Page 211 - Shale Shakers Drilling Fluid Systems

CENTRIFUGAL PUMPS 193

TABLE 11-2. (continued)

Nom- Outside Identification Wall Inside Area Transverse Moment Weight
inal Diam. Steel Stain- Thick- Diam- of Internal Area of Pipe
Pipe less ness eter Metal Inertia
Size Iron Sched. Steel (t) (d) (a) (-•0 (/) Pounds
Pipe No. Sched. Square Square Square per
Inches Inches Size No. Inches Inches Inches Inches Feet Inches 4 foot
5S .218 23.564 16.29 436.10 3.0285 1151.6 55.37
10 10S .250 23.500 18.65 433.74 3.0121 1315.4 63.41
STD 20 .375 23.250 27.83 424.56 2.9483 1942.0 94.62
XS .500 23.000 36.91 415.48 2.8853 2549.5 125.49
30 .562 22.876 41.39 411.00 2.8542 2843.0 140.68
24 24.00 40 .688 22.624 50.31 402.07 2.7921 3421.3 171.29
60 .969 22.062 70.04 382.35 2.6552 4652.8 238.35
80 1.219 21.562 87.17 365.22 2.5362 5672.0 2%. 58
100 1.531 20.938 108.07 344.32 2.3911 6849.9 367.39
120 1.812 20.376 126.31 326.08 2.'2645 7825.0 429.39
140 2.062 19.876 142.11 310.28 2.1547 8625.0 483.12
160 2.344 19.312 159.41 292.98 2.0346 9455.9 542.13
10- .312 25.376 25.18 505.75 3.5122 2077.2 85.60
26 26.00 STD .375 25.250 30.19 500.74 3.4774 2478.4 102.63
XS 20 .500 25.000 40.06 490.87 3.4088 3257.0 136.17
10 .312 27.376 27.14 588.61 4.0876 2601.0 92.26
STD .375 27.250 32.54 583.21 4.0501 3105.1 110.64
28 28.00 XS '26 .500 27.000 43.20 572.56 3.9761 4084.8 146.85
30 .625 26.750 53.75 562.00 3.9028 5037.7 182.73
5S .250 29.500 23.37 683.49 4.7465 2585.2 79.43
10 10S .312 29.376 29.10 677.76 4.7067 3206.3 98.93
30 30.00 STD .375 29.250 34.90 671.96 4.6664 3829.4 118.65
XS 20 .500 29.000 46.34 660.52 4.5869 5042.2 157.53
30 .625 28.750 57.68 649.18 4.5082 6224.0 196.08
10 .312 31.376 31.06 773.19 5.3694 3898.9 105.59
STD .375 31.250 37.26 766.99 5.3263 4658.5 126.66
32 32.00 XS 20 .500 31.000 49.48 754.77 5.2414 6138.6 168.21
30 .625 30.750 61.60 742.64 5.1572 7583.4 209.43.
40 .688 30.624 67.68 736.57 5.1151 8298.3 230.08
10 .344 33.312 36.37 871.55 6.0524 5150.5 123.65
STD .375 33.250 39.61 868.31 6.0299 5599.3 134.67
34 34.00 XS 20 .500 33.000 52.62 855.30 5.93% 7383.5 178.89
30 .625 32.750 65.53 842.39 5.8499 9127.6 222.78
40 .688 32.624 72.00 835.92 5.8050 9991.6 244.77
10 .312 35.376 34.98 982.90 6.8257 5569.5 118.92
STD .375 35.250 41.97 975.91 6.7771 6658.9 142.68
36 36.00 XS 20 .500 35.000 55.76 962.11 6.6813 8786.2 189.57
30 .625 34.750 69.46 948.42 6.5862 10868.4 236.13
40 .750 34.500 83.06 934.82 6.4918 12906.1 282.35
l
Identification, wall thickness and weights are extracted from ANSI B36.10 and B36 19. The notations
STD, XS. and XXS indicate Standard, Extra Strong, and Double Extra Strong pipe respectively.

For a turbulent flow situation, the friction factor number of 22,000. The friction factor may be
(f) may be calculated from the equation: determined on the left side of the chart. For the
example just presented, the friction factor would
be 0.025:

Friction curves, presented in Figure 11-6, may
be used to simplify the calculations. On the left
side of the chart, locate the 6-inch, Schedule 80 The length of pipe connected to the pump must
value. Follow this value horizontally until the line now be determined. Valves, elbows, tees, and
veers upward; then follow the trend between the swages create more pressure loss, or head loss,
lines labeled "inside diameter." This trend line will than a straight pipe. The equivalent lengths of
intersect the vertical line representing a Reynolds these items are presented in Table 11-1. For