Holooly Plus Logo

Question 10.1: Compare the lost head for water and a 30 percent ethylene gl......

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.

Step-by-Step
The 'Blue Check Mark' means that this solution was answered by an expert.
Learn more on how do we answer questions.

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
10.1a
10.2a
10.2b

Related Answered Questions

Question: 10.7

Verified Answer:

Equation 10-30 will yield the desired result: [lat...