Atmospheric air enters a 1 0 − m -long. 15 0 − mm -diameter uninsulated heating duct at 6 0 ° C and 0.0 4 kg / s . The duct surface temperature is approximately constant at T s = 15 °C. (a) What are the outlet air temperature, the heat rate q . and pressure drop Δ p for these conditions? (b) To illustrate the tradeoff between heat transfer rate and pressure drop considerations, calculate q and Δ p for diameters in the range from 0.1 to 0.2 m. In your analysis, maintain the total surface area, A s = π D L , at the value computed for pan (a). Plot q. p. and L as a function of the duct diameter.
Atmospheric air enters a 1 0 − m -long. 15 0 − mm -diameter uninsulated heating duct at 6 0 ° C and 0.0 4 kg / s . The duct surface temperature is approximately constant at T s = 15 °C. (a) What are the outlet air temperature, the heat rate q . and pressure drop Δ p for these conditions? (b) To illustrate the tradeoff between heat transfer rate and pressure drop considerations, calculate q and Δ p for diameters in the range from 0.1 to 0.2 m. In your analysis, maintain the total surface area, A s = π D L , at the value computed for pan (a). Plot q. p. and L as a function of the duct diameter.
Solution Summary: The author calculates Remold's number for the type of flow as follows: Mass flow rate is stackreldotm,i=60°C.
Atmospheric air enters a
1
0
−
m
-long.
15
0
−
mm
-diameter uninsulated heating duct at
6
0
°
C
and
0.0
4 kg
/
s
. The duct surface temperature is approximately constant at
T
s
=
15
°C.
(a) What are the outlet air temperature, the heat rate q. and pressure drop
Δ
p
for these conditions?
(b) To illustrate the tradeoff between heat transfer rate and pressure drop considerations, calculate q and
Δ
p
for diameters in the range from 0.1 to 0.2 m. In your analysis, maintain the total surface area,
A
s
=
π
D
L
, at the value computed for pan (a). Plot q. p. and L as a function of the duct diameter.
. Oil enters a 1.25-cm diameter,3-m long tube at 38°C. The tube wall is maintained at 66°C, and
flow velocity is 0.3 m/s. What is the total heat transfer to the oil and oil exit temperature? Assume
an exit temperature of 50°C.
Temperature (°C)
p(kg/m³)
u (kg/m sec)
Cp J/hg °C)
k(W/m °C)
0.210
0.0725
0.0320
40
0.144
867.05
864.04
1964
60
2047
0.140
80
852.02
2131
0.138
1. Experimental analysis was carried out about turbulent convective heat transfer in trapezoidal cross-sectioned duct.Average Nusselt numbers and Reynolds numbers were determined for each experiment and the following data set have beenobtained from this investigation. Find an engineering correlation between the average Nusselt number and Reynolds numberin the form ofNu = aReb
Choose the right answer
1. The mean Nusselt number for fully developed laminar flow in a circular tube under a
constant heat flux
a. depends on Reynolds number
b. depends on Prandtl number
c. is constant
2. The value of Prandtl number for air is about
а. 0.1
b. О.3
с. 0.7
3. In natural convection heat transfer, the Nusselt number is a function of
a. Re and Pr
b. Re and Gr
c. Grand Pr
4. A fluid is flowing along a plate having a high uniform wall temperature. The heat
transfer along the length
a. decreases
b. remain constant
c. increases
5. For fully developed laminar flow and heat transfer in a heated long circular tube, if the
flow velocity is doubled and the tube diameter is halved, the heat transfer coefficient will
be
a. four times of the original value
before
b. half of the original value
C. same as
d. double of the original value
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