Air, with ρ = 0.00237 slug/ft^3 and ν = 0.000157 ft^2/s, is forced through a horizontal square 9-by 9-in duct 100 ft long at 25 ft^3/s. Find the pressure drop if ε = 0.0003 ft.
Air, with ρ = 0.00237 slug/ft^3 and ν = 0.000157 ft^2/s, is forced through a horizontal square 9-by 9-in duct 100 ft long at 25 ft^3/s. Find the pressure drop if ε = 0.0003 ft.
Compute the mean velocity and hydraulic diameter:
V = \frac{25 ft^3/s}{(0.75 ft)^2} = 44.4 ft/sD_h = \frac{4A}{\mathscr{P}} = \frac{4(81 in^2)}{36 in} = 9 in = 0.75 ft
From Table 6.4, for b/a = 1.0, the effective diameter is
D_{eff} = \frac{64}{56.91} D_h = 0.843 ftwhence Re_{eff} = \frac{VD_{eff}}{\nu} = \frac{44.4(0.843)}{0.000157} = 239,000
\frac{\epsilon}{D_{eff}} = \frac{0.0003}{0.843} = 0.000356Table 6.4 Laminar Friction Constants f Re for Rectangular and Triangular Ducts |
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Rectangular
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Isosceles triangle![]() |
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b/a | f_{Re_{D_h}} | θ, deg | f_{Re_{D_h}} |
0.0 | 96.00 | 0 | 48.0 |
0.05 | 89.91 | 10 | 51.6 |
0.1 | 84.68 | 20 | 52.9 |
0.125 | 82.34 | 30 | 53.3 |
0.167 | 78.81 | 40 | 52.9 |
0.25 | 72.93 | 50 | 52.0 |
0.4 | 65.47 | 60 | 51.1 |
0.5 | 62.19 | 70 | 49.5 |
0.75 | 57.89 | 80 | 48.3 |
1.0 | 56.91 | 90 | 48.0 |
From the Moody chart, read f = 0.0177. Then the pressure drop is
\Delta p = \rho g h_f = \rho g \left(f\frac{L}{D_h}\frac{V^2}{2g}\right) = 0.00237(32.2) \left[0.0177\frac{100}{0.75}\frac{44.4^2}{2(32.2)}\right]or Δp = 5.5 lbf/ft^2
Pressure drop in air ducts is usually small because of the low density.