5. A 50-m duct is 0.060-m in diameter (Figure 2). Calculate the flow rate (m³/sec). Pfluid=917 kg/m³ (density of fluid). 1 Hfluid = 13.6 Pas (viscosity of fluid). TT-3.14 g=9.81 m/s² HINTS: Use Bernoulli. No unit conversion is needed. Consider the flow as laminar. Point 2 is datum level. Velocity and pressure heads at point 1 are zero (open to atm). Elevation and velocity heads at point 2 are zero (datum level and open to atm). 12 m L = 50 m 205000 Pa gage 2 Figure 2

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Chapter6: Forced Convection Over Exterior Surfaces
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Problem 6.34P
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5. A 50-m duct is 0.060-m in diameter (Figure 2). Calculate the flow rate (m³/sec).
Pfluid=917 kg/m³ (density of fluid).
1
Hfluid = 13.6 Pas (viscosity of fluid).
T-3.14
g=9.81 m/s²
HINTS:
Use Bernoulli. No unit conversion is needed.
Consider the flow as laminar.
Point 2 is datum level.
Velocity and pressure heads at point 1 are zero (open to atm).
Elevation and velocity heads at point 2 are zero (datum level and open to atm).
12 m
L = 50 m
205000 Pa
gage
2
Figure 2
Transcribed Image Text:5. A 50-m duct is 0.060-m in diameter (Figure 2). Calculate the flow rate (m³/sec). Pfluid=917 kg/m³ (density of fluid). 1 Hfluid = 13.6 Pas (viscosity of fluid). T-3.14 g=9.81 m/s² HINTS: Use Bernoulli. No unit conversion is needed. Consider the flow as laminar. Point 2 is datum level. Velocity and pressure heads at point 1 are zero (open to atm). Elevation and velocity heads at point 2 are zero (datum level and open to atm). 12 m L = 50 m 205000 Pa gage 2 Figure 2
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