Compare the lost head for water and a 30 percent ethylene glycol solution flowing at the rate of 110 gallons per minute (gpm) in a 3 in. standard (Schedule 40) commercial steel pipe 200 ft in length. The temperature of the water is 50 F.
Equation 10-6 will be used. From Table C-1 the inside diameter of 3 in. nominal diameter Schedule 40 pipe is 3.068 in. and the inside cross-sectional area for flow is 0.0513 ft². The Reynolds number is given by Eq. 10-10, and the average velocity in the pipe is
l_{f} = f \frac{L}{D} \frac{\bar{V}^{2}}{2 g} (10-6)
Re = \frac{ρ \bar{V} D}{μ} = \frac{\bar{V} D}{\text{v}} (10-10)
\bar{V} = \frac{\dot{Q}}{A} = \frac{110 gal/min}{(7.48 gal/ft³) (0.0513 ft²)} = 287 ft/min = 4.78 ft/sec
The absolute viscosity of pure water at 50 F is 1.4 centipoise, or 9.4 × 10^{-4} lbm/ (ft-sec), from Fig. 10-2b. Then
Re = \frac{62.4 (4.78) (3.068/12)}{9.4 × 10^{-4}} = 8.1 × 10^{-4}
From Fig. 10-1 the absolute roughness e is 0.00015 for commercial steel pipe. The relative roughness is then
e/D = 12(0.00015/3.068) = 0.00058
The flow is in the transition zone, and the friction factor f is 0.021 from Fig. 10-1. The lost head for pure water is then computed using Eq. 10-6
l_{fw} = 0.021 × \frac{200}{3.068/12} × \frac{(4.78)²}{2(32.2)} = 5.83 ft of water
The absolute viscosity of the 30 percent ethylene glycol solution is 3.1 centipoise from Fig. 10-2b, and its specific gravity is 1.042 from Fig. 10-2a. The Reynolds number for this case is
Re = \frac{1.042 (62.4) (4.78) (3.068/12)}{3.1/1490} = 3.8 × 10^{4}
and the friction factor is 0.024 from Fig. 10-1. Then
l_{fe} = 0.024 × \frac{200}{3.068/12} × \frac{(4.78)²}{2(32.2)} = 6.66 ft of E.G.S.
= 6.94 ft of water
The increase in lost head with the brine solution is
Percent increase = \frac{100 (6.94 – 5.83)}{5.83} = 19 percent
Table C-1 Steel Pipe Dimensions—English and SI Units | |||||||||
Diameter | Wall Thickness |
Inside Cross- Sectional Area |
|||||||
Nominal Pipe Size, in |
O.D. | I.D. | |||||||
Schedule. Number | in. | mm | in. | mm | in. | mm | ft² | 10^{-3} m^{2} | |
\frac{1}{4} | 40 | 0.540 | 13.7 | 0.364 | 9.25 | 0.088 | 2.23 | 0.00072 | 0.067 |
80 | 0.302 | 7.67 | 0.119 | 3.02 | 0.00050 | 0.046 | |||
\frac{3}{8} | 40 | 0.675 | 17.1 | 0.493 | 12.5 | 0.091 | 2.31 | 0.00133 | 0.124 |
80 | 0.423 | 10.7 | 0.126 | 3.20 | 0.00098 | 0.091 | |||
\frac{1}{2} | 40 | 0.840 | 21.3 | 0.622 | 15.8 | 0.109 | 2.77 | 0.00211 | 0.196 |
80 | 0.546 | 13.9 | 0.147 | 3.73 | 0.00163 | 0.151 | |||
\frac{3}{4} | 40 | 1.050 | 26.7 | 0.824 | 20.9 | 0.113 | 2.87 | 0.00371 | 0.345 |
80 | 0.742 | 18.8 | 0.154 | 3.91 | 0.00300 | 0.279 | |||
1 | 40 | 1.315 | 33.4 | 1.049 | 26.6 | 0.133 | 3.38 | 0.00600 | 0.557 |
80 | 0.957 | 24.3 | 0.179 | 4.55 | 0.00499 | 0.464 | |||
1 \frac{1}{2} | 40 | 1.900 | 48.3 | 1.610 | 40.9 | 0.145 | 3.68 | 0.01414 | 1.314 |
80 | 1.500 | 38.1 | 0.200 | 5.08 | 0.01225 | 1.138 | |||
2 | 40 | 2.375 | 60.3 | 2.067 | 52.5 | 0.154 | 3.91 | 0.02330 | 2.165 |
80 | 1.939 | 49.3 | 0.218 | 5.54 | 0.02050 | 1.905 | |||
2 \frac{1}{2} | 40 | 2.875 | 73.0 | 2.469 | 62.7 | 0.203 | 5.16 | 0.03322 | 3.086 |
80 | 2.323 | 59.0 | 0.276 | 7.01 | 0.02942 | 2.733 | |||
3 | 40 | 3.500 | 88.9 | 3.068 | 77.9 | 0.216 | 5.49 | 0.05130 | 4.766 |
80 | 2.900 | 73.7 | 0.300 | 7.62 | 0.04587 | 4.262 | |||
4 | 40 | 4.500 | 114.3 | 4.026 | 102.3 | 0.237 | 6.02 | 0.08840 | 8.213 |
80 | 3.836 | 97.2 | 0.337 | 8.56 | 0.07986 | 7.419 | |||
5 | 40 | 5.563 | 141.3 | 5.047 | 128.1 | 0.258 | 6.55 | 0.1390 | 12.91 |
80 | 4.813 | 122.3 | 0.375 | 9.53 | 0.1263 | 11.73 | |||
6 | 40 | 6.625 | 168.3 | 6.065 | 154.1 | 0.280 | 7.11 | 0.2006 | 18.64 |
80 | 5.761 | 146.3 | 0.432 | 11.0 | 0.1810 | 16.82 | |||
8 | 40 | 8.625 | 219.1 | 7.981 | 202.7 | 0.322 | 8.18 | 0.3474 | 32.28 |
80 | 7.625 | 193.7 | 0.500 | 12.7 | 0.3171 | 29.46 | |||
10 | 40 | 10.75 | 273.1 | 10.020 | 254.5 | 0.365 | 9.27 | 0.5475 | 50.86 |
80 | 9.750 | 247.7 | 0.500 | 12.7 | 0.5185 | 48.17 | |||
Source: Adapted from A.S.A. Standards B36.10 |