Consider two very large parallel plates. The bottom plate is warmer than the top plate, which is held at a constant temperature of T 1 = 330 K . The plates are separated by L = 0.1 m , and the gap between the two surfaces is tilled with air at atmospheric pressure. The heat flux from the bottom plate is q ″ = 250 W/m 2 . (a) Determine the temperature of the bottom plate and the ratio of the convective to radiative heat fluxes for ε 1 = ε 2 = 0.5 . Evaluate air properties at T = 350 K . (b) Repeat part (a) for ε 1 = ε 2 = 0.25 and 0.75.
Consider two very large parallel plates. The bottom plate is warmer than the top plate, which is held at a constant temperature of T 1 = 330 K . The plates are separated by L = 0.1 m , and the gap between the two surfaces is tilled with air at atmospheric pressure. The heat flux from the bottom plate is q ″ = 250 W/m 2 . (a) Determine the temperature of the bottom plate and the ratio of the convective to radiative heat fluxes for ε 1 = ε 2 = 0.5 . Evaluate air properties at T = 350 K . (b) Repeat part (a) for ε 1 = ε 2 = 0.25 and 0.75.
Solution Summary: The author explains the ratio of convection and radiation heat fluxes and the temperature of the bottom plate. The net rate of heat transfer per unit length is given by q=hpi D_
Consider two very large parallel plates. The bottom plate is warmer than the top plate, which is held at a constant temperature of
T
1
=
330
K
. The plates are separated by
L
=
0.1
m
, and the gap between the two surfaces is tilled with air at atmospheric pressure. The heat flux from the bottom plate is
q
″
=
250
W/m
2
. (a) Determine the temperature of the bottom plate and the ratio of the convective to radiative heat fluxes for
ε
1
=
ε
2
=
0.5
. Evaluate air properties at
T
=
350
K
. (b) Repeat part (a) for
ε
1
=
ε
2
=
0.25
and 0.75.
A furnace is shaped like a 1-m-diameter and 1-m-long vertical cylinder. The base surface has an emissivity of 0.7 and is maintained at a uniform
temperature of 525 K. The side surface has an emissivity of 0.3 and is maintained at a uniform temperature of 600 K. The top surface has an emissivity
of 0.5 and is maintained at a uniform temperature of 450 K. If Fbase-top=0.62; Fside-base=0.31, determine the net radiation heat transfer FROM the side
surface to the top surface (W).
O a. -1986
O b. -1651
O C.
-999
O d.
1986.
O e.
1651
O f. 999
EX3
Two coaxial cylinders of diameters Di = 0.10 m and D: = 0.30 m and emissivities 1 =0.7 and 2 = 0.4
are maintained at uniforn temperatures of T1 = 750 K and T2 = 500 K. respectively. Now a coaxial
radiation shield of diameter D; = 0.20 m and emissivity 3 = 0.2 is placed between the two cylinders.
Determine the net rate of radiation heat transfer berween the two cylinders per unit length of the
cylinders and compare the result with that without the shield.
Please handwriting ok
Part7. A spherical ball with a diameter of 10 cm has an outer surface that is maintained at a temperature of 200°C. It is suspended in the middle of a room that has an average temperature of 20°C. If the surface emissivity is 0.8, determine the rate of radiative heat transfer from the ball to the room in W. (Choose the nearest value) A. 2.3 W B. 4.5 W C. 19.4 W D. 60.8 W
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