If laminar flow is induced at the surface of a disk due to rotation about its axis, the local convection coefficient is known to be a constant, h = C , independent of radius. Consider conditions for which a disk of radius r o = 100 mm is rotating in stagnant air at T ∞ = 20 ° C and a value of C = 20 W/m 2 ⋅ K is maintained. If an embedded electric heater maintains a surface temperature of T s = 50 ° C, what is the local heat flux at the top surface of the disk? What is the total electric power requirement? What can you say about the nature of boundary layer development on the disk?
If laminar flow is induced at the surface of a disk due to rotation about its axis, the local convection coefficient is known to be a constant, h = C , independent of radius. Consider conditions for which a disk of radius r o = 100 mm is rotating in stagnant air at T ∞ = 20 ° C and a value of C = 20 W/m 2 ⋅ K is maintained. If an embedded electric heater maintains a surface temperature of T s = 50 ° C, what is the local heat flux at the top surface of the disk? What is the total electric power requirement? What can you say about the nature of boundary layer development on the disk?
Solution Summary: The author calculates the local heat flux and total electric power requirement of the disk.
If laminar flow is induced at the surface of a disk due to rotation about its axis, the local convection coefficient is known to be a constant,
h
=
C
,
independent of radius. Consider conditions for which a disk of radius
r
o
=
100
mm
is rotating in stagnant air at
T
∞
=
20
°
C
and a value of
C
=
20
W/m
2
⋅
K
is maintained.
If an embedded electric heater maintains a surface temperature of
T
s
=
50
°
C,
what is the local heat flux at the top surface of the disk? What is the total electric power requirement? What can you say about the nature of boundary layer development on the disk?
Steam at 200 psia and 500°F flows at 100 fps in a 4 inches pipe inside diameter. What is the surface coefficient on the inside of the pipe if the thermal conductivity is 0.255 Btu-in/ft2-hr-°R, Cp = 0.559 Btu/lbs-°R, absolute viscousity is 1.2 x 10-5 lbs/ft-sec and specific volume is 2.725 ft3/lbs.
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