roughness of the wall of the pipe. Representative C values for different types of pipe materials are summarized in Table 8.1. As the roughness of the pipe wall increases C decreases. Of the materials in Table 8.1, steel pipe is the roughest material while PVC is the smoothest. Table 8.2a and b contain pressure losses due to friction for selected pipe materials and diameters based on the Hazen-Williams equation.

    Table 8.1. C values for representative types of pipes.
    Material C
    Aluminum pipe with couplers 120
    Aluminum pipe with gates 110
    Cement asbestos pipe 140
    Galvanized steel pipe 140
    Standard steel pipe 100
    PVC 150
    PVC pipe with gates 130
    Table 8.2a. Pressure loss due to friction for smaller diameter pipes (Hazen-Williams Formula). Bold and italicized font represents region where velocity exceeds 5 ft/s.
    Q (gpm) Pressure Loss Due to Friction (psi/100ft)
    Aluminum Sprinkler Pipe, 150 psi Rating, C=120 PVC IPS Class 160, C=150
    Nominal Diameter=2 in. Nominal Diameter=3 in. Nominal Diameter=4 in. Nominal Diameter=6 in. Nominal Diameter=2 in. Nominal Diameter=2.5 in. Nominal Diameter=3 in. Nominal Diameter=4 in. Nominal Diameter=6 in.
    Inside Diameter= 5.898 in. Inside Diameter= 5.898 in. Inside Diameter= 5.898 in. Inside Diameter= 5.898 in. Inside Diameter= 5.898 in. Inside Diameter= 5.898 in. Inside Diameter= 5.898 in. Inside Diameter= 5.898 in. Inside Diameter= 5.898 in.
    2 0.01                
    4 0.04       0.01        
    6 0.08       0.03        
    8 0.13       0.04        
    10 0.20 0.03     0.07 0.03      
    15 0.43 0.05     0.14 0.06      
    20 0.73 0.09     0.24 0.09 0.04    
    25 1.10 0.14     0.36 0.14 0.06    
    30 1.54 0.20     0.51 0.20 0.08    
    35 2.05 0.26     0.68 0.27 0.10    
    40 2.63 0.34     0.87 0.34 0.13    
    45 3.27 0.42     1.08 0.42 0.16    
    50 3.97 0.51 0.12   1.31 0.52 0.20 0.06  
    55 4.74 0.61 0.14   1.56 0.62 0.24 0.07  
    60 5.57 0.71 0.17   1.83 0.72 0.28 0.08  
    65 6.46 0.83 0.20   2.13 0.84 0.32 0.10  
    70 7.41 0.95 0.22   2.44 0.96 0.37 0.11  
    75 8.42 1.08 0.25   2.77 1.09 0.42 0.12  
    80 9.49 1.21 0.29   3.12 1.23 0.47 0.14  
    85 10.61 1.36 0.32   3.49 1.38 0.53 0.16 0.02
    90 11.80 1.51 0.36 0.05 3.88 1.53 0.59 0.17 0.03
    100 14.34 1.83 0.43 0.06 4.72 1.86 0.72 0.21 0.03

    110

    17.11 2.19 0.52 0.07 5.63 2.22 0.86 0.25 0.04
    120 20.10 2.57 0.61 0.08 6.62 2.61 1.01 0.30 0.04
    140 26.74 3.42 0.81 0.11 8.80 3.47 1.34 0.40 0.06
    150   3.88 0.92 0.12   3.95 1.52 0.45 0.07
    160   4.38 1.03 0.14   4.45 1.71 0.51 0.08
    170   4.90 1.16 0.16   4.98 1.92 0.57 0.09
    180   5.44 1.29 0.17   5.53 2.13 0.63 0.10
    190   6.02 1.42 0.19   6.11 2.36 0.70 0.11
    200   6.61 1.56 0.21   6.72 2.59 0.76 0.12
    220     1.87 0.25     3.09 0.91 0.14
    240     2.19 0.30     3.63 1.07 0.16
    260     2.54 0.34     4.21 1.24 0.19
    280     2.92 0.39     4.83 1.43 0.22
    300     3.32 0.45     5.49 1.62 0.24
    320     3.74 0.51     6.18 1.83 0.28
    340     4.18 0.57       2.04 0.31
    360     4.65 0.63       2.27 0.34
    380     5.14 0.69       2.51 0.38
    400     5.65 0.76       2.76 0.42
    420     6.18 0.84       3.02 0.46
    440     6.74 0.91       3.29 0.50
    460       0.99       3.58 0.54
    480       1.07         0.58
    500       1.15         0.63
    550       1.38         0.75
    600       1.62         0.88
    650       1.88         1.03
    700       2.15         1.18
    750       2.45         1.34
    800       2.76         1.51
    Table 8.2b. Pressure loss due to friction for larger diameter pipes (Hazen-Williams Formula). Bold and italicized font represents region where velocity exceeds 5 ft/s.
    Q (gpm) Pressure Loss Due to Friction (psi/100ft)
    Aluminum Gated Pipe, 0.051 Wall, C=110 PVC IPS Class 125, C=150
    Nominal Diameter=6 in. Nominal Diameter=8 in. Nominal Diameter=10 in. Nominal Diameter=6 in. Nominal Diameter=8.5 in. Nominal Diameter=10 in. Nominal Diameter=12 in.
    Inside Diameter= 5.898 in. Inside Diameter= 7.898 in. Inside Diameter= 9.898 in. Inside Diameter= 5.766 in. Inside Diameter= 7.658 in. Inside Diameter= 9.572 in. Inside Diameter= 11.486 in.
    240 0.34            
    260 0.40     0.25      
    280 0.46     0.29      
    300 0.52     0.33      
    320 0.59 0.14   0.37      
    340 0.66 0.16   0.41      
    360 0.73 0.18   0.46      
    380 0.81 0.19   0.51 0.13    
    400 0.89 0.21   0.56 0.14    
    420 0.97 0.23   0.61 0.15 0.05  
    440 1.06 0.26 0.09 0.66 0.17 0.06  
    460 1.15 0.28 0.09 0.72 0.18 0.06  
    480 1.24 0.30 0.10 0.78 0.20 0.07  
    500 1.34 0.32 0.11 0.84 0.21 0.07  
    550 1.60 0.39 0.13 1.01 0.25 0.09  
    600 1.88 0.45 0.15 1.18 0.30 0.10 0.04
    650 2.18 0.53 0.18 1.37 0.34 0.12 0.05
    700 2.50 0.60 0.20 1.57 0.39 0.13 0.05
    750 2.84 0.69 0.23 1.79 0.45 0.15 0.06
    800 3.20 0.77 0.26 2.01 0.51 0.17 0.07
    850 3.58 0.86 0.29 2.25 0.57 0.19 0.08
    900 3.98 0.96 0.32 2.50 0.63 0.21 0.09
    950 4.40 1.06 0.35 2.77 0.70 0.23 0.10
    1000 4.84 1.17 0.39 3.04 0.76 0.26 0.11
    1050 5.30 1.28 0.43 3.33 0.84 0.28 0.12
    1100 5.77 1.39 0.46 3.63 0.91 0.31 0.13
    1150 6.27 1.51 0.50 3.94 0.99 0.33 0.14
    1200 6.78 1.64 0.55 4.26 1.07 0.36 0.15
    1250   1.77 0.59   1.16 0.39 0.16
    1300   1.90 0.63   1.24 0.42 0.17
    1350   2.04 0.68   1.33 0.45 0.19
    1400   2.18 0.73   1.43 0.48 0.20
    1450   2.33 0.78   1.52 0.51 0.21
    1500   2.48 0.83   1.62 0.55 0.23
    1550     0.88     0.58 0.24
    1600     0.93     0.62 0.25
    1650     0.99     0.65 0.27
    1700     1.04     0.69 0.28
    1750     1.10     0.73 0.30
    1800     1.16     0.77 0.32
    1850     1.22     0.81 0.33
    1900     1.28     0.85 0.35
    1950     1.34     0.89 0.37
    2000     1.41     0.93 0.38
    2050             0.40
    2100             0.42
    2150             0.44
    2200             0.46
    Table 8.3. Multiple outlet factors for laterals with equally spread outlets of the same discharge (first outlet one full spacing from inlet to pipe). For center pivots see footnote.*
    No. of Outlets F
    1 1.0
    2 0.634
    3 0.528
    4 0.480
    5 0.451
    6 0.433
    7 0.419
    8 0.410
    9 0.402
    10 0.396
    11 0.392
    12 0.388
    13 0.384
    14 0.381
    15 0.379
    16 0.377
    17 0.376
    18 0.373
    19 0.372
    20 0.370
    22 0.368
    24 0.366
    26 0.364
    28 0.363
    30 0.362
    35 0.359
    40 0.357
    50 0.355
    100 0.350
    >100 0.345

    * F = 0.54 for center pivots without end guns

    F = 0.56 for center pivots with end guns

    Example 8.4

    A four-inch aluminum sprinkler lateral is 1280 feet long. Sprinklers are spaced at 40-foot intervals. The lateral goes up (rises) 12 feet in elevation along its length. Each sprinkler on the lateral discharges 5 gpm.

    Given: L = 1280 ft

    sprinkler spacing = 40 ft

    rise = 12 ft q = 5 gpm

    q = 5 gpm

    Find: Pressure loss due to friction in the lateral in psi. If the inlet pressure to the lateral is 60 psi, what is the pressure at the downstream end of the lateral? Ignore minor losses.

    Solution:

    There are 33 sprinklers on the lateral (1280/40).

    The inlet flow rate is then 165 gpm (i.e., 5 gpm x 33).

    From Table 8.3, the multiple outlet factor is 0.36.

    Interpolating from Table 8.2a, the pressure loss due to friction is 1.1 psi/100 ft.

    \(P_f=F \times (P_f/100 \text{ ft}) \times L \)

    \(P_f= \dfrac{0.36 \times 1.1 \times 1280\text{ ft}}{100 \text{ ft}} = 5.1 \text{ psi}\)

    The pressure at the downstream end of the lateral can be determined using the concepts shown in Figure 8.4.

    \(P_2=P_1 - P_f - P_m - 0.433 \times Rise \)

    \(P_2=60 - 5.1 - 0.433 \times 12 = 49.7 \text{ psi} \)

    A pipeline with outlets, such as a lateral where water is removed by sprinklers, gates, or emitters, has a lower friction loss than a conveyance pipe because the velocity decreases with distance along the pipe. To correct for the effect of the outlets a multiple outlet factor F is used. F = 1.0 for a pipeline without outlets. For laterals with constant spaced outlets, and nearly the same discharge per outlet, use Table 8.3. With center pivots, sprinkler discharge increases with distance from the pivot point. Outlet factors for pivots are given at the bottom of Table 8.3.


    8.3.1: Computing Losses Due to Friction is shared under a CC BY-NC-ND 4.0 license and was authored, remixed, and/or curated by LibreTexts.